Optimization of Hydride Fueled Pressurized Water Reactor Cores by Carter Alexander Shuffler B.S Mechanical Engineering UNIVERSITY OF VIRGINIA, 2002 SUBMITTED TO THE DEPARTMENT OF NUCLEAR ENGINEERING IN PARTIAL FULLFILLMENT OF THE REQUIREMENTS FOR THE DEGREE OF MASTER OF SCIENCE IN NUCLEAR ENGINEERING AT THE MASSACHUSETTS INSTITUTE OF TECHNOLOGY SEPTEMBER 2004 (©2004 Massachusetts Institute of Technology. All rights reserved. Signature of Author: ! ! Department of Nuclear Engineering August 25, 2004 Certified By:_ II. , _ X /7 .- /I - Neil E. Todreas KEPCO Professor of Nuclear Engineering, Professor of Mechanical Engineering Read By:. A - Thesis Supervisor I 2 j Pavel Hejzlar Principal Research Scientist l Thesis Reader ? Accepted By: MASSACHUSE.ITS INSIIT1" OF TECHNOLOGY IOCT 112005 LIBRARIES Jeffrey A. Coderre Chairman, Department Committee on Graduate Students ARCHIVES 2 Optimization of Hydride Fueled Pressurized Water Reactor Cores By Carter Alexander Shuffler Submitted to the Department of Nuclear Engineering on August 25, 2004 in partial fulfillment of the requirements for the degree of Master of Science in Nuclear Engineering Abstract This thesis contributes to the Hydride Fuels Project, a collaborative effort between UC Berkeley and MIT aimed at investigating the potential benefits of hydride fuel use in light water reactors (LWRs). This pursuit involves implementing an appropriate methodology for design and optimization of hydride and oxide fueled cores. Core design is accomplished for a range of geometries via steady-state and transient thermal hydraulic analyses, which yield the maximum power, and fuel performance and neutronics studies, which provide the achievable discharge burnup. The final optimization integrates the outputs from these separate studies into an economics model to identify geometries offering the lowest cost of electricity, and provide a fair basis for comparing the performance of hydride and oxide fuels. Considerable work has already been accomplished on the project; this thesis builds on this previous work. More specifically, it focuses on the steady-state thermal hydraulic and economic analyses for pressurized water reactor (PWR) cores utilizing UZrH1.6 and UO2. A previous MIT study established the steady-state thermal hydraulic design methodology for determining maximum power from square array PWR core designs. The analysis was not performed for hexagonal arrays under the assumption that the maximum achievable powers for both configurations are the same for matching rod diameters and H/HM ratios. This assumption is examined and verified in this work by comparing the thermal hydraulic performance of a single hexagonal core with its equivalent square counterpart. In lieu of a detailed vibrations analysis, the steady-state thermal hydraulic analysis imposed a single design limit on the axial flow velocity. The wide range of core geometries considered and the large power increases reported by the study makes it prudent to refine this single limit approach. This work accomplishes this by developing and incorporating additional design limits into the thermal hydraulic analysis to prevent excessive rod vibration and wear. The vibrations and wear mechanisms considered are: vortex-induced vibration, fluid-elastic instability, turbulence-induced vibration, fretting wear, and sliding wear. Concomitantly with this work, students at UC Berkeley and MIT have undertaken the neutronics, fuel performance, and transient thermal hydraulic studies. With these results, and the output from the steady-state thermal hydraulic analysis with vibrations and wear imposed design limits, an economics model is employed to determine the optimal geometries for incorporation into existing PWRs. The model also provides a basis for comparing the performance of UZrH,1 6 to UO2 for a range of core geometries. Though this analysis focuses only on these fuels, the methodology can easily be extended to additional hydride and oxide fuel types, and will be in the future. Results presented herein do not show significant cost savings for UZrH1. 6, primarily because the power and energy generation per core loading for both fuels are similar. Furthermore, the most economic geometries typically do not occur where power increases are reported by the thermal hydraulics. As a final note, the economic results in this report require revision to account for recent changes in the fuel performance analysis methodology. The changes, however, are not expected to influence the overall conclusion that UZrH1.6 does not outperform UO2 economically. Thesis Supervisor: Neil E. Todreas Title: KEPCO Professor of Nuclear Engineering, Professor of Mechanical Engineering Thesis Reader: Title: Pavel Hejzlar Principal Research Scientist 3 Acknowledgements I'd like to thank Professor Todreas for his guidance and support throughout this thesis. It has been a pleasure working with him this year. The degree of interest he expresses in his students on both a personal and academic level is unique among college faculty. I'd also like to thank Professor Greenspan for his countless suggestions for improving my analysis, and his thoughtful patience in review of my work. Several students provided great assistance at various phases of the project. Without their help I can confidently say this work would not have been possible. These students are Jon Malen, Stu Blair, and Antonino Romano. Finally, I'd like to thank those closest to me: my parents, Jason and Liz, and of course Daniela. Your love and support is tremendous, and I'm looking forward to spending more time with all of you soon. 4 Table of Contents Abstract . ......................................................................................................... 3 Acknowledgements........................................................................................ 4 Table of Figures............................................................................................. 8 List of Tables ............................................................................................... 1. Introduction .......................................................................................... 1.1 1.2 1.3 12 13 Overview of the Hydride Fuels Project ............................................................ 13 Design Optimization Methodology................................................................... 14 Scope of Work and Contribution to the Hydride Fuels Project ........................ 18 2. Steady-State Thermal Hydraulic Design of Square and Hexagonal Array PW R Cores ....................................................... 20 2.1 Parametric Study Overview ................................................................ 20 2.1.1 Reference Core Parameters . . .............................................................. 21 2.1.2 Design Limits 2.1.2.1 2.1.2.2 2.1.2.3 2.1.2.4 2.1.3 ................................................................ 22 MDNBR ........................................................... 23 Pressure Drop ................................................................ 24 Fuel Temperature ........ 24 Axial Flow Velocity ................................................................25 MATLAB/V IPRE Interface ..................................................................... 26 2.2 Results of the Steady-State Maximum Power Analysis ................................... 27 2.3 The Equivalence of Square and Hexagonal Array Geometries ........................ 33 2.3.1 Geometric Relationships for Square and Hexagonal Arrays .................... 33 2.3.1.1 Conversion Between Hydrogen/Heavy Metal and Pitch/Diameter Ratio ........................... ................................................................. 33 2.3.1.2 Relationship Between Square and Hexagonal Array Sub-Channels .... 38 2.3.2 Full Core Hexagonal Array VIPRE Model............................................... 40 2.3.2.1 Rod and Assembly Layout Within the Core ......................................... 41 2.3.3 Comparison of Maximum Power Predictions from Square and Hexagonal Arrays........................................................................................................ 44 3. Vibrations Analysis for Hydride and Oxide Fueled PWRs ............. 47 3.1 Introduction ............................................................... 47 3.2 W ork Scope....................................................................................................... 47 3.2.1 Goals of the Vibrations Analysis. ............................................................. 47 3.2.2 Flow-Induced Vibration Mechanisms - Overview ................................... 48 3.2.3 Methodology . ................. ............................................. 3.3 Assumptions ...................................................................................................... 50 50 3.3.1 Vibrations Analysis in the Nuclear Environment ..................................... 50 3.3.2 Key Assumptions ...................................................................................... 51 3.4 Vibration and W ear Mechanisms............................................................... 53 3.4.1 Dynamic Parameters ................................................................................. 53 3.4.1.1 Nomenclature ........................................................................................ 53 3.4.1.2 3.4.1.3 Linear Mass............................................................... 53 Moment of Inertia ........................................ ......................................... 54 S 3.4.1.4 3.4.1.5 3.4.1.6 3.4.2 Natural Frequency and Mode Shape .. ............ ....................................... 54 Damping Ratio ....................................................... 54 Generation and Distribution of Axial and Cross-flow Velocities......... 55 Vortex-Induced Vibration ........................................ ............................ 59 3.4.2.1 Vortex-Shedding Margin and Design Limit ......................................... 59 3.4.3 Fluid-Elastic Instability............................................................................. 62 3.4.3.1 Fluid-Elastic Instability Margin and Design Limits ............................. 62 3.4.4 Turbulence-Induced Vibration....................................................... 63 3.4.4.1 Turbulence-Induced Vibration in Cross-flow ....................................... 64 3.4.4.2 Turbulence-Induced Vibration in Axial Flow....................................... 66 3.4.4.3 Turbulence-Induced Vibration Response ............................................. 66 3.4.5 Wear Due to Flow-Induced Vibration ...................................................... 67 3.4.5.1 Fretting Wear Performance and Design Limits .................................... 68 3.4.5.2 Sliding Wear Performance and Design Limits .................................... 70 3.5 Summary of Constrained Parameters and Design Limits ........................ 71 3.6 Results of the Maximum Achievable Power Analysis With Vibrations-Imposed Design Limits for Square Arrays ......................................... 72 3.6.1 Results at 60 psia for UZrH.6................................................................... 72 3.6.2 3.6.3 Results at 60 psia for U0 2......................................................................... Comparison Between UZrH1. 6 and UO2 at 60 psia ................................... 3.6.4 Results at 29 psia for UZrH.6 ................................................................... 82 3.6.5 3.6.6 Results at 29 psia for U0 2......................................................................... Comparison Between UZrH 1. 6 and UO2 at 29 psia ................................... 3.6.7 Summary of Maximum Power Results With Vibrations and Wear Imposed Design Limits............................................................................................ 91 Extension of Vibrations Results to Hexagonal Arrays ............................. 93 3.6.8 76 80 86 90 4. Economics Analysis of Hydride and Oxide Fueled PWRs ............... 96 4.1 Introduction ....................................................................................................... 96 4.2 Work Scope....................................................................................................... 96 4.2.1 Goals of the Economics Analysis ............................................................. 96 4.2.2 Methodology ........................................... ......................... 97 4.2.2.1 Lifetime Levelized Cost Method .......................................................... 98 4.3 4.4 Assumptions ....................................................... Inputs ....................................................... 100 102 4.4.1 Maximum Power....................................................... 102 4.4.2 Fuel Burnup ....................................................... 105 4.4.2.1 Neutronics ........................................................................................... 106 4.4.2.2 Fuel Performance ................................................................................ 108 4.4.3 Economic Parameters....................................................... 114 4.4.3.1 Fuel Cycle Unit Costs ...................................... ................. 114 4.4.3.2 Operations and Maintenance Unit Costs .............................. 117 4.4.3.3 Capital Costs ....................................................................................... 118 4.4.3.4 Plant Operating Parameters ....................................................... 120 4.5 Economics Analysis ........................................................................................ 125 4.5.1 Fuel Cycle Costs ..................................................................................... 125 4.5.1.1 The Nuclear Fuel Cycle ........................................ 125 6 4.5.1.2 4.5.1.3 4.5.1.4 4.5.2 Recurring Cash Flows and the Fuel Cycle .......................................... Cash Flows for the First Operating Cycle ........................................... 126 127 Lifetime Levelized Unit Fuel Cycle Cost ........................................... 134 Operations and Maintenance Costs ........................................................ 134 4.5.2.1 Annualizing O & M Cash Flows ........................................................ 135 4.5.2.2 Lifetime Levelized Unit 0 & M Cost................................................. 137 4.5.3 Capital Costs ................ . ....................................... 137 4.5.3.1 Predicting Capital Costs for PWR Backfit .......................................... 138 4.5.3.2 Lifetime Levelized Unit Capital Cost ................................................. 139 4.6 Lifetime Levelized Unit COE .............................................................. ...... 140 5. 4.6.1 Results for Major Backfit: UZrHI. 6 and UO2 at 60 psia ........................ 4.6.1.1 COE Breakdown for 12.5% UZrH .1 6 and 5% UO 2 at 60 psia ............. 4.6.3 Results for Major Backfit: UZrH 1.6 and UO2 at 29 psia ........................ 4.6.4 Results for Minor Backfit: UZrHI . 6 and UO 2 at 29 psia ........................ 140 144 154 158 Conclusions and Future Work ................................................. 161 5.1 Conclusions ..................................................................................................... 161 5.1.1 Steady-State Thermal Hydraulics for Square andHexagonal Array PWR Geom etries ...................................................... 162 5.1.2 Vibrations Analysis for Hydride and Oxide Fueled PWRs .................... 163 5.1.3 Economic Optimization ...................................................... 165 5.2 Future Work ...................................................... 168 5.2.1 Methodology ...................................................... 168 5.2.1.1l Steady-State Thermal Hydraulic Analysis ........................................ 5.2.1.2 Vibrations and Wear Analysis . ....................................... 5.2.1.3 Transient Thermal Hydraulic Analysis............................................... 5.2.1.4 Economics Analysis ........................................ 5.2.1.5 Fuel Performance and Application of FRAPCON to Hydride Fuels.. 5.2.2 New Approaches ........................................ 5.2.2.1 New Fuels ........................................ 5.2.2.2 Hexagonal Arrays and Wire Wrap ..................................... 5.2.2.3 Reference Core..................................... ... 168 169 170 170 170 171 171 172 172 Bibliography .............................................................................................. 173 AppendixA ...... AppendixB ................ 174......... ......................... ............... Appendix C ...................................... Appendix D ........................................ Appendix E ....................................... 180........ 186 199 224 7 Table of Figures Figure 1.1 Design Optimization Flow Chart ................................................................ 17 Figure 2.1 Maximum Achievable Power vs. P/D and Drodfor Square Arrays of UZrH1 .6 and UO2 at 60 psia ............................................................ 29 Figure 2.2 Rod Number, Linear Heat Rate, and Power Ratios vs. P/D and Drod for Square Arrays of UZrH .1 6 and UO2 at 60 psia ................................................................ 29 Figure 2.3 Constraining Parameters vs. P/D and Drod for Square Arrays of UZrH1 .6 and UO2 at 60 psia ................................................................ 30 Figure 2.4 Maximum Achievable Power vs. P/D and Drod for Square Arrays of UZrH1 .6 and UO2 at 29 psia ............................................................ 31 Figure 2.5 Rod Number, Linear Heat Rate, and Power Ratios vs. P/D and Drodfor Square Arrays of UZrH 1. 6 and UO2 at 29 psia ................................................................ 31 Figure 2.6 Constraining Parameters vs. P/D and Drodfor Square Arrays of UZrHl.6 and UO2 at 29 psia ................................................................... 32 Figure 2.7 H/HM Ratio vs. P/D and Drod for Square and Hexagonal Arrays of UZrH 1.6 and U 0 2................................................................ 37 Figure 2.8 Square and Hexagonal Array Unit Cells ........................................................ 39 Figure 2.9 9 Ring Hexagonal Fuel Assembly................................................................ 41 Figure 2.10 1/6th Hexagonal Core Section................................................................ 42 Figure 2.11 Channel Lumping in the 1/6th Hexagonal Core .................................... 43 Figure 2.12 1/ 6 th Section of the Hot Assembly................................................................ 44 Figure 3.1 Cross-flow Velocity Profile as a Function of Core Power ............................. 57 Figure 3.2 Cross-flow and Fundamental Mode Shape Profiles ....................................... 58 Figure 3.3 Vortex-Shedding Margin vs. Hypothetical Cross-flow Velocity at the Reference Core Geometry................................................................ 61 Figure 3.4 Maximum Achievable Power vs. P/D and Drod for Square Arrays of UZrH1.6 at 60 psia with Vibrations and Wear Imposed Design Limits .................................. 73 Figure 3.5 Rod Number, Linear Heat Rate, and Power Ratios vs. P/D and Drod for Square Arrays of UZrHl.6 at 60 psia with Vibrations and Wear Imposed Design Limits .... 74 Figure 3.6 Power(no vibrations) - Power(vibrations) VS. P/D and Drod for Square Arrays of UZrH1, 6 at 60 psia ................................................................ 74 Figure 3.7 Thermal Hydraulic Constraining Parameters vs. P/D and Drod for Square Arrays of UZrH1. 6 at 60 psia with Vibrations and Wear Imposed Design Limits .... 75 Figure 3.8 Vibrations and Wear Constraining Parameters vs. P/D and Drod for Square Arrays of UZrH 1.6 at 60 psia ........................................ ........................ 75 Figure 3.9 Vortex-Shedding Margins and Peak Cross-flow Velocity vs. P/D and Drod for Square Arrays of UZrH1.6 at 60 psia ............................................................ 76 Figure 3.10 Maximum Achievable Power vs. P/D and Drodfor Square Arrays of U0 2 at 60 psia with Vibrations and Wear Imposed Design Limits ...................................... 77 Figure 3.11 Rod Number, Linear Heat Rate, and Power Ratios vs. P/D and Drod for Square Arrays of U0 2 at 60 psia with Vibrations and Wear Imposed Design Limits Figure 3.12 Power(no vibrations)- Power(vibrations) vs. P/D and Drod for Square Arrays of U0 2 at 60 psia ............................................................................ 78 8 Figure 3.13 Thermal Hydraulic Constraining Parameters vs. P/D and Drod for Square Arrays of UO 2 at 60 psia with Vibrations and Wear Imposed Design Limits.......... 79 Figure 3.14 Vibrations and Wear Constraining Parameters vs. P/D and Drod for Square Arrays of U0 2 at 60 psia ................................................................. 79 Figure 3.15 Vortex-Shedding Margins and Peak Cross-flow Velocity vs. P/D and Drod for Square Arrays of UO2 at 60 psia ................................................................ 80 Figure 3.16 (Poweruo2 - PoweruzrH .6) vs. P/D and Drodfor Square Arrays at 60 psia with Vibrations and Wear Imposed Design Limits........................................................... 81 Figure 3.17 Percentage Difference in Wear Rate Limits vs. P/D and Drod for Square Arrays at 60 psia ................................................................ 81 Figure 3.18 Maximum Achievable Power vs. P/D and Drod for Square Arrays of UZrH1. 6 at 29 psia with Vibrations and Wear Imposed Design Limits .................................. 83 Figure 3.19 Rod Number, Linear Heat Rate, and Power Ratios vs. P/D and Drod for Square Arrays of UZrH 1. 6 at 29 psia with Vibrations and Wear Imposed Design Limits ................................................................ 83 Figure 3.20 Power(novibrations)- Power(vibrations) vs. P/D and Drod for Square Arrays of UZrH ,.6 at 29 psia ................................................................ 84 Figure 3.21 Thermal Hydraulic Constraining Parameters vs. P/D and Drod for Square Arrays of UZrHI. 6 at 29 psia with Vibrations and Wear Imposed Design Limits .... 84 Figure 3.22 Vibrations and Wear Constraining Parameters vs. P/D and Drod for Square Arrays of UZrH 1. 6 at 29 psia ................................................................ 85 Figure 3.23 Vortex-Shedding Margins and Peak Cross-flow Velocity vs. P/D and Drod for Square Arrays of UZrHl. 6 at 29 psia ................................................................ 85 Figure 3.24 Maximum Achievable Power vs. P/D and Drod for Square Arrays of UO2 at 29 psia with Vibrations and Wear Imposed Design Limits ...................................... 87 Figure 3.25 Rod Number, Linear Heat Rate, and Power Ratios vs. P/D and Drod for Square Arrays of U0 2 at 29 psia with Vibrations and Wear Imposed Design Limits ................................................................................................................................... 87 Figure 3.26 Power(novibrations)- Power(vibrations) vs. P/D and Drod for Square Arrays of U0 2 at 29 psia ............................................................... 88 Figure 3.27 Thermal Hydraulic Constraining Parameters vs. P/D and Drod for Square Arrays of U0 2 at 29 psia with Vibrations and Wear Imposed Design Limits.......... 88 Figure 3.28 Vibrations and Wear Constraining Parameters vs. P/D and Drodfor Square Arrays of UO 2 at 29 psia ............................................................... 89 Figure 3.29 Vortex-Shedding Margins and Peak Cross-flow Velocity vs. P/D and Drod for Square Arrays of U02 at 29 psia ............................................................... 89 Figure 3.30 (Poweruo2- PoweruzrHl.6)vs. P/D and Drodfor Square Arrays at 29 psia with Vibrations and Wear Imposed Design Limits........................................................... 90 Figure 3.31 Percentage Difference in Wear Rate Limits vs. P/D and Drod for Square Arrays at 29 psia ............................................................... 91 Figure 4.1 Maximum Achievable Power and Transient Limited Regions vs P/D and Drod for Square Arrays of UZrHl.6 and UO2 Incorporating Steady-State and Transient Design Limits at 60 psia ........................................................... 104 Figure 4.2 Maximum Achievable Power and Transient Limited Regions vs P/D and Drod for Square Arrays of UZrH,.6 and UO 2 Incorporating Steady-State and Transient Design Limits at 29 psia ........................................................... 105 9 Figure 4.3 Neutronically Achievable Burnup vs. P/D and Dro for Square Arrays of UZrH 1.6 Fuel ............................................................... 107 Figure 4.4 Neutronically Achievable Burnup vs. P/D and Drod for Square Arrays UO2 Fuel ............................................................... 107 Figure 4.5 Fuel Performance Limited Bumup vs. P/D and Drodfor Square Arrays of UZrH 1. 6 and UO2 at 60 psia ............................................................... 111 Figure 4.6 Fuel Performance Limited Burnup vs. P/D and Drod for Square Arrays of UZrH 1. 6 and UO2 at 29 psia ............................................................... 111 Figure 4.7 Maximum Achievable Burnup vs. P/D and Drod for Square Arrays of UZrH1.6 at 60 psia ........................................................... 112 Figure 4.8 Maximum Achievable Burnup vs. P/D and Drod for Square Arrays of UZrH1.6 at 29 psia ........................................................... 113 Figure 4.9 Maximum Achievable Burnup vs. P/D and Drodfor Square Arrays of U0 2 at 60 psia ..................................................................................................................... 113 Figure 4.10 Maximum Achievable Burnup vs. P/D and Drod for Square Arrays of U0 2 at 29 psia .............................................. 114 Figure 4.11 Unit Fabrication Cost and Rod Number vs. P/D and Drod for Square Arrays of UO 2 ............................................................................................. Figure 4.12 Unit Fabrication Cost and Rod Number vs. P/D and 116 Drod for Square Arrays of UZrH 1 .6............................................................................ Figure 4.13 Plant Capacity vs. Operating Length .......................................................... Figure 4.14 Figure 4.15 Figure 4.16 Figure 4.17 117 123 Refueling Outage Activities ........................................ ....................... 124 Cash Flows for Successive Operating Cycles ............................................ 127 Mass Flows for Front End Fuel Cycle Processes....................................... 128 Cash Flows for Successive Annual O & M Expenditures .......................... 136 Figure 4.18 Lifetime Levelized Unit COE vs. P/D and Drod for Square Arrays of UZrH 1.6 at 60 psia ........................................................... 142 Figure 4.19 Minimum COE and its Components vs. P/D for Square Arrays of UZrH 1. 6 at 60 psia ........................................................... 142 Figure 4.20 L,ifetime Levelized Unit COE vs. P/D and Drod for Square Arrays of UO2 at 60 psia ........................................................... 143 Figure 4.21 Minimum COE and its Components vs. P/D for Square Arrays of U02 at 60 psia ........................................................... 143 Figure 4.22 Maximum Achievable Power vs. P/D and Drodfor Square Arrays of UZrH,.6 and UO2 at 60 psia With Vibrations and Transient Limits Applied ....................... 144 Figure 4.23 COE Breakdown for Square Arrays of 12.5% UZrH 1. 6 at 60 psia ............. 148 Figure 4.24 Plant Operating Conditions for Square Arrays of 12.5% UZrH1.6 at 60 psia .................................................................................................................................. 14 9 Figure 4.25 Plant Operating Conditions for Square Arrays of 12.5% UZrH 1. 6 at 60 psia ............ ..................................................................................................................... Figure 4.26 Figure 4.27 Figure 4.28 Figure 4.29 14 9 COE Breakdown for Square Arrays of 5% UO 2 at 60 psia ........................ 150 Plant Operating Conditions for Square Arrays of U0 2 at 60 psia.............. 150 Plant Operating Conditions for Square Arrays of U0 2 at 60 psia.............. 151 COE Difference and Fuel Enrichment for Major Backfit With UZrH 1. 6 and UO 2 vs. P/D and Drod at 60 psia ............................................................... 152 Figure 4.30 Minor Backfit COE and its Components vs. P/D for UZrH 1. 6 at 60 psia... 153 10 Figure 4.31 Minor Backfit COE and its Components vs. P/D for U0 2 at 60 psia ......... 154 Figure 4.32 Lifetime Levelized Unit COE vs. P/D and Drod for Square Arrays of UZrH 1.6 at 29 psia ........................................................... 155 Figure 4.33 Minimum COE and its Components vs. P/D for Square Arrays of UZrH 1.6 at 29 psia ........................................................... 156 Figure 4.34 Lifetime Levelized Unit COE vs. P/D and Drod for Square Arrays of UO2 at 29 psia ........................................................... 156 Figure 4.35 Minimum COE and its Components vs. P/D for Square Arrays of UO2 at 29 psia ........................................................... 157 Figure 4.36 COE Difference and Fuel Enrichment for Major Backfit With UZrH 1. 6 and U0 2 vs. P/D and Drod at 29 psia .............................................................. 158 Figure 4.37 Minor Backfit COE and its Components vs. P/D for UZrH .1 6 at 29 psia... 159 Figure 4.38 Minor Backfit COE and its Components vs. P/D for UO2 at 29 psia ......... 159 Figure 5.1 Maximum Achievable Power vs. P/D and Drod for Square Arrays of UZrH 1.6 and UO2 at 60 psia and 29 psia .............................................................. 162 Figure 5.2 Maximum Achievable Power and Power Reductions vs. P/D and Drodfor Square Arrays of UZrH 1.6 at 60 and 29 psia with Vibrations and Wear Imposed Design Limits.............................................................. 164 Figure 5.3 Maximum Achievable Power and Power Reductions vs. P/D and Drod for Square Arrays of U0 2 at 60 and 29 psia with Vibrations and Wear Imposed Design Limits ........................................................... 164 Figure 5.4 Major and Minor Backfit COE vs. P/D for UZrH .1 6 and UO 2 at 29 and 60 psia ................................................................................................................................. 167. Figure 5.5 Major Backfit COE Difference vs. P/D and Drod for UZrH .1 6 and UO 2 at 60 and 29 psia ........................................................... 167 11 List of Tables Table 2.1 Fixed Parameters for the Thermal Hydraulic Analysis .................................. 22 Table 2.2 Summary of Steady-State Thermal Hydraulic Design Limits for UZrH1. 6 and U O 2 ........................................................... 22 Table 2.3 General Nomenclature for Geometric Relationships for Square and Hexagonal Arrays ............................................................... Table 2.4 Table 3.1 Table 3.2 Table 3.3 Table 3.4 Table 3.5 Table 3.6 34 Power Predictions by Full Core Square and Hexagonal VIPRE Models ........ 44 Flow-Induced Vibration Mechanisms ............................................................. 50 General Nomenclature for the Vibrations Analysis. ............................... 53 ASME Recommended Damping Ratios ......................................................... 54 Peak Cross-flow Velocities vs. Power for the Reference Geometry ............... 61 Summary of Steady-State Thermal Hydraulic Design Constraints ................. 71 Summary of Steady-State Thermal Hydraulic Results with Vibrations and W ear Lim its ............................................................... Table 4.1 Transient Analysis Summary ............................................................... 93 103 Table 4.2 Fuel Performance Limits for Maximum Burnup .......................................... 109 Table 4.3 PWR Fuel Cycle Unit Costs for U02 ............................................................. 115 Table 4.4 PWR Operations and Maintenance Unit Costs .............................................. 117 Table 4.5 Cost Estimates for Installed Nuclear Components ........................................ 120 Table 4.6 Fixed Plant Operating Parameters ............................................................... 121 Table 4.7 Mass Loss Fractions for Front End Fuel Cycle Processes ............................. 128 Table 4.8 Inlet and Outlet Mass Flow Stream Enrichments at the Enrichment Plant ... 129 Table 4.9 SWU Requirements for Different Enrichments of U0 2 and UZrH1. 6............ 130 Table 4.10 Mass Flows Through the Front End ............................................................ 132 Table 4.11 Fuel Cycle Unit Costs With Respect to the Heavy Metal Loading in the Core .................................................................................................................................. 133 Table 4.12 OECD/NEA Recommended Lead and Lag Times for Front and Back End Processes ............................................................... 133 Table 4.13 Fixed and Variable Unit 0 & M Costs ........................................................ 135 12 1. Introduction 1.1 Overview of the Hydride Fuels Project The concentration of hydrogen in hydride fuels is comparable to that of hydrogen in light water reactor (LWR) coolant. The additional moderation provided in the fuel provides an optimal neutron spectrum with a smaller water volume fraction to cool and moderate the core. The result can be either smaller core volume for new designs or higher power output for existing LWRs that convert to hydride fuels. Candidate fuels include but are not limited to: UZrH.1 6, PuZrH 1. 6, PuH 2-ThH 2, UH 2-ThH 2, UZrH 1 6-ThH 2, and PuZrH 1. 6 -ThH2. Note that fuels with thorium hydride have a higher heavy metal concentration than traditional oxide fuel. Combined with the higher power density offered by hydride fuels, they will allow achievement of higher energy generation per core loading. The expected outcome includes improvements in economics, resource utilization, proliferation resistance, safety, and waste reduction. The investigation of hydride fuels may lead to the development of LWR core designs that may have one or more of the following advantages over contemporary LWRs: · Increased power output, power density, discharge bum-up, and core lifetime; * Reduced fuel cycle, operations and maintenance, and capital costs and therefore reduced cost of electricity; · Reduced waste volume due to higher discharge burnup and partial utilization of thoriurnm; · Increased utilization of commercial and surplus weapons grade plutonium due to higher power and discharge burnup; additionally, the use of PuH2 and PuZr fuel types eliminate fertile 238U; * Improved proliferation resistance due to enhanced plutonium destruction and use of thorium; · Increased capability of LWRs to utilize thorium fuel resources; 13 * Improved LWR safety due to the large negative temperature coefficient of reactivity of hydride fuels; * Reduced heterogeneity and negative void coefficient of reactivity in BWR cores which simplifies control systems and fuel assembly design, as well as improves stability against power oscillations. 1.2 Design Optimization Methodology The Hydride Fuels Project aims to quantify the advantages of hydride fuel use by developing and implementing an appropriate methodology for optimizing LWR core designs. Two cases are considered for optimization: * Minor Backfit: Minor backfit of existing LWRs seeks to limit the plant modifications required for conversion to hydride fuel use by maintaining the existing fuel assembly and control rod configurations within the pressure vessel (i.e., maintaining the same pitch and rod number in the core). In this case, replacement of the steam generators and upgrades to the high pressure turbine will be required to accommodate higher powers; * Major Backfit: Major backfit of existing LWRs does not limit the design space. The layout of hydride fuel in the core can therefore assume any combination of lattice pitch, rod diameter, and channel shape, further referred to throughout this report as a design or geometry. Note that in addition to upgrades and modifications on the steam side of the plant, replacement of the reactor vessel head and core internals will also be necessary. The optimization is carried out by integrating the results from separate evaluations for thermal hydraulics, neutronics, and fuel performance into an economics model, which identifies designs for each backfit case offering the lowest cost of electricity. To provide a fair and consistent basis for the optimization, all analyses are carried out for both hydride and oxide fuels. 14 The participants in the study and their respective responsibilities include: (1) University of California, Berkeley, responsible for neutronics and materials compatibility; (2) MIT, responsible for thermal hydraulics, fuel performance, and economic optimization; and (3) Westinghouse, responsible for practical fuel and core design considerations. The role played by each analysis in the optimization study is briefly summarized below: * Neutronics: The neutronics analysis seeks the maximum fuel burnup that maintains the critical nuclear reaction in the core, accounting for fuel depletion. It depends on fuel type, enrichment, and geometry. It also provides the range of geometries with acceptable fuel and moderator temperature coefficients. * Fuel Performance: The fuel performance analysis seeks the maximum fuel burnup subject to design constraints that protect the integrity of the fuel pin during irradiation. Constraints are placed on: fission gas release and internal fuel pin pressure, clad strain, and clad oxidation. The fuel performance limited burnup depends on the fuel type, and the power in the core. * Thermal Hydraulics: The thermal hydraulics analysis seeks the maximum power that can be safely sustained in the core subject to steady-state and transient design limits. Steady-state limits are placed on the minimum departure from nucleate boiling ratio (MDNBR), fuel bundle pressure drop, fuel temperature, and rod vibration and wear. Transient limits are derived by consideration of the loss of flow and loss of coolant accidents, and an overpower transient. The maximum power in the core depends on fuel type and geometry. * Materials Compatibility: The materials compatibility study supports the neutronics, fuel performance, and thermal hydraulic analyses by specifying materials that are compatible for use with hydride fuels (i.e., cladding material, gap fill). 15 Economic Optimization: An economics model uses the maximum bumup and power defined by the neutronics, fuel performance, and thermal hydraulic analyses to determine the cost of electricity (COE) as a function of fuel type, enrichment, and geometry. Both hydride and oxide fuels are considered, and designs are optimized for the cases of minor and major backfit by identifying the geometries where costs are minimized, and where hydride fuel use offers potential cost savings over oxide. A simplified flow chart showing the interaction of these analyses with their respective inputs and outputs is shown in Figure 1.1. Note the feedback loop connecting maximum power and burnup to the steady-state thermal hydraulic analysis. The vibrations design limits (see Chapter 3) for the steady-state thermal hydraulic analysis depend on the operating cycle length, which in turn is a function of burnup and power. The maximum power and burnup must therefore be determined in iterative fashion. 16 Figure 1.1 Design Optimization Flow Chart Fuel Type, Enrichment, Geometry Fuel Type, Fuel Type, Geometry Geometry R / I Fuel Type, Geometry RBIB ! \ COB 17 1.3 Scope of Work and Contribution to the Hydride Fuels Project To date, considerable progress has been made on the project, and this report builds on this previous work. More specifically, it focuses on the steady-state thermal hydraulic and economic analyses for pressurized water reactor (PWR) cores. The basic methodology for evaluating the steady-state thermal hydraulic performance of square array PWR core designs was laid out by Jon Malen, a recent MIT graduate student [1]. As previously discussed, this analysis seeks the maximum achievable power for core geometries subject to design limits on MDNBR, fuel bundle pressure drop, fuel temperature, and rod vibration. Chapters 2 and 3 of this report will supplement and complete this steady-state analysis by considering hexagonal array designs, and more stringent limits on rod vibrations and wear. Concomitantly with this work, students at UC Berkeley and MIT have undertaken the neutronics, materials, fuel performance, and transient thermal hydraulic studies. Chapter 4 of this report develops an economics model to determine the optimal PWR core designs given inputs from these analyses and the completed steady-state results from Chapters 2 and 3. Results are reported for UZrH1.6 and U0 2, but the methodology can be easily extended to additional hydride and oxide fuel types. 18 19 2. Steady-State Thermal Hydraulic Design of Square and Hexagonal Array PWR Cores 2.1 Parametric Study Overview A recent MIT graduate, Jon Malen (2003), performed a parametric study to determine the steady-state maximum achievable power for square array PWR geometries with design limits placed on MDNBR, fuel bundle pressure drop, fuel temperature, and rod vibration [1]. The performance of new designs with respect to the limits was determined by the VIPRE sub-channel analysis code, which was cleverly linked to a series of student written MATLAB scripts to iteratively determine the maximum power for a user defined range of geometries. For each channel shape, the rod diameter and lattice pitch are the independent variables chosen to describe a specific geometry, and so the design space for the thermal hydraulic analysis is given with respect to rod diameter and the pitch to diameter (P/D) ratio. For square arrays, the design space is: 1.08 <p- (2.1) <1.55 6.5 < L)rod < 12.5 mm (2.2) This range is considered bounding for geometries that can be incorporated into existing PWRs. J. Malen performed the steady-state thermal hydraulic analysis with a single channel VIPRE model for square and hexagonal arrays, and a full core VIPRE model for square arrays. The single channel performance for each array type was identical for matching combinations of rod diameter and hydrogen to heavy metal (H/HM) ratio. For this condition, square and hexagonal sub-channels have the same coolant flow areas and heated and wetted perimeters, which determine thermal hydraulic performance in confined flow channels (See Section 2.3.1 for the derivation). The maximum power is therefore expected to be the same, as confirmed by the single channel results. 20 Based on the single channel analysis, J. Malen assumed that the full core hexagonal power could also be inferred from the full core square results. A full core hexagonal VJIPREmodel was therefore not undertaken. Modeling a core is different than a single channel though, because turbulent interchange of mass, momentum, and energy occur across sub-channel boundaries. Furthermore, these interchanges are slightly different for square and hexagonal arrays [2]. It is therefore important to verify that differences in sub-channel communication do not significantly impact the thermal hydraulic performance equivalence of hexagonal and square designs for matching rod diameters and H/HM ratios. If the discrepancy is large, then the parametric study will need to be performed separately for hexagonal array cores. The purpose of this chapter is twofold. First, several fixed parameters in the thermal hydraulic analysis have recently changed and require regeneration of the maximum power results for the full core square model, using J. Malen's approach. For continuity, the steady-state thermal hydraulic design methodology is briefly re-introduced and summarized. Where more information is desired, the reader is referred to [1]. Second, the thermal hydraulic equivalence of square and hexagonal array designs at matching rod diameters and H/HM ratios is proven by: deriving the geometric relationships for flow area and heated and wetted perimeters for square and hexagonal sub-channels; and constructing a full core hexagonal VIPRE model for a single geometry for comparison with the square model results. 2.1.1 Reference Core Parameters The reference core for the thermal-hydraulic analysis is the South Texas Plant, a 4 loop PWR designed by Westinghouse. It provides a set of fixed hardware dimensions and operating conditions that define boundaries for the thermal hydraulic analysis to ensure the feasibility of new designs (i.e., ensure that new designs can be integrated into existing PWRs). The dimensions and operating conditions that are fixed in this analysis are listed in Table 1.1. Parameters that have recently changed are denoted by an asterisk *. Note that these changes are not a result of changes in the operating conditions at 21 South Texas, but rather misinterpretation in their evaluation during the initial stages of the project. Table 2.1 Fixed Parameters for the Thermal Hydraulic Analysis 111 Parameter Symbol Value Core Radius Rcore -1.83 m (72") Active Fuel Length Lh 4.26 m (168") Core Enthalpy Rise' * Ah 204 kJ/kg Inlet Temperature Tinlet 294 C (561.2 F) System Pressure Psat 2250 psia Radial Peak to Average Power Fq 1.65 Axial Peak to Average Power * Fq'axial 1.55 The reference core geometry and power are: P Dre = 9.Smm = 1.326 (2.3) ef = 3800MWt 2.1.2 Design Limits The steady-state thermal hydraulic design limits, which constrain the maximum power achievable for each geometry, are briefly discussed in this section. They were developed with guidance from industry and MIT faculty by J. Malen to provide safety margin and ensure technical feasibility for new designs using both oxide and hydride fuels. It is important to note that because the limits are placed on thermal hydraulic performance, they are equally applicable to both fuel types. The single exception is the fuel temperature limit, which will be further discussed in Section 2.1.2.3. The limits are summarized in Table 2.2. The changes to the core enthalpy rise and axial power peaking factor noted in Table 2.1 have modified the MDNBR and lower pressure drop numerical limits slightly from those implemented in J. Malen's study. Table 2.2 Summary of Steady-State Thermal Hydraulic Design Limits for UZrH1.6 and UO2 MDNBR 2.173 Pressure Drop 29 psia, 60 psia Fuel Temperature 750 C UZrHi.6, 1400 C UO2 Axial Velocity 8 m/s The core enthalpy rise was fixed to protect the steam generators, which mandates that the hot leg temperature, after core outlet and bypass flow mixing, remain below 326.7 C (620 F). 22 2.1.2.1 MDNBR Departure from nucleate boiling (DNB) is the most limiting constraint on power for commercial PWRs. DNB occurs at the critical heat flux, which is a function of the geometry and operating conditions in the core. It is characterized by a sharp decline in the heat transfer coefficient at the coolant/cladding interface, as vapor blankets the fuel rod preventing fluid from reaching its outer surface. The result is an abrupt rise in the temperature of both the fuel and cladding, which can damage the fuel and/or cause a cladding breach. The performance metric for DNB is the MDNBR, which is the minimum ratio of the critical to actual heat flux found in the core. In commercial design, significant margin exists in the MDNBR limit to account for transients, core anomalies (i.e, rod bow), process uncertainty (i.e, instrument error), and correlation uncertainty. While it is difficult to quantify the magnitude of each, a reasonable MDNBR limit can be obtained by executing VIPRE at the reference core geometry and operating conditions. The reference core's MDNBR limit already accounts for the needed margin. The use of the MDNBR given by VIPRE as the MDNBR limit for the steady-state thermal hydraulic analysis therefore ensures that all new designs will demonstrate the same level of DNB margin as the reference core. This limit is - 2.17. One final note on the MDNBR limit is warranted. Using the limit, as described above, assumes that the margins built into the reference core's MDNBR limit are sufficient for all geometries considered in this study. This may not be true, however, for the transient contribution. Consider, for example, the loss of flow accident (LOFA). Designs that are tighter than the reference core will coast down more quickly, and therefore require additional margin for transients in the overall steady-state MDNBR limit. To account for this, a fellow graduate student at MIT, Jarrod Trant, is evaluating the maximum power with respect to specific transient design limits [3]. Ultimately, the final maximum achievable power will be the minimum power given by either the steadystate or transient analyses, at each geometry. The transient and steady-state results are combined in Chapter 4 of this report for the final economic optimization. 23 Also note that because the equivalence of full core square and hexagonal thermal hydraulic models is undertaken in this chapter, the limits listed in Table 2.2 are assumed to apply equally to both configurations. The correlation used in VIPRE to determine the CHF is the W-3L, which can be used for both arrays if grid spacers are used. If wirewrapped designs are considered in the future, new CHF correlations will apply and the MDNBR limit will need to be modified. This is not undertaken in this study. 2.1.2.2 Pressure Drop The maximum pressure drop sustainable through the primary system is determined by the capacity of the coolant pumps. Two separate pressure drop limits are used in the steady-state thermal hydraulic analysis to reflect the current and 5 year expected enhanced states of pumping technology. While losses occur throughout the entire primary coolant loop, the limit is based on the pressure drop across the fuel bundle, because it will vary most among the redesigned cores. The lower pressure drop limit indicative of current PWR pumping capacity is determined in the same manner as the steady-state MDNBR limit: finding the pressure drop across the fuel bundle given by VIPRE for the reference core geometry and operating conditions. This pressure drop is approximately 29 psia. The enhanced pressure drop limit is based on examination of pumping capacities for the Westinghouse AP600 and AP1000 PWR designs, and a survey of industry experts. The pressure drop in the core nearly doubled between the design of the AP600 and AP1000, and so it is reasonable to believe that in the next 5 years before a hydride fueled core could be constructed, the capacity could again double. The enhanced fuel bundle pressure drop limit is therefore 60 psia. The maximum power is presented for both pressure drop limits in Section 2.2. 2.1.2.3 Fuel Temperature Based on experience with hydride fuels used in TRIGA reactors, a steady-state fuel centerline temperature limit of 750 C was adopted for this analysis [1]. The limit is based on prevention of hydrogen release from the fuel during steady-state irradiation. 24 Excessive hydrogen release can embrittle the clad, pressurize the fuel pin, and introduce an explosive hazard into the core. At temperatures below 750 C, the partial pressure of hydrogen gas is low, and the gas remains evenly distributed in the fuel matrix. Unlike hydride fuels, oxide fuels release non-negligible amounts of fission gas, which, if not limited, can pressurize and even burst the fuel pin. Based on fuel performance data for oxide fuels, the fission gas release fraction can be kept below 5% by limiting the average fuel temperature to 1400 C [4]. This is the temperature limit adopted for oxide fuel. Note that this is more limiting than imposing a peak centerline temperature limit of 2800 C, which is the melting point of UO2. Note that this temperature limit only applies to steady-state operation; J. Trant's thesis [3] will determine if core designs from the steady-state analysis exceed temperature limits during transients. 2.1.2.4 Axial Flow Velocity Because the enthalpy rise across the core is fixed, a specific geometry can only achieve higher powers by increasing the coolant flow through the core. As the bulk flow gets larger, the turbulent axial and cross-flow velocities increase, making a vibrationrelated rod failure more probable. It is therefore desirable to provide design limits to restrict rod vibrations, and resultant wear at the cladding/rod support interface. In lieu of a detailed vibrations and wear analysis for each core design, J. Malen imposed a single limit on the hot channel axially averaged velocity. The limit was based on a judgment during the initial phase of the Hydride Fuels Project that vibration problems could be avoided in PWRs by limiting the axial velocity of coolant to 7 m/s. The limit adopted was 8 m/s, under the assumption that additional grid spacers would be added if deemed necessary by a separate fluid-elastic instability analysis of select, optimum geometries. The wide range of geometries considered and the large power increases reported by the thermal hydraulic analysis makes it prudent to refine this single limit approach. A 25 more thorough analysis of relevant vibration and wear mechanisms is required. This analysis is performed in Chapter 3 of this report. Because the purpose of Chapter 2 is to update J. Malen's results for steady-state maximum power, and to prove the equivalence of hexagonal and square array designs, the single velocity limit is maintained. The final thermal-hydraulic results used in the economic optimization study in Chapter 4, however, will be based on the updated vibrations and wear design limits presented in Chapter 3. 2.1.3 MATLAB/VIPRE Interface The VIPRE sub-channel analysis code was developed by the Electric Power Research Institute (EPRI) to aid in thermal hydraulic modeling and design of LWR cores. More specifically, it predicts the velocity, pressure, and thermal energy fields, and the fuel rod temperatures for interconnected flow channels. VIPRE also predicts DNB performance. To execute VIPRE, a detailed input deck must be constructed in which every facet of the core geometry and the operating conditions must be prescribed. The output deck is an exhaustive text document that must be manually read by the analyst to determine if a given core is operating within pre-defined design limits. Both input deck generation and output interpretation are prone to human error by nature of the complexity of the formatting and the sheer magnitude of the information. The capabilities of VIPRE have been greatly expanded through the efforts of J. Malen and another former MIT student Stu Blair [5] by the development of student written MATLAB scripts. S. Blair initiated the MATLABN/IPRE interface by developing scripts that automatically generate VIPRE input decks and extract relevant VIPRE output with minimal input required from the user. The output is saved into MATLAB space, where it can be easily interpreted and manipulated by the user. Using this basic construct, J. Malen coded additional scripts that iteratively determine the maximum power for a range of geometries subject to user defined design limits. The programs execute according the following sequence: 26 * The design space is specified by the user, which includes the desired range of rod diameters and P/D ratios, as well as the discretization within each range (i.e, 20 equally space rod diameters between 6.5 mm and 12.5 mm); · MATLAB programs generate a VIPRE input deck for the first geometry in the parametric study, and supply an initial guess for power; * VIPRE is executed, and the constrained parameters (i.e, MDNBR, pressure drop, flow velocity, fuel temperature) extracted from the VIPRE output file are compared with the design limits within MATLAB; * If no design limits are exceeded, the power estimate is increased, and VIPRE is executed with an updated input deck; * If one or more design limits are exceeded, the power estimate is decreased, and VIPRE is executed with an updated input deck; * Each VIPRE execution is followed by a comparison of the constrained parameters with their respective design limits; * The maximum power occurs when one constrained parameter meets its design limit, and the remaining parameters stay below their design limits; This procedure continues for every geometry in the parametric analysis. Note that the programs can only be used to evaluate maximum power for square array designs. Considerable modifications to the scripts would be necessary to consider hexagonal arrays. The reader is referred to [1] for a thorough description of the MATLAB scripts. 2.2 Results of the Steady-State Maximum Power Analysis In preparation for the thermal hydraulic comparison of square and hexagonal array PWR geometries, the updated maximum power results for square arrays are presented. Figures 2.1 and 2.4 show the maximum achievable power for square arrays of UZrH1. 6 and U0 2 as a function of P/D ratio and rod diameter for both pressure drop limits. Color maps power, where "hotter" colors indicate higher powers. The color scale is shown at the right of each plot. The maximum power for the enhanced pressure drop case occurs at: P/D - 1.42, Drod- 6.8 mm. The power is - 5458 MWth, almost a 45% 27 increase over the reference core power. A less substantial, but still sizeable increase is realized for the lower pressure drop case, where the maximum power is -4245 MWth. The geometry is shifted slightly from the high pressure drop case: P/D - 1.48, Drod= 6.5 mm. It is helpful to understand how the power gains are realized over the design space. For a fixed core length, the maximum power, L~, depends on the average linear heat rate, q', and the number of rods in the core, N. -- '- N L (2.4) As long as a design limit is not exceeded, the power can be raised by increasing the average linear heat rate and/or the rod number. Figures 2.2 and 2.5 show the ratios of the rod number, average linear heat rate, and power for new geometries to the reference core rod number, average linear heat rate, and power. Note that the product of Figures 2.2A/2.5A and 2.2B/2.5B yield Figure 2.2C/2.5C. A black line is used to denote the contour where each ratio is unity. Figures 2.3 and 2.6 plot the constrained parameters that determine the maximum achievable power for each geometry. Regions where constraints are limiting are shown as dark red. Note that because the fuel temperature limits for UO 2 and UZrH .1 6 are never reached, their maximum achievable powers are identical. 28 Figure 2.1 Maximum Achievable Power vs. P/D and Drod for Square Arrays of tUZrH 60 psia Core Power (x10 6 kWlkt; 6 and U0 2 at a U 1'2 5.5 5 1 1 45 4 10 3.5 "o, : Q 3 2.5 g 2 1.5 1.1 1 15 1.2 1.25 1.3 ' 1.35 1.4 1 1.45 1.5 P/I Figure 2.2 Rod Number, Linear Heat Rate, and Power Ratios vs. P/D and Drod for Square Arrays of UZrH. 6 and UO2 at 60 psia B: q/qre A: N/N ref 12 12 11 11 10 2 o 1.5 IC ' 1 .0 1 I 7 1.1 1.2 1.3 1.4 0.5 7 I .7 0 1.5 P/D C PP 1.1 1.2 1.3 P/D 1.4 1.5 12 1.5 11 1 0.5 7 f:9 1.1 1.2 1.3 1.4 1.5 I P/D 29 Figure 2.3 Constraining Parameters vs. P/D and D,,d for Square Arrays of UZrHL.6 and ITO2 at 60 psia A: Pressure Drop (psia) ill "a B: W3-L MDNBR -- 60 12 -2.5 11 11 -3 1( 1-1 I 20 O -3.5 8 7 -4 rl 1.1 1.2 1. 14 1.1 1.5 1.2 ; 1.4 1.5 D: Fuel CL Temp. UZrH. , (C) 8 12 12 6 11 700 -11 600 :10 9 4 019 500 8 8 7 2 7 1.1 1.2 13 1.4 1.1 1.5 1.2 1.3 1.4 1.5 400 ETemp Fuel UO(C)PD Ave. A _ ^. ' 14UU 12 1200 1000 10 9 c 800 8 600 7 Ann -tuu 1.1 1.2 1.3 1.4 1.5 P/D 30 Figure 2.4 Maximum Achievable Power vs. P/D and D,.,d for Square Arrays of UZrHI.6 and UO2 at 29 psia Core Power (xl 06kWth) 6 12 5.5 5 11 K 45 4 1' 3.5 11 3 2.5 2 1.5 7 1 '1 1.15 1 125 1.2 1.3 1.3 1.4 1.45 1.5 P/D Figure 2.5 Rod Number, Linear Heat Rate, and Power Ratios vs. P/D and Drodfor Square Arrays of UZrH *1 6 and UO02at 29 psia A: N/N B: q/%f ref 1 3 '1 10 'O .. ) 9 2 1 1 1.5 1 1 0.5 8 1.1 1.2 1.3 P/D 1.4 1.5 I n v 1.1 C P/P 1.2 1.3 P/F 1.4 15 I 2 1.5 1 I::: 0.5 0 9 0.5 1.1 1.2 1.3 1.4 PAD 1.5 I 31 Figure 2.6 Constraining Parameters vs. P/D and D,.odfor Square Arrays of UIZrHI.6and UtO2 at 29 psia B: W3-L IvDNBR A: Pressure Drop (psia) 12 I 1 '1 c1c -2.5 11 20 1l0 15 9 Q) 12 25 -3 0t 1yA 10 8 8 l 5 I 1.1 1.2 1.3 P/D 1.4 7 1n U 1.5 1.1 12 .D 1.4 1.5 -3.5 A -~t D: Fuel CL Temp. UZrH. (C)F C: Axial rd 12 I 1U 11 I 12 18 11 - I 700 600 210 4 O9 500 8 8 2 7 f: 1.1 1.2 J 1.4 1.1 1.5 1.2 1.3 1.4 1.5 I Ann Y.UU P/D E: Fuel Ave. Temp UQ(C) 14UU00 12 , I 11 1200 10c 1000 0 800 Q 8 600 7 I 1.1 1.2 1.3 1.4 Ann '-tU 1.5 P/D 32 2.3 The Equivalence of Square and Hexagonal Array Geometries Confined square and hexagonal array sub-channels at the same H/HM ratio and rod diameter have the same coolant flow areas and heated and wetted perimeters, which determine thermal hydraulic performance. It is this fact which motivates the extension of the square array results presented in Section 2.2 to hexagonal designs. It is desirable, however, to prove this equivalency between full core VIPRE models, which, unlike the single channel analysis, accounts for the turbulent interchange of mass, momentum, and energy among sub-channels. 2.3.1 Geometric Relationships for Square and Hexagonal Arrays Before discussing the construction of the full core hexagonal VIPRE model, the relationships between the P/D and H/HM ratios for square and hexagonal arrays are developed. nce defined, the geometric equivalence of square and hexagonal arrays at the same H/HM ratio and rod diameter is shown. Note that this information was first developed by J. Malen and is presented in [1]. Recent changes to the fuel rod cladding and gap thickness correlations, however, invalidate portions of the original derivation. The relationships are therefore re-developed in this report incorporating all updated information. 2.3.1.1 Conversion Between Hydrogen/Heavy Metal and Pitch/Diameter Ratio The general notations for variables used in this derivation are defined in Table 2.3. 33 Table 2.3 General Nomenclature for Geometric Relationships for Square and Hexagonal Arrays - Name Avogadro's Constant Symbol Cladding Thickness tcl Units Value UZrH,. 6 '---- mm Value U0 2 6.02x1023 6.02xl 023 (2.14) & (2.16) (2.14) & (2.16) NA 3 -6 10.43x10 - 6 Densityof the Fuel Pfuel kg/mm Density of Water (at 700 F) PH20 kg/mm 3 6.67x10- 7 6.67x10- ' Diameterof Fuel Pellet Diameterof Fuel Rod Dpellet mm (2.18) (2.18) D mm tg mm (2.15) & (2.17) (2.15) & (2.17) MHM kg/kmol 237.85 237.85 MMatrix kg/kmol 93.2 MH20 kg/kmol 18 18 I I Gap Thickness Molecular Weight of Heavy Metal MolecularWeightof Fuel Matrix (ZrH,.6 ) Molecular Weight of Water Number of Heavy Metal Atoms Per Unit of the Fuel Matrix Element 8.256x10 Y HM Number of Heavy Metal Atoms Number of Hydrogen Atoms Per Unit of the Fuel Matrix Element X Number of Hydrogen Atoms H Pitch P Volume V Weight Percent Heavy Metal w 1.6 mm mm 3 .45 .8813 The number of hydrogen atoms in a prescribed volume of water and fuel (i.e. in a sub-channel/unit cell) is given by: (2.5) H = HHI + Hfuel where, HH Hfu 0 -=2' NA PHO . VHO MHO Hel=X. NA Pfuel' Vfuel ( - w) =: X e(MMatr (2.6) (2. 7) Matrix where, X: number of hydrogenatomsper unit of thefuel matrix w: weight percent heavy metal in thefuel Note that Hfuelis 0 for UO2. The number of heavy metal atoms in a prescribed volume of fuel is given by: 34 HM = YNA Pfiel Vie W (2.8) MHM where, Y: number of heavy metal atoms per unit of the fuel matrix Taking the ratio of equations (2.5) to (2.8) gives the H/HM ratio: H_ HM (.2).(1).MM Y w MHO ) .+(.M. Pfuel ) fuel Y mMatrix W W) ) (2.9)HYMNM Square Array For square arrays, VH 2 0 : = Aflow-sq L (2.10) Vfuel = Afuel* L Aflow-square = pq ,r (2.11) 4 2 pellet 4 Afue Afuel = (2.12) (2.13) To determine the diameter of the fuel pellet, the radial gap and cladding thicknesses must be specified. The original correlations for gap and cladding thickness used in [ 1] scaled linearly with rod diameter. It is believed by industry experts, however, that this leaves the gap and cladding too thin at small rod diameters. New correlations were therefore adopted that impose a minimum cladding and gap thickness. ifDrod < 7.747 mm to= .508 mm tg = .0635 mm (2.14) (2.15) ifDrod > 7.747 mm tc 1 = .508 +.0362 (D - 7.747) mm (2.16) tg =.0635+.0108. (D- 7.747) mm (2.17) Dpellet:=D - 2 -t -2 t (2.18) 35 Substituting constants from Table 2.3 and equations (2.12) and (2.13) into equation (2.9) gives the H/HM ratios for square arrays of UZrH1.6 and U0 : 2 HM =4.745. + 4.991 UZrH1.6 = 1.918 (2.19) (2.20) (HM UO2 Rearranging and solving for P/D gives the desired relationship between the P/D and H/HM ratios: r (P. =j. 166 l D PDsq,UZrH1.6 (D sq,Uo2 1 (41Dpellet) 991 + 0.785 )HM H + 0.785 (2.21) (2.22) Hexagonal Array Equation (2.9) can also be applied to hexagonal arrays. L VH20 = Aflow-hex Aflow-hx =: J.p2* 4 (2.23) - 4 D2 8 (2.24) Substituting equations (2.23) and (2.24) and the constants in Table 2.3 into equation (2.9) gives the H/HM ratios for hexagonal arrays of UZrH 1.6 and UO : 2 2 HM )UZrH .6 Z= 47451 TD +4.991 4.- Ph2x D2 _ Dpellet (2.25) 36 H HAL (2.26) =1.918 = U~o 2 Rearranging and solving for the P/D ratios gives: H pellet HM eD hx,'H11 16 (PI = h (227) +0. 0.191.~~~~~~~~~~~~ ts= 0.473 pelet j( (2.28) +0.907 * Thus it is shown that the P/D ratio depends on both the HIHM ratio and the rod diameter. The H/HM ratio is shown graphically in Figure 2.7 as a function of rod diameter and P/D ratio for square and hexagonal arrays of UZrH. 6 and U0 2. Note that the rod diameter has very little influence on the H/HM ratio. Figure 2.7 H/HM Ratio vs. P/D and Drod for Square and Hexagonal Arrays of UZrH. 6 and UO2 H/HM: Hex. Arrays of UZrH 16 H/HM: Sq. Arrays of UZrH 1.6 201 -- 18 20 1'. 116 : 16 14 12 .,: 0 rod (mm) 8 H/HM: Sq. Arrays of UO 2 8-- cL _ 8l. 42-, 012 od 8 Do(mm) 1.1 130 ' 13 PD 12 PD HIHM: Hex. Arrays of UO 2 -l 1W- 18 10; 10 i 12: 1W 10 5 4 4: 2- 3 01 1.512 0P/ . . 2 7 . 641~ r 2 12 D, (mm)8(mm) 1.4 . 1.2 P/D 37 2.3.1.2 Relationship Between Square and Hexagonal Array Sub-Channels To prove the geometric equivalence of square and hexagonal array sub-channels at the same rod diameter and H/HM ratio, a relationship between the square and hexagonal pitch is determined. This proof is only carried out for UZrH 1.6, but could easily be performed for UO2 given the equations in Section 2.3.1.1. For equivalent rod diameters and H/HM ratios, a constant C is defined such that, Dpellet 2 (H (2.29) Substituting equation (2.29) into equations (2.21) and (2.27) gives the square and hexagonal P/D ratios for UZrH1 .6 with respect to C. =O.166 C+0.785 PI D = Jo ll (P) D (2.30) sq,UZrHI.6 c+0.907 (2.31) hex,UZrH1.6 Solving for Psqand Phe: PSq= D .166C + 0.785 (2.32) Phe,= D 0.191.C + 0.907 (2.33) 1.0746. Pq = Phe (2.34) For equivalent combinations of rod diameter and H/HM ratio, equation (2.34) can be used to relate the rod pitch between square and hexagonal lattices. This relationship also holds for UO2, though the derivation is not provided. The flow areas and heated and wetted perimeters are now presented for square and hexagonal arrays. Square and hexagonal unit cells are shown in Figure 2.8. 38 Figure 2.8 Square and Hexagonal Array UJnitCells jr-f6>(~N TI \ '~I '( { A ) Phex/ Psq \ f2 Drod ) Drod For the square array, the geometric relationships are: Aflo-q .. - P,sq = Psq = (2.35) 4 (2.36) D The geometric relationships for the hexagonal sub-channel, with Phexwritten with respect to Psy according to equation (2.34), are: /3 ·(1.0746.P A i-hex P,,,.hex = fh,he.- = 4 q . Dr. (2.37) -. = 0.5 A2orq 8 = 0. 5 2 Z Psq (2.38) = 0.5. Ph,,q The flow area and heated and wetted perimeters for the hexagonal sub-channel are exactly one half the corresponding values for the square sub-channel. They are identical, however, on a unit rod basis (hexagonal sub-channels have 0.5 rods and square subchannels have I rod). Because the thermal hydraulic performance of new core designs depends on the total flow area and total heated and wetted perimeters, hexagonal and square designs with the same rod number, H/HM ratio, and rod diameter will have the same total flow area and heated and wetted perimeters. Thus the geometric equivalence between square and hexagonal arrays is shown, and it is believed that the square array steady-state thermal hydraulic results presented in Section 2.2 can be extended to hexagonal arrays by modifying the P/D ratio according to equation (2.34): ) D = 1.0746 hex () (2.39) D q 39 This means that the power at Drod = 6.5mm and (P/D)sq = 1.29 should be the same as that for Drod = 6.5mm and (P/D)hex = 1.387, if differences in lateral mixing are negligible. This is proven in the next section by constructing a full core hexagonal VIPRE model. 2.3.2 Full Core Hexagonal Array VIPRE Model As discussed in Section 2.1, the mixing characteristics that determine the interchange of mass, momentum, and energy among sub-channels are slightly different for square and hexagonal array designs. To verify that this discrepancy does not translate into more significant differences in core power, a full core hexagonal VIPRE model was constructed for a single geometry for comparison with the square results. Like the analysis for square arrays, the maximum power was determined subject to design limits on MDNBR, pressure drop, fuel centerline temperature, and axial velocity. It is assumed that the reader has some familiarity with the VIPRE code; it is therefore not the intent of this section to explain in exhaustive detail the construction of a VIPRE input deck and the interpretation of the code's output. Rather an overview of the full core model is provided, followed by the presentation of results. The fixed operating conditions and dimensions adopted from the reference core for the square analysis are also applied to the hexagonal core. For readers interested in these details, please refer to Appendices B and C, where the thermal hydraulic assumptions and the VIPRE input deck are provided. The square and hexagonal geometries chosen for this single model verification are: Dsq = Dhex = 6.5mm (2.40) (P (2.41) =1.29 (De= H sq HM 1.0746 = 1.386 - q (H M e = 1281 (2.42) (2.43) 40 2.3.2.1 Rod and Assembly Layout Within the Core Due to symmetry, a full hexagonal core can be adequately represented by a 1/6t" section. Because the pressure vessel radius, rod diameter, and pitch are fixed, the number of hexagonal fuel assemblies that can fit in the core depends on the number of rings in each assembly. A 9 ring hexagonal fuel assembly was adopted because of its common use in liquid metal cooled fast breeder reactor designs. Figure 2.9 9 Ring Hexagonal Fuel Assembly L DI 3 Dft The dimensions of the fuel assembly are defined by the length of one side of the hexagon, D,, and the distance across the flats of the hexagon, Dft. Dj1 = j2 .Nrings Phex +g (2.44) D). ()5 (2.45) + where, g = (Phx l,=(-p¢1)-"he. +3 .2+g 3 22) (2.46) where, Nps: number of rods per side The rod diameter and pitch are given by equations (2.40) and (2.42), and the reference core pressure vessel radius is given in Table 2.1. With this information, the number of 9 41 ring fuel assemblies that fit radially in the core starting at its center (with the center rod of the first assembly at the center of the core) is 11.5. The 1/6th core section is shown in Figure 2.10. Figure 2.10 1 /6th Hexagonal Core Section 11 VIPRE requires that every sub-channel in the core model be specified in the input deck, which can be a tedious task for the user. For the design range considered in the parametric study, the number of channels in the core can easily approach 100,000. To ease this burden, and lessen the computational strain for program execution, VIPRE allows channel lumping. A lumped channel is simply a large grouping of individual subchannels; it is specified by the total heated and wetted perimeters and flow areas of the individual channels that it comprises. Communication of mass, momentum, and energy are still allowed, although fluid properties and conditions are uniform within each lumped channel. The lumped channels for the 1/6th core section (# 82 - 91) are shown in Figure 2.11. The radial power distribution is peaked near the center of the core, so the hot subchannel in the core always occurs within the central assembly2 . A fine mesh of individual sub-channels is maintained throughout this central assembly, and outer 2 The radial power profile is provided in Appendix B. 1.9 42 assemblies are lumped together in increasingly larger areas. This lumping effect is shown in Figure 2.1 1, where the hot assembly comprises the first 82 flow channels, and is represented by the 1/6th assembly section at the top. Figure 2.11 Channel Lumping in the 1/6h Hexagonal Core Figure 2. 12 shows a close up of the hot assembly section, and demonstrates the correct numbering technique for fuel rods and sub-channels in VIPRE. Note that control rods are not numbered. The position of control rods in the assembly was randomly selected, but the number is chosen so that the number of fuel rods per control rod in the reference core is maintained in the hexagonal core. 43 Figure 2.12 1/6thSection of the Hot Assembly 2.3.3 Comparison of Maximum Power Predictions from Square and Hexagonal Arrays The powers predicted by the square and hexagonal full core models are shown in the Table 2.4. Table 2.4 Power Predictions by Full Core Square and Hexagonal VIPRE Models SquareArray HexagonalArray Drod 6.5 mm 6.5 mm P/D 1.29 1.387 H/HM 12.21 12.21 Heated Rods q' Limiting Constraint 111,760 108,433 2.49 kW/ft 2.46 kW/ft 3933 MWth 3740 MWth Pressure Drop Pressure Drop 44 The difference in predicted power is - 5%. The majority of this discrepancy has to do with how efficiently the core cross section is utilized by the fuel assemblies. Both models demonstrate the same heated and wetted perimeters and flow areas per unit rod, because the rod diameter and H/HM ratios are the same. Notice, however, that the number of heated rods in the core is larger for the square model. This is because the pressure vessel dimensions are fixed, and the hexagonal and square assemblies do not utilize the space in the core with the same degree of efficiency (one model leaves more wasted, unheated flow area at the core's periphery). Vessel space could be optimized for the hexagonal model by changing the number of rings in each assembly, but this is not considered in this analysis. The core power is simply the product of the number of heated rods and the average linear heat rate, which is independent of the core cross section. The linear heat rate is therefore a better indicator of thermal hydraulic performance than the power. The linear heat rates for the square and hexagonal array models are very close, differing by - 1.2%. This discrepancy could be caused by several reasons: the precision of convergence to thermal hydraulic design limits; differences in the sub-channel friction factor; and differences in the turbulent interchange of mass, momentum and energy. Because both models are limited by pressure drop, the friction factor difference is most likely the culprit. The difference, however, is so minute that it is safe to conclude that the steady-state thermal hydraulic analysis for full core square arrays can be safely extended to hexagonal arrays for matching rod diameters and H/HM ratios. 45 46 3. Vibrations Analysis for Hydride and Oxide Fueled PWRs 3.1 Introduction Dynamic forces generated by the turbulent flow of coolant in PWR cores cause fuel rods to vibrate. Flow-induced rod vibrations can generally be broken into two groups: large amplitude "resonance type" vibrations, which can cause immediate rod failure or severe damage to the rod and its support structure, and smaller amplitude vibrations, responsible for more gradual wear and fatigue at the contact surface between the fuel cladding and rod support. While the former group is typically prevented by adequate structural design of the fuel assembly, the latter is unavoidable. Sufficient wear resistance must therefore exist in the fuel assembly components to preclude excessive damage. Ultimately, both vibration types can result in a cladding breach, and therefore must be accounted for in the thermal hydraulic design of hydride and oxide fueled PWRs. The thermal hydraulic analysis to determine the maximum achievable power for hydride fueled cores did not account for specific vibration mechanisms; instead, a single limit on the axial flow velocity was imposed [1]. This limit was based on a judgment during the initial phase of the Hydride Fuels Project that vibration problems could be avoided in PWRs by limiting the coolant axial velocity to 7 m/s in the core. The wide range of core geometries considered and the large power increases reported by the thermal hydraulic study makes it prudent to refine this single limit approach. A more thorough analysis of relevant vibration and wear mechanisms is needed, with appropriate design limits imposed for each mechanism. 3.2 Work Scope 3.2.1 Goals of the Vibrations Analysis The thermal hydraulic analysis for hydride fueled PWRs linked a series of student developed Matlab programs and the VIPRE sub-channel analysis code to iteratively determine the maximum achievable power for a range of core geometries, subject to user 47 defined design constraints. Constraints included minimum departure from nucleate boiling ratio (MDNBR), fuel centerline temperature, bundle pressure drop, and axial flow velocity. The maximum power reported by the study for a given geometry was the highest power for which no constrained parameter exceeded its design limit. The goal of the vibrations analysis is to develop and incorporate new design limits for flow-induced vibration and wear mechanisms into the existing thermal hydraulic programs, replacing the single limit on axial velocity. The results will include new maps of steady-state power for PWR geometries utilizing hydride and oxide fuels. Combined with the transient analysis performed by J. Trant [3], the thermal hydraulic analysis for maximum power will be complete. 3.2.2 Flow-Induced Vibration Mechanisms - Overview Three primary types of flow-induced vibration are observed for cylindrical fuel elements subject to cross and axial flow: * Vortex-Induced Vibration: Vortex-induced vibration can occur by two means: vortex shedding lock-in and vortex-induced acoustic resonance. In vortex shedding lock-in, the frequency of the vortices shed by cross-flow over the fuel rod "lock in" to the rod's structural frequencies, causing resonant vibration. In vortex-induced acoustic resonance, the shedding frequency excites standing acoustic waves created by the operation of fans, pumps, valves, etc. in the coolant loop3 . Because the rules to avoid lock-in are more conservative than the rules to avoid acoustic resonance, only vortex shedding lock-in is considered in this analysis. * Fluid-Elastic Instability: Fluid-elastic instability of a rod bundle occurs when the cross-flow velocity exceeds the critical velocity for the bundle 3 Standing waves are required for the acoustic resonance condition. They are formed when acoustic waves traveling in opposite directions (as when an acoustic wave deflects off of fuel rods) superimpose onto one another. 48 configuration, at which point the rod response increases uncontrollably and without bound. Turbulence-Induced Vibration in Cross and Axial Flow: The fluctuating pressure fields generated by cross and axial flow turbulence in the core exert random forces on the fuel rods, causing vibration. The vibration amplitudes associated with vortex shedding lock-in and fluid-elastic instability are generally very large, and can quickly cause severe damage to the fuel rod and its support structure. If the pitch is tight enough, rod failure by tube-to-tube impaction is also possible. Fortunately, these devastating mechanisms can be prevented by adequate design of the fuel assembly structure for the flow conditions in the core (i.e. using an appropriate number of grid supports and providing adequate stiffness to the fuel rod). Unlike vortex shedding lock-in and fluid-elastic instability, turbulence-induced vibration is generally of small amplitude and cannot be avoided. The principle design concern is therefore not the prevention of the vibration mechanism, but the limitation of resultant wear at the cladding/rod support interface. Wear is a concern for two reasons. First, excessive wear can directly breach the clad or increase the likelihood of a breach from other rod damage mechanisms (i.e. impact stress and fatigue). Second, wear at the cladding/rod support interface lowers the structural frequencies of the rod, making it more susceptible to vortex-induced vibration and fluid-elastic instability. The most common wear mechanism, and historically the most costly flowinduced vibration problem in the nuclear industry, is fretting wear. Fretting results from combined rubbing and impaction between the fuel rod support and the cladding surface. Sliding, or adhesive, wear also occurs where the grid support springs and rod rub against one another. Both wear types are considered in this study. 49 The mechanisms considered and their respective design concerns are summarized in Table 3.1. Table 3.1 Flow-Induced Vibration Mechanisms Flow-Induced Mechanism Vortex-Induced Vibration * Fluid-Elastic Instability * Large amplitude vibrations occur when cross-flows exceed the critical velocity for the rod bundle configuration Turbulence-Induced Vibration in Cross and Axial Flow * Small amplitude rod vibrations from turbulence generated pressure fields cause excessive fretting and sliding wear at the cladding/rod support interface Design Concern Large amplitude vibrations occur when vortex shedding frequencies lock-in to the structural frequency of the rod 3.2.3 Methodology The vibrations analysis is performed using the MATLAB/VIPRE interface described in Section 2.1.3. In order to consider the vibrations and wear mechanisms within this construct, constrained parameters with appropriate design limits need to be developed, which is undertaken in Section 3.4. Unlike the steady-state analysis described in Chapter 2, the constrained parameters for this vibrations and wear analysis cannot simply be "measured" during core operation. Rather they are dependent on multiple parameters including the structural properties of the fuel rod, sub-channel geometry, and the cross and axial flow distributions within the core. With additional MATLAB scripts, the new limits are incorporated into the existing thermal-hydraulic program structure, where the iterative approach to maximum power can once again be employed. 3.3 Assumptions 3.3.1 Vibrations Analysis in the Nuclear Environment Vibrations analysis for nuclear fuel rods is extremely complex given the random nature of turbulent flow in the core. Adding to the complexities, severe thermal, mechanical, and radiation loads, as well as wear accumulation, continuously change the structural mechanics of fuel assembly components. Accurately predicting the vibration 50 response of fuel rods over time is therefore an arduous task at best, and even impossible without the aid of state-of-the-art finite element analysis (FEA) codes. 3.3.2 Key Assumptions The following simplifying assumptions are made so that the vibrations analysis can be performed without the aid of advanced computational tools and with best-practice guidance in the academic literature: The fuel rod is modeled as a linear structure: This assumption is based on treating the grid supports as single pin supports. In reality, the gapped support condition between the grid spacer and the fuel rod allows relative movement between the two components. With this movement, non-linear FEA codes are needed to quantitatively model the rod response, which is beyond the scope of this work. A linear rod model and experimental correlations for rod response are used as a substitute. * Changesto thefuel assemblystructureover time are not considered: Core operating conditions play a significant role in the structural mechanics of fuel assembly components during fuel irradiation. For example, creep-down of the cladding due to pressure forces, support spring relaxation due to irradiation, and wear accumulation combine to slowly open the gap between the fuel rod and its support. Oxidation from temperature extremes and irradiation change the material properties of all structural components in the core. Rod bow may also occur, changing the rod/support structure interaction and the flow distribution of coolant in the core. Because of the difficulty associated with modeling these effects, and the lack of guidance outside of proprietary vendor computer codes, structural changes to the rod and support structure are neglected. * Only the cladding structure is considered in thefuel rod model: A gap exists for fresh fuel rods between the fuel pellets and the cladding. Over time, the fuel swells closing this gap, and it contacts the cladding surface. In addition, gases 51 generated by the fission process and any burnable absorbers present pressurize the pin. For conservatism, the additional rigidity provided by fuel swelling and rod pressurization is not considered. * Only the first vibration mode is considered: The first vibration mode (fundamental mode) typically has the largest impact on rod vibration. With regard to vortex shedding lock-in and fluid-elastic instability, the use of the first mode typically yields the most conservative design margin. Furthermore, several correlations used in place of FEA codes for modeling turbulence-induced vibration response are only applicable for the fundamental mode. * Corepower is the only operatingparameteraffecting the vibrationsperformance of new designs: Implied in the iterative approach to maximum power with vibrations imposed design limits is the sole dependence of vibrations performance on core power. A design that fails a vibrations design limit can be made acceptable, however, by changing other parameters. One example is modifying the fuel rod and assembly hardware to affect the vibration frequency and amplitude of the rod. This can be accomplished by using additional grid spacers, thicker cladding, or a combination of the two. Both, however, have trade-offs. Thicker cladding implies less fuel per rod, and more grid spacers, while making a design more vibration resistant, will increase the pressure drop across the core. For this analysis, the cladding thickness is not considered variable for vibrations design purposes; additional grid spacers will only be considered if a geometry fails to meet all vibrations design limits with modest power reductions. These are the key assumptions used in the vibrations analysis. Additional simplifications for specific vibration and wear mechanisms, where needed, are presented in subsequent sections. 52 3.4 Vibration and Wear Mechanisms 3.4.1 Dynamic Parameters The dynamic parameters and material properties used in the vibrations analysis are defined in this section. They are derived from [6]. 3.4.1.1 Nomenclature Table 3.2 defines the general notation for properties and parameters used in the derivations throughout this section. Table 3.2 General Nomenclature for the Vibrations Analysis Name Added Mass Coefficient Average Length Between Spacers Cladding Density Cladding Inner Diameter Cladding Linear Mass Cladding Moment of Inertia Cladding Outer Diameter Symbol Units Cm Ls m Pet Dcl, mc, Ici Dco or D kg/m 3 m kg/m m tcl m E Pfl mfl C N/m 2 kg/m 3 kg/m Cladding Thickness 4 Cladding Young's Modulus Coolant Density Coolant Linear Mass Damping Ratio Value 6550 m 9.9063 x 101° 700 Mode Shape Function NaturalFrequency fn Number of Grids Number of Spans ng ns Pitch P m Total Fuel Rod Length L, m, m kg/m Total Linear Mass s ~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~ .... 3.4.1.2 Linear Mass Cladding Linear Mass: mcI = Pcl . (Dc - D ) (3.1) 4 Cladding thickness depends on the fuel rod diameter. See equations (2.14) - (2.17). 5 Coolant density is assumed to be constant, and equal to the average coolant density in the reference core. 53 Coolant Linear Mass: Added Mass Coefficient: where, Total Linear Mass: Mfl=Cm "Il~e4 .(f)pfl D2, (D *2 +1) C = (D2 (3.3) 1) }(P D*(1+ (3.2) (3.4) ~D (3.5) mt = mcl +mf 3.4.1.3 Moment of Inertia Cladding Moment of Inertia: ( ICI = 6 4 i) o- (3.6) 3.4.1.4 Natural Frequency and Mode Shape 1 st Natural Frequency: f(=2 .s (3.7) in 1 stMode Shape Function: where, /l (x)= jns Lx n, =ng -1 (3.8) (3.9) 3.4.1.5 Damping Ratio The following table shows ASME recommended fluid damping ratios for different rod support conditions. Table 3.3 ASME Recommended Damping Ratios [61 Mean Values Conservative Values Cn,water or wet steam, tightly supported tube 0. 015 C,nloosely supported tube 0. 01 0.03 0.05 Because a smaller damping ratio leads to larger vibration amplitudes and less margin with regard to fluid-elastic instability, the most conservative value is chosen: = 0.01. 54 3.4.1.6 Generation and Distribution of Axial and Cross-flow Velocities The vibrations performance of fuel rods depends on both the structural properties of the fuel assembly and the distribution of axial and lateral flows in the core. Once the geometry and power level are specified, VIPRE computes the coolant axial and lateral (cross-flow) velocity profiles for each channel and gap specified in the full core model. The distribution of flow around individual rods is accurately captured for the hot assembly, which is at the center of the core. In the outer channels where lumping is used, VIPRE computes average cross-flow and axial velocities. Because the flows are greatest in the hot assembly, and the individual flow distributions around each rod are computed, the vibrations analysis will only consider the coolant velocities in the hot assembly. The vibrations and wear performance of new designs will depend on the magnitude of the cross-flow and axial velocities. It is therefore important to establish their relationship with core power, given the need for each constrained parameter in the thermal hydraulic analysis to scale with power. Though this relationship may seem intuitive, simplified proofs and examples are presented below. 3.4.1.6a Axial Velocity Because the enthalpy rise, Ah, in the parametric study is fixed to the enthalpy rise in the reference core, the power l for a specific geometry can be changed by either increasing or decreasing the mass flow rate .l=cor e Ah lScore through the core. (3.10) The mass flow rate is simply the mass flux G multiplied by the total core flow area. nore = G Alow (3.11) For the conditions of low void fraction that exist in a PWR core, an average mixture density Pmcan be used to relate the axially averaged coolant velocity to the mass flux. G Vaxial- -- (3.12) Pm Making appropriate substitutions yields the desired relationship between average axial velocity and core power. 55 Vaia -= fl Ah =c Pm Ajow' Ah (3.13) It is therefore seen that the axial velocity for a specific geometry is directly proportional to core power. 3.4.1.6b Cross-flow Velocity For bare rod bundles, cross-flows between adjacent channels are generated by two mechanisms: turbulent fluctuations in the axial flow that drive turbulent mass interchange, and transverse pressure gradients that drive diversion cross-flow [2]. Turbulent interchange can be thought of as eddies of equal volume that cross the subchannel boundary. If these eddies are also of equal density, as in the case of single phase flow, no net mass is exchanged. In two phase flow, however, mass is transferred from channels of higher density to channels of lower density. Because the density difference between adjacent channels in a PWR is relatively small, the cross-flow velocity contribution from turbulent interchange is minimized. Diversion cross-flow is therefore the dominant factor driving cross-flows. The transverse pressure gradients that drive diversion cross-flow arise for two reasons: geometric anomalies in the core (i.e., rod bow), and non-uniform changes in coolant density. Geometric anomalies are not considered in this analysis. Density changes between adjacent channels are due to radial heat flux variations, and larger local differences accompanying the onset of boiling. The radial power profile peaks near the core's centerline, and tapers off toward the outer assemblies. Moving through the core, the enthalpy rise is greater for coolant in the centrally located channels. Adjacent channels therefore undergo phase and property changes to a different extent at the same axial location. This gives rise to pressure gradients across channels due to the dependence of pressure drop on local quality and mixture density. These gradients drive diversion cross-flow. As the power increases, the amount of coolant flowing into and out of the hottest channels will also increase. Cross-flow velocities are therefore expected to scale with core power. 56 This effect is illustrated in Figure 3.1, which plots the cross-flow velocity profile given by VIPRE for a randomly selected gap in the hot assembly at three different powers. There are two important things to notice from this figure. First, the cross-flows are greatest for the highest power, and smallest for the lowest power. Hence, the crossflows do scale with core power. Second, the effect of grid spacers on the local cross-flow velocity is to sharply increase its magnitude at each grid location. The first two grids are non-mixing, and therefore the deviations from the normal velocity profile are small. The next eight, however, have mixing vanes, and the magnitudes of the deviations are significantly larger. The negative values indicate that coolant is flowing into the channel. Figure 3.1 Cross-flow Velocity Profile as a Function of Core Power U.1 0.i 0.( 2O. t > -0.1 O-0 -0.1 0 20 40 60 80 100 AxialPositionon) 120 140 160 180 3.4.1.6c Cross-flow and Axial Velocity Inputs to the Vibrations Analysis For conservatism, the local peak cross-flow and axial velocities are used in performing the vibrations and wear analyses, with two exceptions. First, the large crossflows occurring at grid spacer locations are ignored because they are not representative of the remaining cross-flows in the gap. Because they only occur at the grid locations where the rod motion is constrained, their contribution to the overall vibration response of the rods will be negligible anyway. A second exception applies specifically to the case of fluid-elastic instability, where Au-Yang [6] recommends the use of an "effective" cross- 57 flow velocity in evaluating the fluid-elastic instability margin (See Section 3.4.3). The effective cross-flow velocity for the nht mode is obtained by weighting the cross-flow velocity profile in each gap by the vibration mode shape of the rod. Cross-flows occurring at the mid-point between spacers, where the vibration amplitude is largest, will therefore be given more weight than cross-flows occurring at the supports, where the amplitudes are approximately zero. Neglecting changes in the coolant density and linear mass axially along the gap, the effective cross-flow velocity for the first mode is given by: rz2 _ 0 reJj - (3.14) L, Figure 3.2 is a plot of the first vibration mode shape function for a rod simply supported by 10 grid spacers. Also shown is a representative cross-flow velocity profile from VIPRE, with the cross-flows at the grids removed. The maximum, effective, and average cross-flow velocities for the profile are reported on the figure. The effective cross-flow velocity typically lies between the channel maximum and average values. Figure 3.2 Cross-flow and Fundamental Mode Shape Profiles 0. 08 0.06 0.04 .5 0 U, 0.02 0 C, (I) 0 2 U -0.02 ()rAt -U.Ul 0 20 40 60 80 100 120 140 160 180 Axial Position (in) 58 3.4.2 Vortex-Induced Vibration Cross-flow over cylindrical elements generates vortices that are shed alternately from one side of the structure to the other. This shedding produces an uneven pressure distribution around the rod, and resultant forces act on the structure in both the lift (perpendicular to the flow) and drag (parallel to the flow) directions. The force component in the lift direction has a frequency equal to the vortex shedding frequency,f,, while the drag component has a frequency equal to twice the vortex shedding frequency. When the vortex shedding frequencies are well separated from the natural frequency of the structure, only mild vibrations occur. When the shedding frequency in either the lift or drag direction approaches any of the rod's natural frequencies, a phenomenon called lock-in occurs. In this event, the shedding frequency assumes the natural frequency of the vibrating rod, causing larger resonance-type vibrations. This effect may cause immediate failure of the rod, or lead to premature wear. Because the shedding frequency may actually shift to the natural frequency of the rod, sufficient separation must exist between the two frequencies to preclude this resonant behavior. 3.4.2.1 Vortex-Shedding Margin and Design Limit The vortex shedding frequency is given by: f=s=SV D (3.15) where the Strouhal number, S, was found by Weaver and Fitzpatrick [6] to depend on the P/D ratio and channel shape. For square arrays, S = 2(P/D / - 1) ) (3.16) and for hexagonal arrays, S-i= 1 DII~ 1 1.73(P/D-1) (3.17) (3.17) To assess the susceptibility of new core designs to vortex-shedding lock-in, a vortex shedding margin (VSM) is defined in both the lift and drag directions. This margin indicates the separation distance between the rod and shedding frequencies. Au- 59 Yang [6] recommends that lock-in will be avoided as long as this margin is greater than or equal to 30%. The vortex shedding margins in the lift and drag directions are defined as: VSMif =ffI VSM dragIf, (3.18) -2 (3.19) 2 fs where, f: fundamentalfrequencyof the rod And the design limit to avoid vortex-shedding lock-in is: VSMliQ & VSM drag 0.30 (3.20) Lock-in can occur for any of the fuel rod's natural frequencies. For the range of geometries considered in this study and the corresponding magnitude of cross-flow velocities reported by VIPRE, the shedding frequencies are closest to the fundamental rod frequency. The use of the first natural frequency in the VSM is therefore the most conservative approach; if a core design avoids lock-in with the fundamental mode, then all higher order frequencies will avoid lock-in too. The vortex-shedding margins in both the lift and drag directions for the reference core geometry are plotted as a function of a hypothetical cross-flow velocity in Figure 3.3. It is evident that, depending on the cross-flow velocity, vortex-shedding margins can be increased by either raising or lowering the cross-flow velocity. Because the crossflow velocities scale with power, this implies that designs failing a vortex-shedding design limit can be made acceptable by either increasing or decreasing the power in the core. This could prove problematic when incorporating the vortex-shedding design limits into the thermal-hydraulic codes, which are set up to reduce, not increase, power if a design limit is exceeded. To resolve this issue, it is helpful to examine the magnitudes of the peak cross-flows at the reference core geometry for several different powers. These are shown in Table 3.4 below. Notice that even for very large powers, the cross-flow velocities stay well within the desirable cross-flow range where reducing power will 60 increase the vortex-shedding margin. It is therefore concluded that lowering the power is a viable approach for improving the vortex-shedding performance of new designs. Figure 3.3 Vortex-Shedding Margin vs. Hypothetical Cross-flow Velocity at the Reference Core Geometry A C'.. I I I : 40) -- -| | : | S VSM LiftDirection 1 Drag Direction ]- -iVSM _ I 2) 300 > I I I I I I I _ I 20() n0 I I 25() ' ~ I 350 Ž I I- - I L r - -r - - L . I I_ L . _ ~ ~ I I ----- I I . I I ~ { _ ~~ ~~~I I I I I I I I I _ I -. ...-......... I -- -I -_ I _ . -~r I _ a)o 10() _ . _ I I\ - 50 0 I \ I( - I -X-I -- \ -I I ------ I I -I 0.1 . I I . I -- 0.05 - 0.15 0.2 I I T 0.25 0.3 - . I I I - __ 0.35 0.4 Cross-flow Velocity (m/s) Table 3.4 Peak Cross-flow Velocities vs. Power for the Reference Geometry Power (MWth) Cross-flow Velocity (m/s) 2000 0.0313 3000 0.0473 4000 0.0696 5000 0.0985 A final note on vortex-induced vibration: even if lock-in is avoided, the shedding of vortices contributes to small amplitude rod vibrations, and therefore rod wear and fatigue with time. The magnitude of this vibration, however, is usually small and bounded by turbulence-induced vibration, which is considered in Section 3.4.4. The off lock-in vortex-shedding contribution to fretting and sliding wear is therefore not considered. 61 3.4.3 Fluid-Elastic Instability Fluid-elastic instability of a tube bundle occurs when the cross-flow velocity reaches the critical velocity, at which point the vibration response of the tubes suddenly increases uncontrollably and without bound. Unlike other vibration mechanisms, the instability of the tube, and therefore its vibration amplitude, continues to increase as the cross-flow velocity rises above the critical value. A tube that is elastically unstable can experience rapid structural damage by any combination of the following damage mechanisms: * Tube-to-tube impaction: this causes impact wear at the midpoint of a span length. Within a few days, or even hours in the most extreme cases, enough material can be removed from the cladding surface to burst the fuel rod. * Fatigue failure: this occurs when stress in the fuel rod exceeds the endurance limit for the cladding material. The fuel rod will sever at the location where the stress is highest, often at the grid supports. * Acceleratedfretting wear: accelerated wear rates accompanying the large vibration amplitudes can quickly wear through the cladding surface at contact points. 3.4.3.1 Fluid-Elastic Instability Margin and Design Limits A fluid-elastic instability margin (FIM) is defined to quantify a tube bundle's performance with regard this mechanism. It is the ratio of the maximum effective crossflow velocity in the hot assembly, Veff,to the critical velocity for the bundle geometry Vcritical: rFIM- ef (3.21) Vcritical 62 The FIM' can be thought of as a safety margin: as long as the effective cross-flow velocity remains below the critical velocity (and the FIM remains below 1), fluid-elastic instability will not occur. The design limit is therefore: FIM <1 (3.22) The most widely accepted correlation for estimating the critical velocity for a tube bundle is Connor's equation [6]: Vcritical =Pnf 'f Pfl (3.23) where Pettigrew [7] suggested a P/D effect on Connors' constant: / = 4.76. P-1)+0.76 (3.24) The critical velocity is constant for a fixed geometry and, with the exception of small changes in coolant density, does not depend on the power and flow conditions in the core. Evident in Connor's equation is the conservatism accompanying the use of the first natural frequency, which yields the lowest critical velocity and the largest FIM. Because of the relationship between effective cross-flow velocity and power, the FIM will scale with power and can therefore be incorporated as a design constraint into the existing thermal hydraulic analysis. 3.4.4 Turbulence-Induced Vibration Turbulence from cross and axial flows generate random pressure fluctuations around fuel rods, causing them to vibrate. The energy associated with the pressure fluctuations is distributed over a wide range of frequencies. Vibration occurs when the rod selects the portion of this energy that is closest to its natural frequency. Unlike fluidelastic instability or vortex shedding lock-in, whose respective impacts can be minimized and even eliminated in the design phase of the fuel assembly structure, turbulenceinduced vibrations cannot be avoided. Furthermore, no specific design limits are applicable because the vibration amplitudes accompanying turbulence are small. The 63 principle design concern is therefore not the prevention of the mechanism but the limitation of resultant wear at the cladding/rod support interface over time. Assessing the wear performance of new core designs requires knowledge of the rod response, or its displacement amplitude. Turbulent flows and the associated pressure distributions causing rod vibration, however, are random; it is therefore impossible to determine a detailed time history of the rod response. Instead, probabilistic methods are used to estimate the root mean square (RMS) response from both cross and axial flow turbulence. The total rod response is simply the summation of the cross and axial flow contributions, and becomes the primary input to the wear performance portion of the vibrations analysis (See Section 3.4.5). 3.4.4.1 Turbulence-Induced Vibration in Cross-flow Despite the latest advancements in computational fluid dynamics, the turbulent rod response remains best characterized by a combination of experimental and analytical J techniques and correlations. Assuming the vibration modes of the rod are well separated, Au-Yang [6] recommends the following relationship for estimating the RMS rod response from cross-flow turbulence: (2 .) - 64* where, GF: Jnn.' . mt (Xross n n (3.25) randomforce power spectral density joint acceptance The turbulent forcing function that drives the rod response is characterized by the random force power spectral density (PSD), GF, and the joint acceptance Jn. The joint acceptance is the probability that a structure originally vibrating in the nth mode will remain in the nth mode under the excitation of the forcing function. Assuming that the correlation length for the forcing function is equal to the length between grid spacers, and remembering that only the first vibration mode is considered, Au-Yang recommends a value of 0.64 for the joint acceptance of a simply supported tube. JI = 0.64 (3.26) 64 Based on experimental testing, Pettigrew and Gorman [6] suggested the following empirical equation for the random force PSD for single-phase turbulent cross-flow over tube bundles: GF = CR D2 Pl (3.27) ross The random lift coefficient, CR,depends on the normalized random pressure PSD, GP, which has been correlated by Au-Yang to the dimensionless frequency, F. The relationships are provided here: F= CR (3.28) VI.S = J7 GP (3.29) where, GP = 0.01 for F <0.1 0.2 for 0.1 <F <0.4 5.3e4F 7 /2 for F > 0.4 Referring back to equation (3.25), the mode shape function, ,if (x), is assumed constant and equal to its maximum value. This adds conservatism to the determination of the RMS response. The maximum of the mode shape function is easily obtainable from equation (3.8): Y/l,max= (3.30) L The final form of equation (3.25) for the upper bound RMS rod response from turbulent cross-flow is given by: Yrms-cross 64 3 m 3 (3.31) 65 Vibration in Axial Flow 3.4.4.2 Turbulence-Induced For comparable velocities, axial-flow induced vibrations are generally of much less concern than cross-flow-induced vibrations. In PWR cores, however, the axial velocity is often two or more orders of magnitude larger than the peak cross-flow. With this in mind, the rod response contribution from turbulent axial flow is often more significant than the cross-flow contribution. The method for determining the RMS rod response from cross-flow turbulence can be applied to axial flows, with the use of appropriate PSD forcing functions. A simpler approach, however, is recommended by Paidoussis [6], who developed the following correlation from experimental data to estimate the upper bound maximum rod response from axial-flow turbulence: 1.6 =5e-5 Ymax-axial 1.8 4 .25 ( - 4 l+u2 ' 1+4 .) (3.32) where, K: a: 5. Ofor turbulentflow 7rfor simply supported rods V: Vaxialvs p f A it V,,ial: peak axial velocity A,: outer rod cross sectionalarea e: Re: LID Reynold's number hydraulic diameter Dh: : pfl A,/m, Pfl: coolant density m,: total linear mass Assuming the rod response follows a normal distribution, the RMS axial response is approximately one third of the peak response: YYrms-axial - Y m a x -axial (3.33) 3 3.4.4.3 Turbulence-Induced Vibration Response The total RMS rod response is equal to the sum of the cross and axial flow contributions: Yrms = Yrms-axial + Yrms-cross (3.34) 66 This is the primary input for the wear portion of the analysis. 3.4.5 Wear Due to Flow-Induced Vibration There are three primary types of wear mechanisms caused by flow-induced vibration: impact, fretting, and sliding wear. Impact wear, or tube-to-tube impaction, occurs when fuel rods experience very large amplitude vibrations. Because this behavior is precluded by design limits for fluid-elastic instability and vortex-induced vibration, impact wear is not considered. Fretting wear is the most common wear mechanism, and historically the most costly flow-induced vibration problem in the nuclear industry. Fretting results from combined rubbing and impaction between the fuel rod support and the cladding surface. Sliding, or adhesive, wear occurs by the rubbing motion between the grid support springs and rod. It is often difficult to distinguish between these latter two wear types. Fretting wear is typically associated with smaller vibration amplitudes for gapped supports, where both wear and impact stress make contributions to material degradation. Sliding wear is typically associated with slightly larger vibration amplitudes, and results from the relative motion of two surfaces in continuous contact with one another. Modeling the rate and accumulation of wear for nuclear fuel rods is extremely complex. Because specific design limits for wear are vague, cumulative rod wear for new designs will be limited by the end of life cumulative wear calculated for reference core fuel pins. To estimate wear, the wear rate must be calculated, which requires knowledge of the relative motion between the rod and its support. Because the linear rod model assumed in this analysis treats the grid spacers as pinned supports, no relative motion exists. Once again, non-linear structural dynamics and FEA codes are needed to solve the problem quantitatively. The academic literature, however, has simplified models for qualitatively assessing the fretting and sliding wear performance of new designs using a linear rod model under known flow conditions. This is the approach adopted for the wear analysis. 67 3.4.5.1 Fretting Wear Performance and Design Limits Determining the cumulative fretting wear requires knowledge of both the fretting wear rate, fretting and the wear coefficient, Kr d . Because most of the damping for a vibrating fuel rod comes from the interaction between the rod and its support, Yetisir et al [6] suggested that the fretting wear rate can be approximated as the power dissipated by the vibrating rod. The power dissipation depends on the structural properties of the rod and the RMS response from flow-induced vibration. The power dissipation, or fretting wear rate, for the first vibration mode is given by: 'fretting =32,r 3 . r ' f 13 L mt y2 rs (3.35) Notice that this equation implies that the fretting wear rate is independent of time; in reality this is not true. Reasons for this include: spring relaxation, cladding and grid material degradation, and wear accumulation. These factors combine to slowly open the gap between the fuel rod and its support, changing both the rod's vibration frequency and amplitude. To accurately determine the cumulative wear as a function of time, an iterative approach incorporating non-linear FEA codes is required to continuously update the wear rate given by equation (3.35) as the dynamic properties of the fuel rod change. This is beyond the scope of this work. It is generally accepted by industry, however, that after a brief "break-in" period, the wear rate does not change significantly, unless the rods are allowed to remain in the core until failure. Because the reference core design is sufficiently robust to prevent wear-related rod failures, and the cumulative wear of new designs is limited to the cumulative wear of the reference core, a constant wear rate can safely be assumed for this analysis. The cumulative volume of material removed by fretting wear as a function of time, T is approximated by Archard's equation [6]: Qfretting= fretting Krod T (3.36) The wear coefficient, Krod, is material dependent and must be determined experimentally. Because the cladding and grid materials are identical for both new and 68 the reference designs, the wear coefficients will be the same. By taking the ratio of the cumulative fretting wear for new designs to the cumulative fretting wear for the reference core, the wear coefficients cancel. Qfretting,new -f retting,new Tnew Teref Qfretting,ref mt (3 Yrmsnew 337 Tnew ref ms Tref Recognizing that the lifetime of the fuel in the core is equal to the product of the number of batches, n, and the cycle length, T,, and that the cumulative fretting wear ratio for the end of life fuel must remain below 1, equation (3.37) becomes: Qfreting,new ( mt YrMs 2 new Qfretting,ref mt Yrms f ,e (3.38) (3.38) n Tc,ref Rearranging and canceling terms yields: Afretting,new = t Yms fretting,ref m, ymsref Inew <cre f c,new (3.39) This is the desired relationship for the fretting wear analysis: the wear rate ratio is the constrained parameter, and the ratio of the cycle lengths is the design limit. If a new design has a shorter cycle length than the reference core, then it can safely accommodate a higher rate of wear. Note that the wear rate limit, due to its dependence on cycle length, will depend on both the power and the fuel bumup. The power, however, depends on the wear rate limit, and the burnup, when limited by fuel performance constraints, depends on the power. The relationships among the individual analyses in the optimization study were illustrated in Figure 1.1. Several iterations are therefore required to determine the core power subject to the design limit for fretting wear. Another comment on the wear rate limit is also warranted. The Hydride Fuels Project is examining different enrichments of UZrH1 .6 for potential use in PWRs; each enrichment, via the neutronics analysis, has a different achievable burnup for the same geometry. Burnup increases with enrichment, and so does the cycle length. The economics analysis presented in Chapter 4 will show that costs are minimized at higher 69 enrichments for UZrH1. 6 and lower enrichments for U0 2. The wear rate limits are therefore determined for the highest enrichment (12.5%) hydride fuel and the lowest enrichment (5%) oxide fuel. Note that a consequence of this is imposing a more stringent wear rate limit on hydride fuel than oxide fuel. The benefit, however, is that the maximum power input to the economics analysis will be specifically adapted to the lowest cost enrichments for each fuel type. Ideally, the vibrations analysis would be performed separately for all enrichments of hydride and oxide fuels, but this is not undertaken in this work. 3.4.5.2 Sliding Wear Performance and Design Limits Connors [6] suggested that the sliding wear rate is equal to the product of the normal contact force between the rod and support spring, F,, and the total sliding distance, Sd. siding = (3.40) Fn ' Sd The normal contact force is given by: - D y,,(3.41) - s F = L, 0D · L --+ LA,j E+ 4E,, I,, s where, u: coefficient offriction Acl: claddingcross-sectionalarea The sliding distance is given by: Sd = Tr.f, g. T (3.42) where, g: diametralgap betweenthe tubeand support Assuming a constant wear rate, the cumulative sliding wear at time t is: Qsliding = T' Krod Fn ' f'g 'gT (3.43) As in the case of fretting wear, the cumulative sliding wear in new designs is limited to the cumulative sliding wear in the reference core. Taking the ratio of the wear 70 rates and reducing like terms yields the desired constrained parameter and design limit for the sliding wear analysis: (* sidingref 1 D __I+ -- rs *w l (D. Yrms fAl)re-- 2 A,, 41 2 s~1idingref Ac+ 4n l A, IC (3.44) Tc,new e e The wear rate limit is once again equal to the ratio of cycle lengths. 3.5 Summary of Constrained Parameters and Design Limits Table 3.5 summarizes the final list of constrained parameters and design limits used in the steady-state maximum power analysis for hydride and oxide fuels. The first four are the new relationships developed in this chapter to limit flow-induced vibrations and wear to acceptable levels. The remaining limits were carried over from the original analysis presented in Chapter 2. Table 3.5 Summary of Steady-State Thermal Hydraulic Design Constraints Design Constraints For: Constrained Parameters Vortex-Shedding Lock-in VSMif,, VSMdrag Fluid-Elastic Instability FIM Fretting Wear frettng,n Design Limit Equatosce Equations > 0.3 (3.18), (3.19) <1 (3.21) (3.39) < cnew fretting,ref SlidingWear siding,new DNBR MDNBR Pressure Drop AProdbundle Fuel Temperature (3.44) T,r sliding,ref Tcenterline- UZrHl. 6 Taverage - U0 2 cnew > 2.17 < 29 psia, 60 psia < 750 C < 1400 C 71 3.6 Results of the Maximum Achievable Power Analysis With Vibrations-Imposed Design Limits for Square Arrays 3.6.1 Results at 60 psia for UZrH1 . 6 The maximum achievable power for UZrH 1.6 at 60 psia is shown in Figure 3.4 with vibrations and wear imposed design limits. The peak power geometry, occurring at P/D - 1.37 and Drod = 6.5 mm, is - 5017 MWth. This is -450 MWth lower than the peak power determined by the thermal hydraulic analysis without the vibrations and wear limits (See Figure 2.1). Figure 3.5 shows the ratios of the rod number, average linear heat rate, and power for the new geometries to the reference core rod number, average linear heat rate, and power. A black line is used to denote the contour where each ratio is unity. The regions where the hydride core has a higher power than the reference core have been reduced significantly; no regions exceed the reference linear heat rate (compare with Figures 2.2B and 2.2C). The reduction is more clearly seen in Figure 3.6, which plots the difference in power achievable with and without the vibrations and wear limits imposed. The peak power reduction is close to 2200 MWth, and occurs at a P/D 1.16 and Drod 11.8 mm. Figures 3.7 and 3.8 plot the constrained parameters, where dark red shading indicates that a design limit has been reached (and therefore constrains power). While MDNBR and pressure drop continue to limit large regions of the design space, the area originally occupied by the axial velocity limit has been replaced and enlarged by limits on fretting and sliding wear. Recall that one of the primary inputs to the wear rate equations is the RMS rod response, which is composed of axial and cross-flow components (equation (3.34)). Because the axial velocities in the core are orders of magnitude larger than the cross-flows, the axial flow term dominates the RMS rod response. It is therefore expected that the wear limits will be reached where the axial velocities are greatest, which is the observed behavior. The fluid-elastic instability margin, as shown in Figure 3.8C, never approaches its limit of 1; its maximum value over the entire design range is 0.34. The vortex shedding 72 margins are plotted separately in Figures 3.9A and 3.9B in both the lift and drag directions. Unlike the wear parameters, the vortex-shedding margins are very sensitive to changes in the cross-flow velocity. As shown in Figure 3.9C, VIPRE experienced difficulty in converging to cross-flow solutions for P/D ratios less than - 1.2. The code's output for several geometries, apparent by large velocity spikes, do not appear likely and made it difficult to maintain the vortex-shedding design limits in the thermal hydraulic code in this region. The limits were therefore only imposed for geometries with P/D ratios greater than 1.2. As a result, several of the vortex shedding margins at the tighter geometries are less than 30%, as evident in the figure. These need to be re-investigated, particularly if the economically optimum geometries fall into this region. It is hoped that an updated version of the VIPRE code will soon be available at MIT, and that the convergence problems will be resolved. Figure 3.4 Maximum Achievable Power vs. P/D and Drodfor Square Arrays of UZrH1.6 at 60 psia with Vibrations and Wear Imposed Design Limits Core Power (xl 06 kWh ) 5 12 4.5 4 11 135 '10 B 9 2.5 1.5 7 1.1 1.15 1.2 1.25 1.3 1.35 1.4 1.45 1.5 P/ 73 Figure 3.5 Rod Number, Linear Heat Rate, and Power Ratios vs. P/D and D,.odfor Square Arrays of UZrH1. 6 at 60 psia with Vibrations and Wear Imposed Design Limits B: q/q., A NI/Nf 12 13 12 1.5 11 <11 ' 10 2 110 1g 8 1 Q 7 I0 1.1 1.2 1.3 P/D 1.4 1 88 0.5 I 7 1.1 1.5 1.2 O-Dlt 1.3 P/D 1.4 1.5 12 1.5 11 1 c 108 7 1.1 1.2 1.3 1.4 1.5 I P/D Figure 3.6 Power(,, vibrations) - Power(vibrations)VS.P/D and Drodfor Square Arrays of UZrH1.6 at 60 psia Core Power Difference (kWh) x106 I 10 . ... IZ.D 1: 2 11 1 5 IU Q c 8 5 7 1.1 1.15 1.2 1.25 1.3 P/D 1.35 1.4 1.45 1.5 74 Figure 3.7 Thermal Hydraulic Constraining Parameters vs. P/D and D,.,,dfor Square Arrays of UZrH1. 6 at 60 psia with Vibrations and Wear Imposed Design Limits B: W-3L MDNBR A: Pressure Drop (psi) 60 12 12 I 11 10 20 1.1 1.2 1.3 1.4 1.5 I0 P/D C: Axial Velocity (m/s) 1.2 1.3 P/D 14 1.5 D: Fuel CL Temperature (C) 12 11 l 700 10 600 'a9 4 o I -4 1.1 la 11 -3 5 7 8 12 -3 7 8 8 7 I -2.5 11 11 10 40 500 8 I 7 1.1 1.2 1.3 R/D 1.4 2 I 1.5 1.1 1.2 1.3 1.4 Adln -J 1.5 P/D Figure 3.8 Vibrations and Wear Constraining Parameters vs. P/D and Drodfor Square Arrays of UZrH1. 6 at 60 psia A: Fretting Wear Limit B: Sliding Wear Limit 12 12 I 0.8 11 I 10 0.4 0.4 9 C-) 8 0.2 I0 7 11 1.2 1.3 1.4 1.5 I 0.8 10 006 'O9 0.4 8 0.2 I0 7 1.1 PID C: FIM I 11 1.2 1.3 PJD 1.4 1.5 1 12 I 0.8 1 '1 0.6 O 0.4 0.2 7 1.1 1.2 1.3 1.4 1.5 I0 PID 75 Figure 3.9 Vortex-Shedding Margins and Peak Cross-flow Velocity vs. P/D and D,.,t for Square Arrays of UZrH1. 6 at 60 psia A: VSM Lift (%) B: VSM Drag (%) 12 12 -100 11 10 I 7 1.2 1.3 1.4 -200 o9 -400 1.1 03 -200 -300 8 I -100 11 1.5 -300 8 7 1.1 P/D C: Peak Cross-flow Velocity (/s ) 1.2 1.3 1.4 1.5 I -400 PI/ 0.2 ....... 0.1 12 :ro d . 8 - (mm) - _ P/D _1.4 3.6.2 Results at 60 psia for UO2 The maximum achievable power for UO2 at 60 psia is shown in Figure 3.10. The peak power geometry and peak power are almost identical to hydride: 5045 MWth at P/D - 1.37, Drod = 6.5mm. Figure 3.11 shows the ratios of the rod number, average linear heat rate, and power for the new geometries to the reference core rod number, average linear heat rate, and power. The regions where the oxide core has a higher power and linear heat rate than the reference core have been reduced, though not to the extent experienced by the hydride fuel (compare with Figures 2.2B and 2.2C). The reduction is more clearly seen in Figure 3.12, which plots the difference in power achievable with and without the vibrations and wear limits imposed. The peak power reduction is 1435 MWtl,, and occurs at a P/D - 1.2 and Drod = 12.5 mm. Figures 3.13 and 3.14 plot the constrained parameters, which demonstrate similar behavior to the case of hydride fuel. MDNBR and pressure drop continue to limit large regions of the design space, and the axial velocity limit is replaced by fretting and sliding 76 wear, once again because of the dominance of the axial flow term in the rod response equation. The fluid-elastic instability margin remains well below 1. The vortex shedding margins and the peak cross-flow velocities are shown in Figure 3.15. The cross-flow convergence problems are again evident, and so the vortex shedding design limits were not maintained below a P/D of 1.2. Figure 3.10 Maximum Achievable Power vs. P/D and Drod for Square Arrays of UO2 at 60 psia with Vibrations and Wear Imposed Design Limits Core Power (xl 0 6 kWth) 12 5.5 5 11 4.5 '- 10 .5 ~o .5 8 .5 7 1.1 1.15 1.2 1.25 1.3 1.35 1.4 1.45 1.5 P/D 77 Figure 3.11 Rod Number, Linear Heat Rate, and Power Ratios vs. P/D and D,.,,dfor Square Arrays of UJO2 at 60 psia with Vibrations and Wear Imposed Design Limits A: N[Neref B q/q,%f 12 12 3 1.5 11 11 a:: 7 2 10 1 8 S I 1.1 1.2 1.3 PfD C 1.4 05 7 1.5 1.1 1.2 DD 1.3 P/D 1.4 15 I 12 1.5 11 0O5 8 I 7 1.1 1.2 1.3 1.4 1.5 P/D Figure 3.12 Power(novibrations)- Power(,brations) VS. P/D and Drodfor Square Arrays of U0 Core Power Difference (kWtU) 2 at 60 psia XI196 Z.D 12 L 11 1.5 - 10 1 8 05 7 1.1 1.15 1.2 1.25 1.3 1.35 1.4 1.45 1.5 Q P/D 78 Figure 3.13 Thermal Hydraulic Constraining Parameters vs. P/D and Drodfor Square Arrays of U0 2 at 60 psia with Vibrations and Wear Imposed Design L,imits B: W-3L MDNBR A: Pressure Drop (psi) 60 12 I 40 11 12 I -25 11 11 -3 20 8 I En 1.1 1.2 1.3 1.4 -3-5 8 7 I -4 1.1 1.5 P/D 1.2 V C: Axial Velocity (m/s) 0 12 I 11 6 1c 1.3 P/D 1.4 15 D. Fuel Ave Temoerature (C) 12 lI 11 I 10 4 I 1.1 1.2 1.3 1.4 1400 1000 *9 8 7 2 1200 1.5 I 1.1 1.2 1.3 1.4 800 1.5 P/D P/D Figure 3.14 Vibrations and Wear Constraining Parameters vs. P/D and Drodfor Square Arrays of UO2 at 60 psia A: Fretting Wear Limit 12 B: Sliding Wear Limit I 1 'O 71 7 1.1 1.2 1.3 1.4 1.5 12 0.8 I 0.8 3611 0.6I1 0.6 0.4 9 0.2 8 7 I0 P/D 0.4 0.2 I0 1.1 1.2 1.3 14 1.5 P/D 1 12 0.8 11 0.6 O( 0.4 0.2 0 1.1 1.2 1.3 1.4 1.5 P~ 79 Figure 3.15 Vortex-Shedding Margins and Peak Cross-flow Velocity vs. P/D and D.od for Square Arrays of UO2at 60 psia A: VSM: Lift (%) B: VSM: Drag (%) '12 I -100 11 10 2I 8 1.1 1.2 1.3 1.4 1.5 I PfD C: Peak Cross-flow Velocity (s) I -100 11 -200 v10 -200 -300 9 -300 -400 8 7 -400 -jnn --- v I 1.1 1.2 1.3 1,4 Inn -J UU 1.5 P'D 03 U.2 0. 12 8'- (m) Drod (M) 1.2 P/D 3.6.3 Comparison Between UZrH1.6 and UO2 at 60 psia Figure 3.16 shows the difference in maximum achievable power for UO2 and UZrH .6 at 60 psia with vibrations and wear imposed design limits. Note that oxide fuel has a power advantage in the sliding and fretting wear limited regions because of the difference in wear rate limits applied to each fuel. Recall Section 3.4.5.1, which explained the rationale for using a more stringent wear rate limit for UZrH1.6. The limit depends on cycle length, which will vary with enrichment for each fuel type. The idea is that the wear rate limit for each fuel is determined at the enrichment that is expected to yield the most desirable economics. As will be revealed in Chapter 4, costs are minimized by using 12.5% UZrH 1 6 and 5% UO2. This approach ensures that the maximum power input to the economics analysis will be specifically adapted to the lowest cost fuels. Figure 3.17 shows the difference in the wear rate limits between the two fuels that causes the power discrepancy in the wear limited regions. The difference is quantified as the percentage by which the oxide limit is larger than the hydride limit. In the wear limited design regions, the percentage difference ranges from - 10% to 65%. 80 Figure 3.16 (Powertuo2 - Powertz,.Ii. 6) vs. P/D and Drod for Square Arrays at 60 psia with Vibrations and Wear Imposed Design Limits Core Power Difference (U0 2 - UZrH1 .6 ) (x 106 kWth) 2 1. 8 11 6 1. 1.4 ic z - 12 E E v iD - 3 4 E 2 7 1.1 1.15 1.2 1.25 1.3 P/D 1.35 1.4 1.45 1.5 Figure 3.17 Percentage Difference in Wear Rate Limits vs. P/D and Drod for Square Arrays at 60 psia Wear Rate Difference [(UO2 - UZrH1 .6 )/U 2] (%) 12 11 ., 1C 50 E 2 D~ 9 E I 1.1 1.15 1.2 1.25 1.3 P/D 1.35 1.4 1.45 1.5 81 3.6.4 Results at 29 psia for UZrH1. 6 The maximum achievable power for UZrH1 .6at 29 psia is shown in Figure 3.18 with vibrations and wear imposed design limits. The peak power geometry, occurring at P/D - 1.49 and Drod= 6.5 mm, is - 4245 MWth. This is unchanged from the peak power determined by the thermal hydraulic analysis without the vibrations and wear limits (See Figure 2.4). The ratios of the rod number, average linear heat rate, and power for the new geometries to the reference core rod number, average linear heat rate, and power are shown in Figure 3.19. Comparing with Figures 2.5B and 2.5C, it is evident that the regions where the hydride core has a higher power than the reference core have been reduced, though not as significantly as for the 60 psia pressure drop case. Note that the reference core's linear heat rate is not exceeded at any geometry. The difference in achievable power with and without the vibrations and wear limits imposed is plotted in Figure 3.20. The peak power reduction is - 1210 MWth, and occurs at a P/D - 1.23 and Drod= 12.5 mm. Figures 3.21 - 3.23 plot the familiar constraining parameters for the thermal hydraulic and vibrations analysis. MDNBR and pressure drop continue to constrain power for large regions of the design space. Because the axial velocities are lower at 29 psia, however, the wear limits are not as constraining on power as for the higher pressure drop case. This is most evident when comparing Figures 3.22A and 3.22B with Figures 3.8A and 3.8B. In fact, the fretting wear limit is never reached at 29 psia, and the region where the sliding wear constrains power is reduced. As expected, Figure 3.22C shows that no geometries have problems with fluidelastic instability. The vortex shedding margins are again plotted separately in Figure 3.23, along with the peak cross-flow velocity. As for 60 psia, VIPRE experienced difficulty converging to cross-flow solutions for P/D ratios less than - 1.2, and so the vortex shedding design limits were not imposed in this region. 82 Figure 3.18 Maximum Achievable Power vs. P/D and Drod for Square Arrays of UZrH .1 6 at 29 psia with Vibrations and Wear Imposed Design Limits Core Power (xl 06 kWth) 4 12 .35 11 I .9I 3 10 2.5 Q. 9 2 8 1.5 1 7 1.1 1.15 1.2 1.25 1.3 1.35 1.4 1.45 1.5 P/D Figure 3.19 Rod Number, Linear Heat Rate, and Power Ratios vs. P/D and Drodfor Square Arrays of IIZrH 1 6 at 29 psia with Vibrations and Wear Imposed Design Limits A: N/Nre f B: q/qf 12 12 1.5 11 2 1 8 1 8 .7 I0 7 a, 1.1 1.2 1.3 1.4 P/D C· 1.5 MD 10 1 0.5 1.1 1.2 1.3 P/D 1.4 1.5 I 12 1.5 11 10 0.5 8 I 7 1.1 1.2 1.3 1.4 1.5 P/D 83 Figure 3.20 Power(,{, vibrations) - Power(,ibrations)vs. P/D and D,od for Square Arrays of UZrH. 6 at 29 psia Core Power Difference (kWt) -I 1 5 13 11 12 11 q 10 Qa 5 8 7 J 1.1 1.15 1.2 1.25 1.3 1.35 1.4 1.45 1.5 P/D Figure 3.21 Thermal Hydraulic Constraining Parameters vs. P/D and Drod for Square Arrays of UZrH1.6 at 29 psia with Vibrations and Wear Imposed Design Limits B: W-3L MDNBR A: Pressure Drop (si) 12 25 I 11 12 -2.5 I 20 15 -3 10 10 8 5 7 I 1.1 1.2 1.3 P/D 1.4 n -3.5 8 7 -4 -u 1.'5 1.1 C: Axial Velocity (m/s) 1.2 1.3 P/D 1.4 1.5 D: Fuel CL Temoerature (C} o 0 12 12 I 11 700 11 600 C 8 7 1.1 1.2 1.3 P/D 1.4 1.5 I 2 500 8 7 400 1.1 1.2 1.3 P/D 1.4 1.5 84 Figure 3.22 Vibrations and Wear Constraining Parameters vs. P/D and D,.odfor Square Arrays of UZrH1 6 at 29 psia A: Fretting Wear Limit B: Sliding Wear Limit 12 12 I 11 0.8 8 7 I 0.8 11 0.6 10 0.4 ' 9 0.2 8 7 I In I 1.2 1.3 P/D 1.4 I 1.1 1.5 C: FIM 0.4 0.2 v 1.1 0.6 1.2 1.3 P/D 1.4 I0 15 1 12 I 11 0.8 10 0.6 9 0.4 .9 8 0.2 In 7 v '1.1 1.2 1.3 1.4 1.5 P/D Figure 3.23 Vortex-Shedding Margins and Peak Cross-flow Velocity vs. P/D and Drodfor Square Arrays of UZrH1. 6 at 29 psia D: VSM Drag (%) D: VSM Lift (%) 12 12 11 I I -100 -100 -200 1C ic -300 7 -400 1.1 1.2 1.3 1.4 -200 -300 8 7 1.5 P/D Peak Cross-flow Velocity (m/s) 1.4 1.5 I -400 P/D 0.3 0.2 0.1 10 Dro d (mm) P/D 85 3.6.5 Results at 29 psia for U0 2 The maximum achievable power for UO2 at 29 psia is shown in Figure 3.24 with vibrations and wear imposed design limits. The peak power geometry, occurring at P/D - 1.49 and Drod = 6.5 mm, is - 4245 MWth. This is unchanged from the peak power determined by the thermal hydraulic analysis without the vibrations and wear limits (See Figure 2.4), and is identical to UZrH1. 6 (see Figure 3.18). The ratios of the rod number, average linear heat rate, and power for the new geometries to the reference core rod number, average linear heat rate, and power are shown in Figure 3.25. Comparing with Figures 2.5B and 2.5C, it is evident that the regions where the oxide core has a higher power and linear heat rate than the reference core have been reduced. The difference in achievable power with and without the vibrations and wear limits imposed is plotted in Figure 3.26. The peak power reduction is - 589 MWth, and occurs at a P/D - 1.19 and Drod = 12.5 mm. The constraining parameters for the thermal hydraulic and vibrations analysis are plotted in Figures 3.27 - 3.29. MDNBR and pressure drop are the primary constraints. Like UZrH 1. 6, the fretting wear limit is never reached and the region where sliding wear constrains power is reduced because of the lower axial velocities. Figure 3.28C shows that fluid-elastic instability is not constraining for any geometries, and Figure 3.29 shows the vortex shedding results, where design limits were not incorporated for P/D ratios < 1.2 because of the cross-flow convergence problem. 86 Figure 3.24 Maximum Achievable Power vs. P/D and D,.odfor Square Arrays of lOz2 at 29 psia with Vibrations and Wear Imposed Design Limits Core Power (xl 06 kWth) 6 5.5 5 11 4.5 ,p 1C 4 A 35 8 c 3 2.5 8 2 1.5 7 1 11 1.15 1.2 1.25 1.3 1.35 1.4 1.45 1.5 P/D Figure 3.25 Rod Number, Linear Heat Rate, and Power Ratios vs. P/D and Drodfor Square Arrays of lJO2 at 29 psia with Vibrations and Wear Imposed Design Limits B: qqref A: N/N e f 12 3 11 ' r 12 1.5 11 10 2 I10 1 Q 9 8 7 1.1 1.2 1.3 P/D r P/ 1.4 1.5 I 0.5 I 7 0 1.1 1.2 1.3 P/f 1.4 1.5 12 1.5 11 10 1 0.5 :3 8 */ 1.1 1.2 1.3 1.4 1.5 I P/D 87 Figure 3.26 Power(n,, ibraltions) - Power(vibrations)vs. P/D and Drod for Square Arrays of U0 Core Power Difference (kWt) 2 at 29 psia x10 I1 11 10 -' 10 9 5 8 7 0 1.1 1.15 1.2 1.25 1.3 1.35 1.4 1.45 1.5 P/D Figure 3.27 Thermal Hydraulic Constraining Parameters vs. P/D and Drodfor Square Arrays of UO2 at 29 psia with Vibrations and Wear Imposed Design Limits A: Pressure Drop (psi) B: W-3LMDNBR 12 25 I 11 1.,0 15 9 I 20 12 I 11 10 -3 10 8 7 I 1.1 1.2 1.3 1.4 -3.5 8 5 7 0 1.1 1.5 1.2 P/D C: Axial Velocity-r (m/s) - 1.3 P/D 1.4 1.5 ) F l A1e TPmnPrnter.h C)f 8 12 12 I6 , 10 -2.5 I -4 1400 I 1200 11 1000 "1; 4 8 7 1 1.1 1.2 1.3 P/D 1.4 1.5 i 2 800 *9 8 600 7 I 400 1.1 1.2 1.3 1.4 1.5 P/D 88 Figure 3.28 Vibrations and Wear Constraining Parameters vs. P/D and D,.,rd for Square Arrays of U0 2 at 29 psia A: Fretting Wear Limit I B: Sliding Wear Limit 12 12 I '11 0.8 11 0.4 0.2 I0 7 1.1 1.2 1.3 PD 1.4 8 7 1.1 1.5 1.2 1.3 1.4 I 0.8 0.6 0.4 j I 0.2 0 1.5 P/D C: FIM 1 '11 I 0.8 11 0.6 1 I9. 2 0.4 0.2 I I0 1.1 1.2 1.3 1.4 1.5 PD Figure 3.29 Vortex-Shedding Margins and Peak Cross-flow Velocity vs. P/D and Drodfor Square Arrays of UO2 at 29 psia A: VSM: Lift (%) B: VSM: Drag (%) 12 I 11 -100 -200 I -200 10 -300 7 1.1 1.2 1.3 1.4 8 I -500 7 : P/D D: Peak Cross-flow Velocity (m/s) .. . .... 0:3 02]... od (mm) rod -400 1.1 1.2 1.3 1.4 I -500 1.5 P/D . . I. . ... . 0.1 01 12 -300 -400 1.5 -100 I -v I - -1 1.2 P/D 89 3.6.6 Comparison Between UZrH 1. 6 and UO2 at 29 psia Figure 3.30 shows the difference in maximum achievable power for UO0 2 and UZrH. 6 at 29 psia with vibrations and wear imposed design limits. As discussed in Section 3.6.3 the oxide fuel has a power advantage in the wear limited regions because of the more stringent wear rate limits applied to UZrH 1 6. Figure 3.31 shows the corresponding difference in the wear rate limits, quantified as the percentage by which the oxide limit is larger than the hydride limit, that causes the power discrepancy. In the wear limited design regions, the percentage difference ranges from - 20% to 50%. Figure 3.30 (Powero02 - PowertzrHl.6) vs. P/D and Drodfor Square Arrays at 29 psia with Vibrations and Wear Imposed Design Limits Core Power Difference (UO2 - UZrH1 ) 6 (x 108 kWth) 1.b 1 11 E E 0.5 (q O 1.1 1.15 1.2 1.25 1.3 P/D 1.35 1.4 1.45 1.5 90 Figure 3.31 Percentage Difference in Wear Rate Limits vs. P/D and D,0 d fior Square Arrays at 29 psia Wear Rate Difference [(UO2 - UZrH1 6 )/UO 2 ] (%) 80 12 70 11 Rn 50 103 4U 30 3 20 10 7 K. 1.1 1.15 1.2 1.25 1.3 P/D 1.35 1.4 1.45 1.5 3.6.7 Summary of Maximum Power Results With Vibrations and Wear Imposed Design Limits Table 3.6 summarizes the steady-state thermal hydraulic results for UZrH 1 6 and UO2 at 60 psia and 29 psia with vibrations and wear limits imposed. Three geometries are considered: the peak power geometry, the reference core geometry, and the geometry at the reference pitch offering the maximum power. This last one is chosen because of its relevance to the minor backfit scenario considered later in the economics analysis (Refer again to Section 1.2 for a definition of minor backfit). Note in examining the results in Table 3.6 that the predicted power for oxide at the reference core geometry is - 3800 MWth at 60 psia, and 3420 MWth at 29 psia. As discussed in Chapter 2, the reference core geometry is MDNBR limited, and so the predicted powers should be independent of the pressure drop limit. The vibrations analysis is not expected to impact it either because the wear limits are based on maintaining the same margin for cumulative fretting and sliding wear as the reference 91 core. The power is correctly predicted, however, only for the higher pressure drop limit. There are three primary reasons for this. First, the reference core geometry is not directly included in the parametric analysis, and so all data for this configuration must be interpreted from output at nearby geometries6 . Second, there is a convergence limit of 1% for all thermal hydraulic design limits, which means that the peak power is reached when the constraining parameter is within 1% of its respective limit (i.e., when the MDNBR is less than or equal to 1.01 x 2.173 = 2.194). This causes the power to be slightly lower than if the limit were perfectly met. A convergence limit is necessary, however, to expedite execution of the programs. Finally, the interpolation technique employed introduces error (i.e, linear, cubic, spline, etc.), which combined with the convergence limit, causes the predicted power for the reference core geometry to deviate from its true value. The exact reason the discrepancy is only apparent at 29 psia is unknown, although it most likely has to do with interpolation error with the lower powers at 29 psia. Another reason may be that the reference core geometry at 29 psia is limited by two thermal hydraulic design limits (MDNBR and pressure drop). If the code converges to the pressure drop limit first, than the convergence limit's impact on power will be more significant than for the higher pressure drop case (where only MDNBR constrains the reference core power). 6 The parametric study considers 20 equally spaced rod diameters between 6.5 and 12.5 mm, and 20 equally spaced P/D ratios between 1.08 and 1.55. The reference core geometry is not part of this design range. 92 Table 3.6 Summary of Steady-State Thermal Hydraulic Results with Vibrations and Wear Limits 60 psia Power (MW,) Q/Qref q/qref UZrH 1. 6 5017 1.32 0.66 1.37 6.5 Pea2 5045 1.33 0.66 1.37 6.5 UZrH.6 3471 0.91 0.91 1.326 9.5 UO 2 Ref. Geom 3821 1 1 1.326 9.5 Ptch UZRef. Ref. Pitch 3503 0.92 0.92 1.3 9.66 Ref.Pitch 4066 1.07 1.07 1.264 9.97 Peak Power Peak Power Ref. Geom Ref. Pitch P D (mm) 29 psia Power(MW,) Q/Qref q'/qef P/I D (mm) 4245 1.12 0.66 1.49 6.5 4245 1.12 0.66 1.49 6.5 .6 UZrH.1e3332 0.875 0.875 1.326 9.5 UO 2 Ge3420 Uf2 0.9 0.9 1.326 9.5 UZrH 1 .6 kUZrH.6 Peak Power UO 2 Peak Power UZrH Ref. Geom Ref. Geom UZrH 1. 6 UZrH.6 3314 0.875 0.875 1.3 9.66 U0 2 Ref. Pitch Ref. Pitch 3511 0.924 0.924 1.3 9.66 Ref. Pitch 3.6.8 Extension of Vibrations Results to Hexagonal Arrays The vibrations and wear analysis was only performed for square array designs. It is believed, however, that the results can confidently be extended to hexagonal geometries supported by grid spacers. Recall from Chapter 2 that the maximum power obtained for square and hexagonal array geometries for matching rod diameters and H/HM ratios was found to be the same. This is because the flow areas are identical per unit rod, and minor differences in the turbulent interchange of mass, momentum, and 93 energy and the friction factor between the two configurations do not significantly impact the overall power. For equivalent geometries, square and hexagonal arrays will therefore have the same mass flux, flow area, and average axial velocity. Because the vibrations limits that constrained power for square arrays involved sliding and fretting wear, and wear is dominated by the axial flow, it is expected that the maximum achievable power for hexagonal arrays subject to vibrations and wear limits will be identical. If in the future wire wrapping is used in hexagonal designs (i.e, for tighter geometries where a pressure drop benefit can be realized), then a separate analysis will be required to verify that flow-induced vibration limits are not exceeded. J. Trant has provided some preliminary information on this in his thesis [3]. 94 95 4. Economics Analysis of Hydride and Oxide Fueled PWRs 4.1 Introduction For energy production technologies, the cost of electricity (COE) is used to make comparisons and guide investment decisions among competing options. To this end, an economic analysis is performed to identify the optimum PWR geometries using UZrH1.6 and UO2 fuels, and provide a fair basis for their comparison over the design range of the parametric study. In this chapter, an economic model is developed and applied to both fuel types with inputs from recent work in thermal hydraulics and fuel design. While results are presented for UZrH 1. 6 and UO2, the model can be easily adapted to other hydride fuels. Specific assumptions are made regarding plant and fuel costs and the economic parameters that influence them over time. Due to these assumptions and the numerous models available for both collecting and interpreting economic information for nuclear facilities, the cost of electricity (COE) results may not necessarily appear consistent with the financial accounts of utilities. Because the model is equally applied to UZrH .1 6 and UO 2 fuels, however, cost comparisons can be made with less regard for the specifics of the modeling techniques and any discrepancies with commercial records. 4.2 Work Scope 4.2.1 Goals of the Economics Analysis The COE is broken into three cost components: fuel cycle, operations and maintenance (O & M), and capital costs. The economics analysis seeks the COE via these components for square and hexagonal array PWR designs using UZrH 1. 6 and UO2 fuels. Results are presented for both fuels at enrichments of 5%, 7.5%, and 10%. Results are also presented for 12.5% enriched UZrH.1 6. The Hydride Fuels Project aims to quantify the benefits of hydride fuel use in existing LWRs for two cases: 96 * Minor backfit, where the plant modifications required for fuel conversion are minimized by maintaining the existing fuel assembly and control rod configurations within the pressure vessel (i.e., maintaining the same pitch and rod number in the core). In this case, replacement of the steam generators and modifications to the high pressure turbine are required to accommodate designs offering higher powers than the reference core; * Major backfit, where the layout of fuel in the core can assume any geometry. Note that in addition to upgrades of the steam generators and high pressure turbine, this option will require replacement of the vessel head and the core internals to accommodate the new layout of fuel assemblies and control rods at increased power. The final COE results are used to identify optimum geometries where the overall costs are minimized, and where the use of UZrH1.6 fuel offers cost savings over U0 2. In addition to presenting cost estimates, the economics analysis provides important information for utilities considering the fuel switch from UZrH .1 6 to U0 2. For example, the operating cycle length, plant capacity factor, annual energy production and outage length are all byproducts of the COE calculations. 4.2.2 Methodology The structure for the economics analysis was laid out by a former MIT student, Jacopo Saccheri [8], and is consistent with OECD/NEA reports on the economic evaluation of nuclear fuel cycles [9]. The primary inputs include the maximum power from the steady-state and transient thermal-hydraulic analyses, and the maximum burnup from neutronics and fuel performance studies. The fuel cycle, O & M, and capital costs are then determined for each geometry and fuel type. 97 4.2.2.1 Lifetime Levelized Cost Method The methodology employed is the lifetime levelized cost method, which determines the levelized cost of electricity per unit of energy produced over the plant's lifetime. It is also called the levelized busbar unit cost of electricity, to reflect that all expenses up to the plant/transmission line interface are included. The term "levelized" simply means that the costs, originally incurred at discrete times, are transformed into one equivalent, continuous stream of expenditures. This method therefore allows direct comparison of alternatives having vastly different cash flow histories. The basic equations relating discrete cash flows and levelized costs are presented in the following paragraphs. In order to charge the correct price for service, a utility must first decide on the rate of return on investment, r, that is desired. The rate of return is also commonly called the discount rate, or nominal interest rate. Discrete expenditures for fuel cycle, O & M, and capital costs are incurred at different times during the plant's life. To get the levelized cost, these expenditures are discounted back to a reference date, which is chosen to be the start of irradiation for the first fuel cycle (i.e., t = 0). Discounting all expenditures to this date with continuous compounding of interest yields the present value of all costs, PVos, PVcoss= and a relationship with the lifetime levelized cost, Clev. .'Ce e-rtdt 'CN e -rN = P (4.1) N where, CN: TN: N h discretecashflow time relative to the ref date for the Nh discrete cash flow Tpant,: plant life In addition to the discount rate, an escalation rate, g, can be included for recurring cash flows to account for non-inflationary price increases with time. Rewriting equation (4.1) to include this cost escalation effect yields: PVCot= E CN e - rTN =E N CT ePlant .e-rtdt (4.2) N where, Co: jSt discretecashflow at referencedate 98 Integrating equation (4.2) with respect to time and solving for the lifetime levelized cost yields: Clev = P coss [1- r (4.3) where: capitalrecoveryfactor [1 (4.4) eplnl The capital recovery factor, or carrying charge rate, relates the lifetime levelized cost of electricity, Clev, to the present value of all expenditures. It correctly accounts for the time value of money at the desired rate of return on investment. The lifetime levelized unit cost of electricity, CIev,is obtained by normalizing Ce by the energy production from the plant. If energy production is assumed to occur at a uniform rate over time, the lifetime levelized unit cost is simply the levelized cost ($/yr) divided by the annual energy production (kW-hre/yr). The annual energy production, Eannual,from the plant is: (4.5) Eannua,, = th .-. L.8766 where: Q,h: core thermalpower a: plant thermal efficiency L: plant capacityfactor The final relationship for the lifetime levelized unit cost of electricity is given by the quotient of equations (4.3) and (4.5): _ Clev Eannual L 8.766 (4.6) rTp PVcosts th *77 1-e . If costs and the power are recorded in $ and kWth, and interest rates are annualized (yr-l), then equation (4.6) reports the levelized unit COE in mills/kW-hre, the desired units for this analysis. To get the individual levelized unit costs for the fuel cycle, O & M, and capital components, equation (4.6) is applied with the relevant cash flow 99 histories incorporated into the PVc,,, term. The levelized unit COE is simply the sum of the cost contributions from these individual components. Clev = Clev-fcc + Clev-O&M + Clev-cap (4 7) The details of the cash flow histories for fuel cycle, O & M, and capital costs are presented in Section 4.5. 4.3 Assumptions The lifetime levelized cost method relies on accurate predictions for nuclear costs and the terms under which they are financed (i.e. rate of return) for the length of plant operation. Forecasting these costs and conditions, however, is a difficult task. For example, economists are hesitant to project long term nuclear fuel prices, plant O & M costs, and the rate of return on capital demanded by nuclear investors because of uncertainties in the future accessibility to uranium at world prices, the quality and quantity of tomorrow's nuclear work force, and the future of energy market competition. With the hiatus on nuclear construction orders in the US approaching 25 years, significant debate also exists over many of the current cost estimates for constructing new or upgrading existing plants. The use of hydride fuel, which is new to commercial reactors, will undoubtedly involve costs that are not currently accounted for in the three component COE model. Because of the uncertainty and the speculative nature of most long term cost projections for nuclear power, several assumptions are necessary to keep this analysis simple and ultimately focused on the comparison of UZrHI.6 and UO2 performance in PWRs. Only direct costs associatedwith thefuel cycle, 0 & M, and capital are considered: The use of hydride fuels commercially will involve additional firstof-a-kind (FOAK) costs that accompany the introduction of new technologies within the nuclear realm. Examples include fees associated with NRC licensing and certification, research and development, and plant design. Because FOAK 100 costs are only incurred once, this economics analysis will focus on the Nthhydride plant, where the 3 component COE model sufficiently covers all costs. * Discountand escalationrates are constantover theplant's life: The discountrate can be thought of as the sum of three components: a basic market growth rate, an inflation rate, and an allowance for risk. The risk allowance portion scales with investment risk which, for nuclear power, tends to be higher than for other energy technologies because of the greater probability for investment loss. The market growth and inflation rate portions are less dependent on the specific technology and more heavily tied to the state of the overall economy. All three components fluctuate in time, and it is beyond the scope of this report to either analyze or attempt to predict this variability. As a result, a fixed discount rate of 10%/yr is chosen to account for all three components. Similar arguments can also be made for the escalation rates used to project non-inflationary price increases for fuel cycle and O & M costs. Their contribution will also be assumed constant at 1%/yr. Because considering discount and escalation rate variability would have the same impact on both fuels, this assumption is expected to have little impact on the final economic comparison. * Interest is compounded continuously: Because the lifetime levelized COE represents a continuous stream of expenditures, the escalation and discount rates are compounded continuously through time for all cost calculations. * The unit cost information available for commercial PWRs is cautiously extended to new hydride and oxidefueled designs: The unit costs for the fuel cycle, O & M, and capital portions of the COE analysis are widely available for existing PWRs using UO2 fuel. Several of the unit costs, however, require modification to accommodate: UZrH1. 6 fuel, for which no economic data is currently available, and the large range of geometries considered in this study that deviate significantly from standard PWR designs. The details of the assumptions are left for Section 4.4.3. 101 4.4 Inputs The primary inputs to the economics analysis are presented in this section. They include the maximum power from the steady-state and transient thermal-hydraulic analyses, the maximum burnup from the neutronics and fuel performance studies, and specific unit cost estimates for front and back end components of the fuel cycle, O & M activities, and plant capital. 4.4.1 Maximum Power The vibrations analysis in Chapter 3 completed the steady-state thermal-hydraulic analysis for maximum power in square and hexagonal array PWR cores using UZrH.6 1 and UO2 fuels. Parallel to this work, another MIT student J Trant [3] performed a transient analysis for the same core designs, in which additional limits were imposed on the maximum achievable power. The transients considered were the loss of coolant, loss of flow, and overpower events. Each is briefly discussed below. * Loss of Coolant Accident (LOCA): The LOCA postulates a break in the primary coolant loop, at which point the pressurized fluid flashes to steam and blows down into the containment structure. Though the control rods are immediately driven in to stop the nuclear reaction, decay of fission products provides a continued heat source that must be removed to protect the integrity of the clad and fuel. LOCA performance is evaluated by considering the time history of the peak clad temperature following the steam line break. As long as the peak clad temperature for new designs remains below the peak clad temperatures for the reference core at each time step, the LOCA is not limiting. Because the clad temperature is driven by the decay heat in the fuel, which depends on the steadystate power prior to the accident, a design that exceeds the LOCA limit can be made acceptable by reducing the steady-state power in the core. * Overpower Transient: The overpower transient postulates a rod bank withdrawal during steady-state operation, which causes a sudden increase in power (assumed to be 18% of the steady-state power), which may lead to DNB. Like the steady102 state thermal hydraulic analysis for maximum power, DNB performance during transients is measured by the MDNBR. The overpower design limit is therefore the MDNBR of the reference core during the overpower event. If the limit is exceeded, the steady-state power is reduced until the design is acceptable. Loss of Flow Accident (LOFA): The LOFA postulates a loss of flow in the primary coolant loop, which, depending on the power and flow conditions in the core during coast down, may also lead to DNB. The LOFA design limit is therefore the MDNBR for the reference core during coast down. If the limit is exceeded, the steady-state power is reduced until the design is acceptable. The transients and their respective design limits are summarized in Table 4.1. Table 4.1 Transient Analysis Summary Transient Constrained Parameter LOCA Peak cladding temperature LOFA MDNBR Overpower MDNBR Design Limit * The time history of the peak clad temperature following a LOCA for the reference core * The MDNBR during coast down for the reference core * The MDNBR during an 18% overpower transient for the reference core The transient analysis yields new maps for maximum power. The thermalhydraulic input to the economics study is the most limiting power reported by either the transient or steady-state analyses, for each geometry. Because of differences in the vibrations and transient performance, discrepancies exist between the maximum achievable powers for UZrHI.6 and U0 2 fuels. The final power maps incorporating the steady state and transient design limits are presented below for square arrays. Recall from Chapter 2 that the thermal hydraulic performance for square and hexagonal arrays is identical for equivalent rod diameters and H/HM ratios. The hexagonal array results can 103 therefore be inferred from the figures by adjusting the P/D ratio according the following relationship: (/D)hex = 1.0746 (P/D),q. Figures 4.1 and 4.2 show the maximum achievable powers at the 60 and 29 psia pressure drop limits for square arrays of UZrH .1 6 and UO2. The peak powers, as shown in the plots, are the same for both fuels and occur at: P/D - 1.39, Drod = 6.5 mm for 60 psia, and P/D - 1.49, Drod = 6.5 mm for 29 psia. The peak powers are very close to the peak powers reported by the steady-state thermal hydraulic analysis (See Figures 3.4, 3.10, 3.18, and 3.24). As discussed in Chapter 3, more stringent wear rate limits lead to additional power reductions in the wear rate limited regions for UZrHi.6; this is particularly evident when comparing the crest of the maximum power regions below. Figures 4.1 and 4.2 also show the regions (shaded in white), where the steady-state power has been further reduced by transient limits. Figure 4.1 Maximum Achievable Power and Transient Limited Regions vs P/D and D,.odfor Square Arrays of UZrH1.6 and U0 2 Incorporating Steady-State and Transient Design Limits at 60 psia Power TJZrH (xl o6kW Power UTO (xl 06 kW.) _ _D a C0 1 11 I iQ 1.1 1.2 1.3 1.4 5 4 14 P/D Transient Limited Region: UZrH 4 '1 3 3 2 2 I 1.5 5 1 1 1.1 1.2 1.3 15 1.4 I i P/D Transient Limited Region: UO, 6 12 11 o10 .0 1.0 Q Q 1.1 1.2 1.3 P/D 1.4 15 1.1 1.2 1.3 1.4 1.5 P/D 104 Figure 4.2 Maximum Achievable Power and Transient Limited Regions vs P/D and Drodfor Square Arrays of UZrH1.6 and U0 2 Incorporating Steady-State and Transient Design Limits at 29 psia Power UZrH . 6 (xl 06 kWth) Power UO2 (xl 06 kWth ) _Q 6 1 12 12 5 -11 5 11 4 10 3 8 I 7 1.1 1.2 1.3 1.4 4 3 E~ 2 2 P/D - [ 12 11 11 . 10 10 rrV__: ; 9 8 8 7 7 13 P/D 1.4 1.5 1. Transient Limited Region: UO, 12 1.2 14 1.1 P/D Transient Limited Region: UZrH, ,O. 11 I1 1I 1.5 9.0 -. 0 1.1 1.2 1.3 1.4 i. 1.5 P/D 4.4.2 Fuel Burnup Similar to the transient and steady-state approaches to maximum power, the achievable burnup for UZrH 1 6 and UO2 fuels depends on the results from two separate and independent analyses. Performed at UC Berkeley and MIT, the analyses seek the maximum discharge bumup subject to neutronics and fuel performance constraints, respectively. Results from both are presented in this section. As in the case of maximum power, the input to the economics analysis is the minimum discharge burnup reported by either the neutronics or fuel performance studies for each geometry. Note that the bumup is determined independently of cycle length, which is considered variable in this economics analysis. 105 4.4.2.1 Neutronics The neutronics analysis serves two roles. First, it provides the maximum burnups for hydride and oxide fuels that can maintain the critical nuclear reaction in the core. Second, it provides the range of geometries with acceptable (negative) fuel and moderator temperature coefficients. UC Berkeley employed SAS2H, which is part of the SCALE module, to determine the unit cell 3-batch burnup for UZrH1. 6 and U0 2 fuels as a function of pin geometry and fuel enrichment. The maximum burnup is reached when the core average K, drops below 1.05. The margin of 0.05 is provided to account for leakage. Results for square arrays are presented in Figures 4.3 and 4.4. As expected, higher burnups are obtained for higher enrichment fuels. Note the difference in the curve shapes for hydride and oxide fuels. The addition of hydrogen to the fuel matrix shifts the optimum geometries to tighter configurations, because less coolant is needed for neutron moderation. The neutronics performance depends primarily on the H/HM ratio, and so the neutronically constrained burnups for hexagonal arrays can be inferred from the square results for matching rod diameters and H/HM ratios. 106 Figure 4.3 Neutronically Achievable Burnup vs. P/D and Di.d for Square Arrays of UZrH.6 Fuel 5% (MWD/kgHM) 40 7 5% (MWDkgHM) i 35 10 0 I 1.5 ROO(mmM8 10% (MW/kg H,M) 110 ' 48 80 78 46 75 76 44 70 74 42 65 12 72 40 10 DROD (mm) 8 I 106 105 150 . 104 130 120 95 102 110 I 130 DRo (mm) 8 60--: 40- 40 . 0 12 , . . . ---: 2... IV'" DROD (mm)8 1.1 . . 20 . >- " 30 . . for Square Arrays UO2 Fuel Drod . 100 80 , I 120 1.3 1 7.5% (MWD/kgHM) 60 50 20 125 . Figure 4.4 Neutronically Achievable Burnup vs. P/D and 5% (MWD/kg HM) 135 . 1" 100 70 140 . . 100 13 I *. :. .;.-;' 140 DRCD(mm)8 P 12.5% (MWD/kgHM) 108 - 1.5 1 1.3 1..5 P/D I 10 . M" . 80 . - ; -: 60 40 60 20 1" "~ . 1.3 1.1 P/D NvL~ DROD (mm) 8 .5 40 A I 10% (MWD/kg HM) .'.-: '. 110 120- - 100 nn ' -1 IUVVU 90 80 80 60 70 12 ' * · . OD (mm)D '8 1.1 .. P/D I PtD6 .5 I 60 107 The range of geometries with acceptable temperature coefficients for UO2 is: 1.0738<(P) D sq () , <1.4 1.5 6 .5<Drod <12.5mm Drod < 8.5mm sq All other geometries in the parametric study are unacceptable. Unfortunately, the outlook for UZrH,.6 is not as optimistic. No geometries considered in this parametric study had negative moderator temperature coefficients (MTC). The cause is the large amount of soluble boron needed in the coolant to combat the excess reactivity in UZrH 1.6. UC Berkeley is currently investigating ways to resolve this issue. Possible solutions include introducing thorium into the fuel matrix, and using different burnable absorbers to reduce the amount of soluble boron required. Only the former has been considered in detail, and preliminary results indicate that utilizing UZrHi.6-ThH2 provides a large design range with acceptable temperature coefficients. In light of this information, the economic optimization is continued in this chapter for UZrH1. 6 because it is believed that the poor MTC performance can be improved. It is also important to firmly establish the optimization methodology because it applies to all hydride fuels. 4.4.2.2 Fuel Performance In addition to reactivity considerations, the discharge burnup is also limited to protect the integrity of the fuel pin during irradiation. In the fuel performance analysis, design constraints are placed on: internal fuel pin pressure and fission gas release, clad strain, and clad oxidation. Each is briefly discussed below. Internal Pressure: Gases generated during the fission process are originally trapped in the fuel matrix. As the fuel heats up, this gas is released into the plenum space, where it exerts an outward force on the pin. This may cause outward creep and ballooning of the clad, and a rise in the conductance across the pellet/clad gap. With more resistance to heat transfer, the fuel temperature rises 108 and more fission gas is released into the plenum. The potential therefore exists for a positive feedback loop that can severely damage or even burst the pin. Gases are also generated when burnable poisons are used to compensate the negative reactivity effects of fuel depletion. The fission gas and burnable poison contributions to overall fuel pin pressure need to be taken into account. * Clad Strain: Clad strain is predominantly the result of three mechanisms: external coolant pressure, differential thermal expansion between the fuel and clad, and fuel swelling due to irradiation and the accumulation of fission gas in the fuel matrix. Excessive strain can induce failure of the pin. * Clad Oxidation: The outer surface of the clad is continuously oxidized by primary coolant during irradiation, and can lead to both material and thermal degradation of the cladding material. For example, a thickening oxide layer reduces the wall thickness, possibly rendering the clad unfit to withstand the stresses and strains imposed on it. Oxide buildup increases the thermal conductivity of the clad; this raises its temperature and accelerates the rate of oxidation. For Zircaloy materials, the oxidation process also generates hydrogen, which migrates into the clad to form platelets of zirconium hydride. These platelets embrittle the material, deteriorating its mechanical properties. With guidance from industry, design limits were quantified for each fuel performance constraint; these are listed in Table 4.2. Table 4.2 Fuel Performance Limits for Maximum Burnup 11] Fuel InternalPressure (psia) Clad CorrosionThickness CladStrain (mm) (%) U02 .01 1.0 (tension) 2500 UZrH.6 Note that the limits on clad corrosion and strain apply equally to UO2 and UZrH1.6 fuel rods. The internal pressure limit, however, is neglected for hydride fuel pins because of low fission gas generation. 109 The maximum burnup with fuel performance imposed design limits is evaluated using the FRAPCON code, which simulates the thermal-physical properties of U0 2 fuel pins under steady-state conditions. The input requirements for FRAPCON include core geometry, peak linear heat rate, and mass flow rate. All are provided by the steady-state thermal hydraulic analysis7. For conservatism, the fuel is assumed to operate at the peak linear heat rate in the core, and the code progressively outputs clad strain, oxide layer thickness, and pin pressure as a function of burnup. The maximum burnup is achieved when one constraint reaches its limit, and the others remain below their respective limits. Because FRAPCON can only be used to simulate burnup in UO2 fuel, additional assumptions were required to extend its use to UZrH1 .6. * The internal pressure constraint was neglected due to the low fission gas release. * The thermal expansion properties of the fuels, which affect clad deformation and the limit on clad strain, were assumed to be identical. T The fuel performance limit that dominates over most of the design range is clad corrosion, which depends on the amount of time the fuel remains in the core. Because the heavy metal loading in U0 2 is 2.5 times greater than UZrH 1.6 at the same geometry, the residence time for UZrH .1 6 will be 40% of the residence time for UO2 if the same burnup limit is applied. It is therefore assumed that an equivalent FRAPCON burnup for UZrH 1.6 can be obtained by multiplying the output from the code without the internal pressure constraint by, 2.5. This ensures that the residence time for both fuels in the core at discharge will be the same. Of the three, the second assumption is the most difficult to justify, but its impact is minimized because clad oxidation limits most geometries. Because the FRAPCON analysis was performed before the transient limits were applied to the maximum power, they are not incorporated into the maximum burnup results. This adds conservatism, however, because the discharge burnup would increase if transient limits on core power were imposed. 7 110 The FRAPCON analysis was undertaken by a recent MIT post-doc, Antonino Romano. The following figures show the maximum burnups for square arrays of UZrH 1.6 and UO2 at both pressure drop limits, subject to fuel performance design constraints. Because the FRAPCON burnup depends on the output from the thermal hydraulic analysis, the hexagonal results can once again be inferred by adjusting the P/D ratios. The fuel performance limited burnup, unlike the neutronics analysis, is independent of enrichment. Note the large indentations in the oxide curves at both pressure drop limits that occur in the regions of higher power. The same effect is not observed in the hydride figures because the limiting constraint is internal pressure. Figure 4.5 Fuel Performance Limited Burnup vs. P/D and Drod for Square Arrays of UZrH. 6 and UO 2 at 60 psia UZrH, ; (MWD/kg9M) UO2 (MWD/kgHS '. "- : ' 200 - 180 200,, : .' ..' .. 60 150., . 140 14 120 50 100. 50 40 '. 100 12 /4 15 *80 13 12 """ rod ...... - PID 5 30 cn U 11 11 .:,:':, Figure 4.6 Fuel Performance Limited Burnup vs. P/D and Drodfor Square Arrays of UZrH. 6 and UO 2 at 29 psia IJZrH 6 (MWD/kg HM ) UJO (MWDkHM) 200 2 . 200 -:- . : 180 , 160 150 140 100 , 120 50\ 15 , 12 100 n rod ....... 3 8 -. _ 12 1.1 PD PD 14 80 o80 .. 80. 80.:- ,:i . 60. 75 : , 70 , 65 60 55 '' 40, 50 45 20. 12 - Dro d (mm) 8 r- h1 11 14 0.I r1 ;i1 114 2 P/D 15 5 40 35 30 111 The maximum achievable bumup for UZrHi.6 and U0 2 fuels is the minimum bumup reported by the neutronics or fuel performance studies. Figures 4.7 - 4.10 present the combined results as a function of enrichment, pressure drop, and geometry for UO2 and UZrHi. 6. With the exception of very small rod diameters and P/D ratios, the burnup for tJZrH 1 .6 is limited by the neutronics. UO 2 is limited primarily by neutronics for smaller P/D ratios, and fuel performance for larger P/D ratios, though as the enrichment increases fuel performance takes on a more dominant role. Figure 4.7 Maximum Achievable Burnup vs. P/D and D,,d for Square Arrays of UZrHi. 6 at 60 psia A: 5% UZrH 6 B: 7.5% UZrH .6 (MWD/kgH ,,,) (MWD/kgHM) VIM' 50 48 80 45 46 70 - . 44 60 42 50 40 12 Dd (mm) 8 35 12 10 8 Dd (mm) 1.4 1 2 P/S I 75 70 65 ; 60 D: 12.5% UZrH C: 10% UZrH 1 6 (MWD/kgHM) I 55 1.2 P/D (MWD/kg,, , ,) 140 . 100 . 120 I . 90 80 70 I 60 . .. ., 100 . 50 100 80 ; 12 (mm]Q 'rod """' . I 1 60 P/D 112 Figure 4.8 Maximum Achievable Burnup vs. P/D and D.od for Square Arrays of UZrHI. 6 at 29 psia A: 5% UZrH1 6 (MWD/kgHM) B: 7.5% UZrH 16 16 (MWD/kgHM) 45 40. - I 35 12 Drd (mm) 8 48 78 46 76 74 44 72 42 70 40 I 68 12 P/D D: 12.5% UZrH , (MWD/kg,,,) C: 10% UZrH 1 6 (MWD/kgHM) 140 100 110 . - 90 -- 80 : : 100 . 80 50:; 70 - )8 12 150 120 100 90 12 rod(mm) 12 PD I 70 100 .o , 10 n /mm \ umd " _ 14 I .Z P/D Irrrrio I 80 Figure 4.9 Maximum Achievable Burnup vs. P/D and Drod for Square Arrays of U0 2 at 60 psia A: 5% UO 2 (MWD/kgHM) 60-- : : B: 7.5% UO 2 (MWD/kgHM) -. I , 40 40 20 30 40 20 20 1. 1.4 .2 P/D D_, ,. C: 10% UO 2 (MWD/kgHM) 80 1-' i- I 60 0U 50 40 Dod(mm) 8 1.2 P/D I 30 80 70 : 60 40- 50 40 20- ; Drod (mm) 8 70 .I IA u 60- 12. - ---, ' 1. 30 1.2 P/D 113 Figure 4.1) Maximum Achievable Burnup vs. P/D and D,.,d for Square Arrays of UO2 at 29 psia A: 5% UO 2 (MWD/kgHM) 60--'"' '-, . B: 7.5% UO . . 50 ~ A| - awn 401 -v 20 - . 1. 4 . 12 C: 10% U0 2 (MWD/kgHM) 80 - . . ' -iH i , . 80 - ~ cn, I OU - 30 40'4 20 12 I 10 1.2 P/ Dd (mm) 8 (MWD/ka,.. '- - . '. . 11 'dk...- ou 70 . 60 uu-~~~~~~~~~~~' 50 40 120 II ~ ", - 14 '. PD 1 I 30 dU 70 60 40 12 D,,d(mm) 8 j.t . ' 50 40 -. ' 1.2p/D I 30 4.4.3 Economic Parameters This section presents the unit cost information and plant operating parameters necessary to determine the cash flow histories for the fuel cycle, O & M, and capital cost portions of the economics analysis. 4.4.3.1 Fuel Cycle Unit Costs The nuclear fuel cycle has costs associated with procurement and fabrication of fuel assemblies, and storage and disposal of spent fuel. For this analysis, this data is derived from two sources: the June, 2004 US spot market for uranium services, and OECD/NEA recommendations [9]. 114 Table 4.3 PWR Fuel Cycle Unit Costs for U0 2 Cost Component Symbol Unit Price Mining/Ore Core $4 l/kgHM Conversion Cconv $8/kgHM Cenr,SWU $108/kgswu* Enrichment Cfab $ Temporary Spent Fuel Storage Cstor $ Waste Disposal Cdisp 275 Fabrication 25 /kgHM 0/kgHM 1 mill/kW-hre * Separative Work Units (SWU) are a measure of the amount of work necessary to separate the enrichment plant feed into the desired enriched product and a depleted waste stream. Determining the mass of SWU required to achieve a desired enrichment is discussed in Section 4.5.1.3a. 4.4.3.1a Fabrication Costs for UO2 The unit fabrication cost is given with respect to the unit mass of heavy metal and is based on the cost to manufacture fuel assemblies for commercial PWRs. It has been suggested by industry experts, however, that as much as 50% of the total fabrication cost depends on the number of fuel rods in the core. Therefore, to account for geometries offering larger and smaller numbers of fuel rods than the reference core, an adjustment is made to the unit fabrication cost via a scaling factor. This scaling factor depends on both the portion of fabrication costs that scale with the rod number, x, and the difference between the number of rods in a new geometry, N, and the reference core, Nref. The new unit fabrication cost for oxide fueled cores is given by: Cfab,oxide Cfab (-X) +(Cfb 'X) 1+ Nref LKrefrel11 (4.8) (4.8) Simplifying the expression yields: Cfab,oxide = Cfab + (Cfb x). N-N ref Nre Nref 1 (4.9) Assuming that x = 50%, the unit fabrication cost and rod number are shown in Figure 4.1 1 for square arrays of UO2. The unit fabrication cost and rod number for the reference core are denoted by black lines. 115 Figure 4.11 UTnitFabrication Cost and Rod Number vs. P/D and D,odfor Square Arrays of tO 2 UnitFabrication Cost($/kgrM) - -I- , I· . RodNumber(x 14) * . *15 114 ~Enn Mr 600 450 15 12 400 10 10 - . 350 5 '-8 5 300 2250 1 I! 500 400 _ 300 8 200 1.5 1.3 I1-2-Of P/D 1.1 - 9 1-00o 12.5 I h ~1C"0200 PD 1.1 12.5 65 4 4.4.3.1b Fabrication and Storage Costs for UZrH1 .6 The mining, conversion, and enrichment processes are independent of the fuel type, and so their associated unit costs are identical for UZrH. 6 and UO2 fuels. The fabrication cost, however, is based on the specific chemical processes necessary to manufacture 1JO2fuel pellets from enriched UF6 gas, and so does not apply to UZrH 6. With no cost information available from industry, the fabrication cost must be approximated. An assumption is therefore made that the fabrication costs for UZrHt. 6 and UO2 are identical for equivalent volumes of fuel. The unit fabrication cost for UZrHI 6 is therefore given by: (4. l.oxide 'Poxide C(W'HA (fib.hdride = (4.10) fihaoxide M'[Li hydride Phyvdride where, wMHt: weightpercent heavy metal in the fuel matrix p: fuel density The unit fabrication cost for UZrH. 6 is therefore larger than oxide because of its lower heavy metal content. Assuming again that x = 50%, the unit fabrication cost and rod number are shown in Figure 4.12 for square arrays of UZrH 1 .6, with the values at the reference geometry denoted by black lines. 116 Figure 4.12 Unit Fabrication Cost and Rod Number vs. P/D and D,.,dfor Square Arrays of UZrHi.6 UnitFabrication Cost($/kIk Rod Number(x 1i) 16 1400 - . ~~~~~681 :" . I DUU I , . . . . .-: 50952 . 14 1200 1000 1000 15 12 10 10 5 8 800 500 - 1 65 8 1;.5,@h PID 1 2 ' :", 600 0 1 65 6 4 11 1F1 12 5 Like the fabrication costs, the unit cost for UO2 spent fuel storage is based on the heavy metal content in the fuel. Assuming that storage costs are dominated by the availability of space in the spent fuel pools and dry cask storage, storage costs for UO2 and UZrH 1. 6 should be identical for equivalent fuel volumes. The same relationship used to relate the unit fabrication costs is thus applicable to the unit storage costs: 'H WH.oxide 'Poxide L stor.hlldride-=- stor.oxide' / I II (I . I 'HAhvdride ' Phydride 4.4.3.2 Operations and Maintenance Unit Costs O & M includes all costs associated with energy production that are not directly related to the fuel cycle. Examples include material and manpower costs for outages, replacement energy costs, and the salaries of year round personnel. They are categorized as fixed or variable. Fixed costs do not depend on the operating conditions of the plant, and variable costs do. The O & M unit costs are derived from expert recommendations acquired by Jacopo Saccheri at MIT [8]. Table 4.4 PWR Operations and Maintenance Unit Costs Cost Category __ Variable Fixed Cost Component Symbol Unit Price Refueling Outage CRO $800,000/day Forced Outage CFO $100,000/day Replacement Energy ('repP 30 mills/kW-hre Personnel Cpers $150,000/person-yr Number of Personnel Npers 600 117 All costs presented in Table 4.4 are considered in the O & M analysis except replacement energy. Note that equation (4.6) shows that the levelized unit cost is obtained by normalizing the total cost by the energy produced from the plant; this does not include replacement energy purchased from other utilities during outages. Including the replacement energy costs unjustly increases the COE, because the utility receives revenue from its sale that is unaccounted for in the economics analysis. It is therefore assumed that the costs and revenues associated with replacement energy are perfectly balanced, and do not affect the overall COE. 4.4.3.3 Capital Costs With the lack of new plant construction in the US over the last two decades, vendor estimates for capital costs are regarded with extreme caution by potential investors. Historically, the difference between initial estimates and final realized costs for nuclear construction was large, often by a factor of 3 or more. Reasons for this include but are not limited to the lack of owner control of the construction process, "regulatory ratcheting" by the NRC in the wake of the accident at Three Mile Island, and growing public opposition to nuclear power. While it is not the intent of this report to examine the current state of these factors and their ability to contribute further price increases to the industry, it is important to note that any cost projections for nuclear power will be regarded as highly speculative until demonstrated by construction of a new plant in the US. Uncertainties aside, there are two capital cost estimates addressed in this economics analysis, both of which involve backfitting existing PWRs for use with hydride fuels. The first scenario, minor backfit, is geared toward integrating hydride fuels into existing plants without major modifications to the pressure vessel. This is accomplished by maintaining the fuel assembly and control rod configurations; the design space is therefore limited to geometries at the existing core pitch. The conversion costs from the point of view of capital include the costs to replace the steam generators 118 and upgrade the turbine units , if the new geometries offer increased power. Coolant pumps will also require upgrades, but their contribution to the capital investment is small compared to the turbine and steam generators, and so will not be considered. The major backfit scenario considers retrofitting a much wider range of geometries into existing PWR cores (i.e, all remaining geometries in the parametric study). The potential power upgrades are larger, and in addition to steam generator replacement and turbine upgrades, the vessel head and core internals will require replacement. An additional cost should also be considered. Existing units that decide to switch to hydride fuel will have to discard partially irradiated UO2 fuel assemblies. Since the utility has already incurred the cost of this fuel, a simple model for fuel depreciation is needed so that the remaining "worth" of the fuel can be estimated and added to the overall capital cost of the conversion process. In this analysis, it is assumed that the value of the fuel depreciates linearly with time, and so the total value of the fuel in the core at the end of an operating cycle is approximately 1/3 of the total cost of the fuel assemblies when new9. The costs for new steam generators, vessel heads, and core internals are available from current industry experience. It is assumed that the vessel head and core internal replacement costs are fixed, and not dependent on the power. The steam generator and turbine upgrade costs, however, are expected to demonstrate an economy of scale. This is based on historical economic information, that shows that the unit cost (i.e, $/kW) for these components is lowered as the power output from the plant increases. A scaling argument is therefore used to predict the capital cost of major nuclear plant components as a function of the reference cost, Costref, power, , and a scaling factor, m [10]. The cost for a new component is given by: 8 It is assumed that the turbine has untapped capacity that can be exploited with appropriate modifications and upgrades. New turbines are therefore not required. 9 Assuming a linear depreciation model, at the end of an operating cycle 1/3 of the fuel is worth 0, 1/3 of the fuel has 1/3 of its value, and 1/3 of the fuel has 2/3 of its value. The average worth is therefore - (1/3) * (O + 1/3 + 2/3) - 1/3 of the total cost of the fuel for a new core. 119 (t~ Lmcompo.nr (4. 12) := Costref kne Costnew The upgrade cost is approximated as the difference in cost between the component sized to operate at a new power, and the component sized to operate at the reference core power. Costupgrade= CoStnew - Costref = Costref e f J -. The costs of components for the major and minor backfit scenarios are summarized in Table 4.5. It is assumed that these estimates are for installed components, and so the cost of labor is not considered separately. The reference turbine cost and the scaling factors are taken from historical data available in the Department of Energy's "Nuclear Energy Cost Database" [10], while the cost estimates for the reference steam generators, vessel head, and core internals are obtained from Professor R. Ballinger of MIT, an observer familiar with industry cost experience. The value for existing UO2 fuel that is lost when the backfit is performed is obtained from equation (4.40), presented later in this Chapter. Table 4.5 Cost Estimates for Installed Nuclear Components Cost Component Steam Generators (Ref Q) Vessel Head Core Internals Turbine Generator (Ref Q) Existing Fuel Value Symbol Price Scaling Factor, m CsGref $100,000,000 0.6 Chead $25,000,000 Cint $25,000,000 Cturb,rf $338,000,000 Cfuel $66,586,000 0.8 4.4.3.4 Plant Operating Parameters The following operating parameters are fixed for the economics analysis. 120 Table 4.6 Fixed Plant Operating Parameters Parameter Refueling Outage Length (ref. core) Symbol TROref Value 20 days/cycle FOR 0.01 L' 0.99 Thermal Efficiency 1 0.33 Batches n 3 ForcedOutageRate Availability Plant Life Tplant 20 yrs The 20 year plant life is based on current NRC license extensions for existing LWRs. It is expected that an existing unit that converts to hydride fuel can expect to operate for this period of time. The refueling outage length is based on the most efficient units operating commercially today. 4.4.3.4a The Operating Cycle Two significant indicators of plant performance are missing from Table 4.6: the capacity factor, L, and the cycle length, Tc. The cycle length, which is the time between successive startups, is made up of three components: the duration of fuel irradiation and the downtime for forced and refueling outages. The effective full power years (EFPY) at discharge is used to denote the total irradiation time for the fuel. It depends on the thermal power, Qth,and the amount of energy available from the fuel through the burnup, Bu, and heavy metal loading in the core, MHM. Because the fuel is handled n times during its lifetime before being discharged from the core, the irradiation time for an individual cycle is EFPYC,which is equal to the quotient of EFPY and n. The cycle length is therefore given by: Tc = EFPY + TFO + TR ° 365.25 (yrs) (4.14) where EFPYC is in years, and the forced outage length per cycle, TFO,and the refueling outage length per cycle, TRO,are in days. EFPY and EFPYC can be determined by: EFPY = EFPYcn BuEP -M MHM A1h 1000 10(4.1 365.25j 5) 121 where the units are: t MWD(kgM =1000 j(Birth) 365.25(dSj J =(Yr)(4.16) __-~~~~ \M}- (yr) The availability is a measure of the plant's operating capacity, accounting for outages that are not planned and require the plant to be either de-rated in power or shutdown. Both EFPY (yrs) and EFPYC (yrs) are related to the forced outage length, TFO(days), through the availability. Note that the sum of EFPYCand the forced outage length is the available cycle length, TAV(yrs). EFPY =(EFPY+ TFO .L'=(EFPY n + 365 L'=.25 . n TA L' (yrs) (4.17) Solving for the forced outage length yields: TFO = EFPYC -( -1) 365.25 (days) (4.18) With the refueling outage length given in Table 4.6, all unknowns in equation (4.14) for the cycle length have been defined. The cycle length is then used to solve for the capacity factor, which is a measure of the plant's operating capacity accounting for both planned and unplanned shutdowns: L EFPYC - (4.19) r Substituting for both Tc and EFPYC, the capacity factor can also be written as: L Bu B//L, + 0.001 T (4.20) Q .sn where the specific power, Qp, is: aOA Mp= kth MH kgHM , (4.21) 122 Thus it is seen that the plant capacity factor depends on the burnup in the fuel, the mass of heavy metal loaded in the core, and the power. A helpful way to visualize the relationship among these terms is by constructing a simple plot of plant capacity versus time, for three different operating scenarios. This plot is shown in Figure 4.13. The plant capacity is the fraction of rated power at which the plant operates. When the plant operates at 100% capacity, the operating cycle length (the length between shutdowns) is EFPYC. When the plant operates at its availability, which accounts for time down due to forced outages, the length of operation is the available cycle length, TAV. And finally, when the plant is operating according to its true capacity, which accounts for time down due to both forced and refueling outages, the operating length is equal to the cycle length, Tc. Because the total energy available from the core is the same for all three operating scenarios, the areas represented by each combination of plant capacity and operating length are equivalent. Figure 4.13 Plant Capacity vs. Operating Length Plant Capacity TFO TRO ::~~~1 h1-p 1 L L · ·--- · r---- :: :: ::·:··:: · :::· :':'"·'::':: · 10 EFPYc TAV Tc Time There is one final note regarding the refueling outage length. The value listed in Table 4.6 is exemplary of the most efficient PWR units, which typically operate on an 18 month cycle. During the refueling outage two types of maintenance activities occur: those associated with refueling evolutions, and those associated with maintenance and 123 inspections of the plant equipment (i.e., reactor vessel, steam generators, turbine, etc.). With advice from plant engineers in industry, the average time devoted to each outage activity was approximated for a typical refueling outage. Figure 4.14 Refueling Outage Activities TRO _ _ L ._ 3 daysfor reactor shutdownand startup 10 daysfor refuelingevolutions 2: 3+ 4: 20 daysfor maintenanceand inspections 1: Because of the large variation in cycle length for the designs in the parametric study, it is believed that the critical path maintenance devoted to non-refueling activities (i.e, 4 in Figure 4.14) should scale with the time between successive shutdowns. For example, a PWR operating on a 9 month cycle still requires a total of 13 days for refueling evolutions, but the remaining critical path maintenance can most likely be performed in fewer than the originally allotted 7 days. An assumption is therefore made that the critical path maintenance devoted to non-refueling activities scales linearly with the cycle length. A PWR operating on a 9 month cycle would therefore need a total of 16.5 days for its refueling outage (13 days for refueling, and 3.5 days for remaining critical path maintenance). TR =13T ref (days) (4.22) Equation (4.14) shows that the cycle length depends on the refueling outage length. Multiple iterations are therefore required for the refueling outage and cycle lengths to converge to constant values. The procedure is as follows: an initial guess for the cycle length is made using the reference refueling outage length; the new refueling outage length is determined using equation (4.22); a new cycle length is then determined. 124 The process repeats itself until neither the refueling nor cycle lengths change significantly between iterations. 4.5 Economics Analysis This section develops and discusses the details necessary to determine the cash flows for the fuel cycle, O & M, and capital cost components of the COE, subject to the range of operating conditions and core geometries considered in the parametric study. The results for the lifetime levelized unit cost components are presented, but the combined COE analysis is delayed until Section 4.6. 4.5.1 Fuel Cycle Costs 4.5.1.1 The Nuclear Fuel Cycle The nuclear fuel cycle includes all activities related to the procurement, use, storage, and disposal of nuclear fuel. It can be open or closed. In the open, or oncethrough cycle, uranium is mined from ore deposits, enriched and fabricated into fuel assemblies, burned in the reactor, and disposed of directly in a geologic repository after a period of on-site storage. In the closed cycle reprocessing of the discharged fuel is employed to chemically separate fissile material from the fission products for later incorporation into fresh fuel assemblies. There are significant safety concerns accompanying spent fuel reprocessing and the potential use of the technology as the basis for an advanced nuclear weapons program. Because of these concerns, and the stable low cost of uranium ore and nuclear fuel services, the US has adopted the open cycle for today's operating reactor fleet. The fuel cycle cost analysis therefore only considers the once-through direct fuel cycle option. In future analyses of hydride fuels incorporating plutonium, reprocessing cost estimates will need to be included. The once-through fuel cycle is typically broken into two stages: 125 * Thefront end: The front end encompasses all activities from the initial mining of uranium ore to the fabrication of new fuel assemblies. More specifically, it includes all the costs associated with: extraction/mining of uranium ore, conversion of ore to gaseous UF6, 235U enrichment, and fabrication of fuel pellets and fuel assemblies. * The back end: The back end includes all costs associated with the temporary storage of spent fuel at the reactor site and permanent disposal in a geologic repository. 4.5.1.2 Recurring Cash Flows and the Fuel Cycle The lifetime levelized unit fuel cycle cost is given by: Clev,fcc Clevc - CEannual PVfcc th L 8.766 r '1 (4.23) r e-rTplanI All terms in this equation have been previously defined except for the total present value of fuel cycle costs, PVfc, which depends on the cash flow histories for all operating cycles over the lifetime of the plant. To predict the cost for the nth successive cycle, the present value for the first operating cycle, PVfcc,,,,is found, and projected forward using the escalation rate and cycle length. PVfcc, = PVfcco en g T C ' (4.24) In this way, the fuel cycle costs are modeled as discrete cash flows through time, as shown in Figure 4.15. 126 Figure 4.15 Cash Flows for Successive Operating Cycles Time PVfc,o PVfP, 4 PVfcc,2 PVfcc,3 PVfcc,4 1"V fcc,5 PVfcc, 6 The total present value can then be found by discounting each cash flow expenditure back to the reference date by the discount rate, r. The reference date is the start of irradiation for the first operating cycle. PVfc =· PVfcc,o+ EPVfcc,n .e - nr' T (4.25) n=l This is the desired cost term in equation (4.23). The only unknown is the present value of costs for the first operating cycle, PVfc,,,, which is discussed in the next section. 4.5.1.3 Cash Flows for the First Operating Cycle To obtain the desired cash flows for the front and back end components of the first operating cycle, four things are needed: a mass balance of material flows through the front end processes, the unit cost for each component based on the heavy metal loading in the core ($/kgHM),the time relative to the start of irradiation when each cost is incurred, and the mass of heavy metal loaded into the core. 4.5.1.3a Front End Mass Balances The front end unit costs listed in Table 4.3 are based on the mass of heavy metal entering the individual processes. For example, the unit conversion cost is $8 per kilogram of heavy metal entering the conversion plant. Due to material losses, however, the mass of heavy metal flowing through each process is not the same as the mass of heavy metal that ends up in the core. Thus, the production of 1 kg of heavy metal for 127 core loading requires more than 1 kg of heavy metal mined from uranium deposits. Mass flow balances of the front end are therefore used to determine the equivalent front end costs with respect to the unit mass of heavy metal loaded into the core. The mass flow balance is performed using mass loss fractions, 1, as recommended by NEA/OECD [9]. The mass loss fractions, given in Table 4.7, relate the mass flows, M, into and out of each process. Mm" ( 1 Mout (4.26) - Table 4.7 Mass Loss Fractions for Front End Fuel Cycle Processes Mass Loss Fraction Symbol Mining/Ore Value lore 0 Conversion Iconv .005 Enrichment lenr equation(4.32) Fabrication lfab .01 Figure 4.16 traces the flow of heavy metal through the front end of the fuel cycle required to produce 1 kg of heavy metal at the reactor. The individual mass flow terms, Mx, are developed below. Figure 4.16 Mass Flows for Front End Fuel Cycle Processes Mtails Power Plant The unit mass of heavy metal loaded into the power plant is 1 kg. Mpp= 1 kgHM (4.27) 128 Fuel Fabrication Mass flows into the fabrication plant as enriched UF6 , and flows out as the mass of heavy metal in either U0 2 or UZrH,.6. Mo~fab (ll 0IfabJ 1|(4.28) M pp -lfab Fuel Enrichment The enrichment loss, lenr, depends on the fuel enrichment, and so it is not assigned a specific value in Table 4.7. For this study the fuel enrichment varies between 5% and 12.5% for UZrHI.6and between 5% and 10% for UO2. Unlike the other front end processes that have a single output mass flow stream, the enrichment plant has two: the tails (or waste) stream, Mt,,is,with the depleted uranium by-product, and the enriched product stream, Mfab,headed to the fuel fabrication plant. Both depend on the product enrichment. I:[nthis study, the feed and tails enrichments are fixed, and the product enrichment is variable, as shown in Table 4.8. Table 4.8 Inlet and Outlet Mass Flow Stream Enrichments at the Enrichment Plant Flow Stream Symbol Mass Fraction Enrichment Feed f 0.00711 Tails t 0.003 Product p 0.05, 0.075, 0.10, .125 Simple mass flow balances on 235 U and the total mass of heavy metal are applied to obtain the desired ratio between the feed and product mass flow streams. Menr, f =Mtas t+Mfab p (4.29) Mtails = Menr - Mfab (4.30) and, Substituting equation (4.30) into equation (4.29) and rearranging terms yields the desired mass flow ratio. Menr ( -t) Mfab f -t) ~~Mnrloa~~~ ~(4.31) (p~-) 129 where, (IlenrJ)( (4.32) There is an additional step, however, to finalize the unit cost for the enrichment process. Table 4.3 lists the unit cost for enrichment with respect to kg of SWU, or separative work units. Like the mass flow streams, the unit enrichment cost also depends on the final enrichment of the fuel. This is accounted for by determining how many units of "separative work" are required to separate the feed into output streams with desired enrichments. SWU depends on a potential function, V,which is applied to the input and output streams at their respective enrichments, e. V(E) =:(2E -1). ln (4.33) 1--E The enrichment dependent SWU is defined using this potential function and the mass flows for each stream connected to the enrichment plant: Mtais V(t) - Menr,,V(f) (4.34) (kgswu kgHM M fab Substituting for the mass flows from equations (4.29) and (4.30), and for the potential function from equation (4.34), it can be shown that: SWU =[V(p)- V(t)]- (P) [V(f - V(t)] (kg u) (4.35) The unit SWU requirements for the 4 enrichments considered in this study are listed in Table 4.9. Table 4.9 SWU Requirements for Different Enrichments of UO2 and UZrH1.6 SWU (kgswU/kgHM) 5% 7.5% 10% 12.5% UO 2 7.19 12.17 17.28 - UZrHI. 6 7.19 12.17 17.28 22.48 130 Note that the product of SWU and the unit enrichment cost listed in Table 4.3 ($108/kgswu), yields the desired enrichment cost per kg of heavy metal loaded into the core (Table 4.9 lists the kg of SWU per kg of heavy metal loaded into the core). Fuel Conversion The conversion process transforms uranium ore, U3 08 , into gaseous UF6, according to the following mass balance: Menr (4.36) Mc = 1 | 1conv ) Uranium Mining/Ore There are no losses in the mining and milling operations, so, More ( 1 Mc =1 (4.37) 'onv re Combining equations (4.27), (4.28), (4.31), (4.36), and (4.37), the mass of natural uranium required to produce 1 kg of heavy metal at the reactor is: More -- l (P-t fco -t .M 1-lfab kg(I (4.38) These equations can also be used to get the mass flows through each front end process necessary to yield 1 kg of heavy metal at the reactor. This information is given in Table 4.10 for different enrichments of U0 2 and UZrH1 .6. Note that the units are kg of heavy metal through the process per kg of heavy metal loaded into the core. 131 Table 4.10 Mass Flows Through the Front End Front End Unit Mass Flows (kP HM throuh nrocess/k HM in the core) UO UZrH. 6 5% 7.5% 10% 5% 7.5% 10% 12.5% 1 1 1 1 1 1 1 Fabrication 1.01 1.01 1.01 1.01 1.01 1.01 1.01 Enrichment 11.55 17.7 23.84 11.55 17.7 23.84 29.98 Conversion 11.61 17.79 23.96 11.61 17.79 23.96 30.13 Mining/Ore 11.61 17.79 23.96 11.61 17.79 23.96 30.13 Reactor 4.5.1.3b Back End Mass Balances The back end unit costs for spent fuel storage and disposal are listed in Table 4.3. The disposal fee is already levelized with respect to the energy production from the plant, and need only be added to the lifetime levelized unit fuel cycle cost as determined by equation (4.23) for the remaining front and back end processes. The unit storage cost requires no mass flow balance because it is already based on the heavy metal loading in the core. Even though the burnup in the fuel changes this mass between initial loading and final discharge, this analysis assumes that the storage costs, like the front end costs, are based on the original heavy metal loading in the core. 4.5.1.3c Fuel Cycle Cash Flows With the information in Tables 4.3, 4.9, and 4.10, the unit costs for the front and back end components can be determined with respect to the initial heavy metal loading in the core. 132 Table 4.11 Fuel Cycle Unit Costs With Respect to the Heavy Metal Loading in the Core Unit Cost (/kg H Sym. 5% UO 7.5% 10% 5% UZrHj.6 7.5% 10% 12.5% Mining/Ore UCore 476.01 729.39 982.36 476.01 729.39 982.36 1235.33 Conversion UCo,,n 92.81 142.32 191.68 92.81 142.32 191.68 241.04 Enrichment UCenr 776.52 1314.36 1866.24 776.52 1314.36 1866.24 2427.84 Fabrication* UCfab 277.75 277.75 277.75 687.81 687.81 687.71 687.71 Storage Fuelmp. Fuel Storage UCtor 250 250 250 618.54 618.54 618.54 618.54 * This is the unit fabrication cost for the reference core geometry. For geometries with larger and smaller rod numbers, the unit fabrication costs are still given by equations (4.9) and (4.10), with Cfabreplaced by UCfab. The front and back end costs occur at different times relative to the start of fuel irradiation and therefore must be referred to this date using the discount rate by appropriate lead and lag times to obtain their true present value. OECD/NEA recommended lead and lag times for the front and back end processes are given in Table 4.12 [9]. Table 4.12 OECD/NEA Recommended Lead and Lag Times for Front and Back End Processes Symbol Value Fuel Fabrication Tfab 1 yr Uranium Enrichment Tenr 1.5 yr Uranium Conversion Tco,,v 1.5 yr Transaction 2 yr To Uranium Ore Purchase - Tc* Tstor Temporary Spent Fuel Storage * A negative sign denotes that the storage costs are incurred after the start of fuel irradiation and so the cost must be referred back in time to the reference date Keeping in mind that the disposal fee is added at the end, the present value of unit costs for the first operating cycle is given by: PV(UCfC,G) TJCoree + con r er + UCenre + C fabeUCbstor e - r Tc (4.39) And the total present value for the first operating cycle is given by: PVc, o = PV(UCfcC,O) MHM ($) (4.40) 133 The mass of heavy metal in the core, MHM,is: MHM = N (4) (D-2tcI -2 tg ) Lh W (kgH) (4.41) where, N: number offuel rods in the core D: clad outerdiameter tcl: clad thickness tg: Lh: p: w: radialgap thickness fuel rod heatedlength densityof thefuel weightpercentheavy metal of thefuel 4.5.1.4 Lifetime Levelized Unit Fuel Cycle Cost Using the present value for the first operating cycle given by equation (4.40), the total present value for all fuel cycle costs incurred over the life of the plant can be determined: PVfcc=PVfcc,o+PVfcc,n .e-'e (4.42) n=l where, PVfcc,, = PVfcc,o e g (4.43) And the final lifetime levelized unit fuel cycle cost is given by: Ecc annual L,it7 *L 8.766 1-e rTplat where Cdispis given in Table 4.3. 4.5.2 Operations and Maintenance Costs Operations and maintenance costs include all production costs associated with energy generation from the plant not included with the fuel cycle, and can generally be divided into two categories: fixed and variable. Fixed costs are steadily incurred over the life of the plant and do not depend on operating parameters (i.e, operating cycle length, capacity factor, energy production per cycle, etc.). Variable costs take these factors into consideration. The fixed and variable costs considered in this analysis and their respective unit costs are given in Table 4.13. 134 Table 4.13 Fixed and Variable Unit O & M Costs Cost Category Symbol Unit Cost Fixed Costs Plant personnel Cpers $150,000/pers-yr Refueling Outage CRo $800,000/day Forced Outage CFO $150,000/day Variable Costs As discussed in Section 4.4.3.2, the expenditures and revenues associated with the purchase and sale of replacement energy during plant outages are assumed equal, and so are not included. 4.5.2.1 Annualizing O & M Cash Flows The lifetime levelized unit O & M cost is given by equation (4.6): levO&M &M Clev"O&M -- ,,Eannual Eannuali *ith PVO&M 1 L 8.766 r j L1eraa, -r (445) where all temls have been previously defined except the total present value of O & M expenditures over the plant's life, PVo&M.Like the fuel cycle cost analysis, it is helpful to redefine the O & M unit costs with respect to consistent units. For example, in Table 4.13 the unit personnel costs are in $/year, while the outage costs are in $/day. For ease of calculations, all O & M unit costs will be annualized so that their sum constitutes the total O & M expenditures for the first year of plant operation. With the refueling outage length, TRO,defined in equation (4.22), the annual cash flow for refueling costs is: CFRo =: ROTRO TC ($ (4.46) yr The units for TRo and Tc are (days/cycle) and (years/cycle). Similarly, the forced outage length defined in equation (4.18) can be used to determine the annual cash flow for forced outage costs: 135 CFFO = CFO TFO $ (4. 47) TC where TFOis in (days/cycle). The product of the number of plant personnel and their annual salaries yields the total annual personnel costs: (4.48) CFpers = Npers Cpers The total annual 0 & M expense for the first year of plant operation is therefore: CF&M, = CFRo + CFFo + CFpers (4.49) ) Recall that a constant escalation rate is used to account for non-inflationary price increases in the cost of labor and materials over time. The nth successive annual O & M expenditure is therefore given by: CFO&M , = CFo&M,o eg n ' (4.50) ' where the initial cost, CFo&M,o,is assumed to occur at the end of the first year of plant operation. This is shown in Figure 4.17. Figure 4.17 Cash Flows for Successive Annual O & M Expenditures Time CFo&NI,O C& CFo&M, CFo&M,2 CFo&M,oU 3 CFO&M,4 CFo&M,S 136 4.5.2.2 Lifetime Levelized Unit O & M Cost With discrete O & M expenditures projected over the plant's life, the total present value is determined by discounting each cost term back to the present by the discount rate. PVO&M = (4.51) CFO&M,n e-r(n+l) n=O The lifetime levelized unit O & M cost can then be determined according to equation (4.45), which is repeated below: EvO&M&Eannual th PV&M -r -L8.766 r 1-e-rTp](.2 (4.52) 4.5.3 Capital Costs Capital is typically the largest component of the COE, and includes costs associated with siting, design, construction, refurbishment, and upgrades of nuclear facilities. They are unique among the COE components because they are not continuously incurred over the life of the plant. Instead, these sunk costs occur during the plant's construction phase, when aging equipment needs replacement, and when equipment modifications/replacements are made in preparation for power upgrades. Because the Hydride Fuels Project seeks to quantify the benefits of hydride fuel use in existing LWRs, only capital costs associated with the backfit are considered for the final optimization. These expenditures are only a fraction of the design and construction costs for a new plant, and so their contribution to the overall COE will not differ significantly from the fuel cycle and O & M components. In the minor backfit scenario, the existing fuel assembly and control rod configurations are maintained and capital costs are incurred to upgrade the steam side of the plant (the steam generators and turbine) for operation at higher powers. Because the coolant temperatures at the inlet and outlet of the core are fixed, it is assumed that no further modifications are required to the pressure vessel. For the major backfit scenario, the layout of fuel in the core can assume any geometry within the bounds of the 137 parametric study, and so in addition to steam generator and turbine upgrades, replacement of the vessel head and core internals is also required. Note that designs offering lower powers than the reference core for both backfit scenarios will not incur capital costs for the turbine and steam generator units. The major backfit case will still require replacement of the vessel head and core internals, however, to accommodate the new geometry of the fuel assemblies. Both the major and minor backfit cases will also incur the cost of discarded UO2 fuel assemblies. 4.5.3.1 Predicting Capital Costs for PWR Backfit Section 4.4.3.3 discussed the capital expenditures assumed for the different backfit scenarios. They are summarized below: Major Backfit Capital Costs · Steam Generators - Replace ifQnew > Qref * VesselHead- Replacefor all Qnew,, * Core Internals- Replacefor all Qnew * TurbineUnit - UpgradeifQnew > Qref · ExistingFuel - Add remaining value of discardedfuelfor all Qnew Minor Backfit Capital Costs · Steam Generators - Replace ifQnew > · Turbine Unit - Upgrade if Qnew> Qref · ExistingFuel - Add remainingvalue of discardedfuel for all Qnew Qref Using the capital costs defined in Table 4.5, and the scaling arguments provided in equations (4.12) and (4.13), the backfit expenditures for each scenario can be determined: If Qnew> Qref jChead + + Cbacfit,major= head + Cint + c fuel +c . + CSG,ref C +C new )ref J ewre (4-53) 138 Cbactfiminor = Cfuel +CSG,ref r + Cturbref e y ef J [L ) mL (4-54) ref) If Qnew< Qref Cbacft,major = Chead + Cint + Cfitel (4-55) Cbackft,minor= Cfuel (4-56) As in the case of O & M, it is assumed that the replacement energy costs incurred during the fuel conversion outage are directly passed onto the consumer, and so their costs and associated revenues balance. 4.5.3.2 Lifetime Levelized Unit Capital Cost The general form of the equation for the lifetime levelized unit capital cost is: lev'cap lev,cap Eannual where PVcapis equal to (4.52) r 77.-L8.766 l-eT -,- COStbackfitminor l ant orCStbackfit,major Unlike fuel cycle and O & M costs, the capital costs for hydride fuel conversion are only incurred once during the plant's lifetime. The selection of Tplanttherefore has a significant impact on Cevcap because it determines the total amount of energy produced that can be sold to recover the initial capital investment. If Tplantdecreases, the energy production decreases, and Cle,,capincreases (meaning the utility must charge more for the electricity consumed to recover the capital investment). The impact on the fuel cycle and O & M costs is much less significant because they are recurring in time, and the energy production to recover their investment is fixed by the spacing between recurring cash flows (i.e., 1 yr. for O & M, or Tc for fuel cycle costs). The plant life chosen for this analysis as listed in Table 4.6 is 20 years. It is based on the life of NRC license extensions granted for approved LWRs. 139 4.6 Lifetime Levelized Unit COE The results from the economics analysis are presented in this section for the major and minor backfit scenarios at both pressure drop limits. Throughout this report, the equivalence of square and hexagonal arrays has been suggested for identical combinations of rod diameter and H/HM ratio. It is believed that this relationship holds for the thermal hydraulic, neutronics, and fuel performance studies, which comprise the primary inputs to the economics analysis. The relationship should therefore hold for the cost analysis. In this section results are only presented for square arrays, but the hexagonal costs can be inferred for equivalent geometries. 4.6.1 Results for Major Backfit: UZrH1.6 and UO2 at 60 psia The lifetime levelized unit cost of electricity for the major backfit scenario at 60 psia is shown in Figures 4.18 and 4.20 for different enrichments of UZrH 1.6 and U0.2 Also shown on each plot, as a black line, is the minimum COE at each P/D ratio. These lines are re-plotted in Figures 4. 19A and 4.21A independent of rod diameter to provide a clearer comparison of the COE among different enrichments and fuel types. Also shown in Figures 4.1.9 and 4.21 are the fuel cycle, O & M, and capital costs that comprise the minimum COE (i.e., adding Figures 4.19(B-D) gives 4.19A). The minimum COE for UZrH1 .6 is 18.4 mills/kW-hre for 12.5% enriched fuel at: P/D = 1.32, Drod= 9 mm. Note that this is very close to the reference core configuration, but that there is a large range of P/D ratios with costs that are within a small fraction of this minimum value (i.e, 1.22 < P/D < 1.42). The minimum COE for U02 is slightly lower at 17.9 mills/kW-hre for 5% enriched fuel at: P/D = 1.39, Drod = 6.5 mm. The range of P/D ratios with costs close to this minimum value, however, is narrower than for UZrH1.6 . UZrH1. 6 appears to offer the potential for cost savings over UO 2 in the P/D range 1.2 to - 1.35. A more detailed comparison of the results is presented in Section 4.6.1.2. There is a lot of useful information in these figures. First, examine Figure 4.22, which plots the familiar maximum powers for UZrH1.6 and UO2 . Lines showing the maximum power as a function of P/D ratio have been added. Note the similarities 140 between these maximum power lines and the minimum COE lines plotted in Figures 4.18 and 4.20. They do not perfectly overlay one another, but their shapes and placements on the parametric map are similar, thus establishing a strong correlation between minimum cost and high power. There are exceptions to this rule. For example, Figure 4.18 shows of P/D ratio for each enrichment of UZrH 1.6 that the minimum COE as a fimunction plateaus at a rod diameter of - 9 mm, before making a sudden jump to lower rod diameters where the achievable power is higher. Next compare the minimum COE curves shown in Figures 4.19A and 4.21A. The costs for UZrH 1.6 are minimized at its highest enrichment; the opposite is true of oxide for most of the geometry range. Also note the difference in the curve shapes. As P/D increases, UZrH .1 6 costs rapidly approach the most economical geometries, and then begin a gradual trend of increased cost. The reason for this, revealed in Figures 4.19B and 4.19C, is rising fuel cycle and O & M costs. The UO 2 costs, however, experience a more gradual descent and are not redirected upward like UZrH1.6. Figure 4.21B shows that the fuel cycle costs are consistently decreasing (with the exception of a brief increase around P/D = 1.4 for 7.5% and 10% enriched fuels), and therefore keep the overall COE from rising. This reason for this is explained in detail in Section 4.6. 1.1. To provide increased understanding of the behavior of the COE curves, the next section examines in detail the COE and its individual components for 12.5% UZrH 1. 6 and 5% UO2. These enrichments are chosen because they provide the lowest overall COE. Following this examination is the final comparison of costs for the major backfit scenario employing UZrH 1. 6 and UO2, with specific attention given to geometries where cost savings can be realized for hydride fuel. 141 Figure 4.18 Lifetime Levelized Unit COE vs. P/D and Drodfor Square Arrays of UZrH.6 at 60 psia ,4: 5% UZrH 1.6 (mills/kW-hre) B: 7.5% UZrH 1.6 (mills/kW-hre) 60 12 11 12 E 10 50 11 50 E 40 40 CE 8 30 8 30 7 7 1.3 1.4 1.5 Pf/D 0 C' 1no, I 7rH (milIqk ALhrp) 1.1 1.2 1.3 1.4 1.5 PfD 19 r°F, I 17rH {milIQkALhrp. 1.1 1.2 fl 60 12 11 12 60 11 50 10 50 10 40 :c 9 8 30 7 n 1.2 1.3 1.4 30 8 7 20 1.1 40 9 20 1.5 1.2 1.1 1.3 PID P/D 1.4 1.5 Figure 4.19 Minimum COE and its Components vs. P/D for Square Arrays of UZrHI.6at 60 psia . 8 MinimumFuel CycleCost vs PD A: MinimumCOE vs P.O 35 - 11' 12 30A1 . ...... . ........- ..... ---------- _: 0 A:m 8F: ; V. LLI i '~-m : o ~:~ CS : ° : 1-- :El i oo: 9 ,7 ...... ( LL 120 : , 11 ---.--. , ......... -. I o 12 13 14 -- --- ----- -- . A,, 7 , 6 5% Enrichment 7 5% Enrichment 11)%Ernllchent 12.5% Enrichment 12 . 1:3 . 14 15 PiO O MinimumCapital Costvs PDO "- 15 C10 MinimumP/O &M ost vs P. 0 ..oc AL .-I----- 183 11 15 00 - 3.5 ---:- 'Z i= - . , . . : t 3. 3-. E ci ~ 9000 a C ! 7 '7t : , ' b : : , 2 a I ---t9 12 13 P/D 14 15 .... ....... .. ........ -8--. .. . . . .1-- --------- ;IZ - 15- :a~ :; 11 2 5 . ..... I (3j () 1 : -- - - - - : : 12 66,14 13 14 ,~4 t" I 15 P/D 142 Figure 4.20 Lifetime Levelized Unit COE vs. P/D and D,.odfor Square Arrays of UO 2 at 60 psia B 7.5% UO A: 5% UO2 (mills/kW-hre) (mills/kW-hre) 12 1: 80 11 '~- 1C - 2 60 I 11 50 60 C oI IliD 40 40 0 30 . 7 7I 20 20 1.1 1.2 1.3 1.4 1.5 P/D C: 10% UO. (mills/kW-hre) 1.1 1.2 1.3 P/D 1.4 1.5 70 1 1 60 E1 1 E 50 ,, 40 Q 30 . . . 1.2 1.1 . . . 1.3 P/D 20 _ , , 1.4 1.5 Figure 4.21 Minimum COE and its Components vs. P/D for Square Arrays of U0 2 at 60 psia A:MinimumCOEvs.PD /I1~yJ 40 --- - --;------ --------- B: MinimumFuelCycleCostvs.P/D 1S _ r ----- 12.5 .I :35 30 ----- II t - A. : - --- - ------ -- 15 --- --- I o E : 10 : :* c 25 I 1C 3 -------- 6A 4 : 20 ; ; [ L___.: 15 --------------- 11 12 : .. 1.3 PiD -------- oCLi-) -- +~- +n* AD A a . :.:.,. 14 , 75 ' :: 2 nA nA4A ; 1 15 A i ** 11 5%Enrichment 7.5%Enrichment 10% 10 Enrichment Enchment 1.2 1.3 P/D 15 I..I... .. 3 ---2 . 14 C: Minimum CapitalCostvs PD 4 20 . , 2 C Minimum O & M Cost vs. PID 14 . -.X .: - .------ E j -. ----- 1. aa : ' -----I - -- r .. 8 '"-_ ..... ..... ....... ' ''5 a 6: :: '. 11 12 13 PD 0*.:* - ... - : I :~~~~~~~~~~~~~~~~~~~~~~~~~~~~ : . ' 14 15 11 12 13 PiD 14 15 143 Figure 4.22 Maximum Achievable Power vs. P/D and Drodfor Square Arrays of UZrH.6 1 and UO2 at 60 psia With Vibrations and Transient Limits Applied ,Avi-n a D, TT7rH -,a ivlt 6 lrl i,.m m D,.rr TTf /-1 ' 6 1r,; \ 5 5 11 45 4 45 2e 1 5 '9 3 2.5 25 2 15 1 15 1 IL2 1. 1 13 P/D 4.6.1.1 COE Breakdown for 12.5% UZrH 1. 6 and 5% U0 2 at 60 psia Figures 4.23 and 4.26 plot the COE and its individual cost components for the major backfit scenario considering 12.5% UZrH. 6 and 5% UO2. Figures 4.24, 4.25, 4.27, and 4.28 plot the corresponding power, specific power, burnup, annual energy production, capacity factor, cycle length, annual outage length, and planned outage length. Following is a discussion of the cost components of the COE for each fuel as they relate to the operating parameters in Figures 4.24, 4.25, 4.27, and 4.28. Fuel Cycle Cost The fuel cycle cost analysis was presented in Section 4.5.1, where it was shown that the total cost in $ for a single operating cycle depends on the mass of heavy metal in the core (See equation (4.40)). The lifetime levelized unit fuel cycle cost, cevfcc, is equal to the refueling cost divided by the energy produced during the operating cycle. The energy production is the product of the fuel burnup and the mass of heavy metal in the core. Thus for a fixed geometry, evfcccan be increased or decreased by varying the burnup in the fuel. It is therefore not a surprise that the plots of Ce,ftc for 12.5% UZrH .1 6 and 5% UO2 in Figures 4.23B and 4.26B show a striking resemblance to the fuel bumups in Figures 4.24C and 4.27C. The figures are practically inverted, with the minimum fuel cycle costs corresponding to regions of maximum burnup. 144 The core power also plays a role in the determining the fuel cycle cost through the specific power, though its contribution is less significant than burnupl°. For a fixed burnup, ,,evf,,c will decrease as the specific power increases, because the operating cycle length, and therefore the period of time that the plant operates to recover the fuel cycle expenditure, is reduced. The effect of specific power on the fuel cycle cost is therefore a simple matter of the interest accrued between successive refuelings. Because this effect is marginal, the minimum fuel cycle costs will favor regions of higher burnup. Figures 4.24A, 4.24B, 4.27A, and 4.27B plot the core power and specific power. Note their similarity. Note that regions where the power and specific power are largest do not coincide with areas where the fuel cycle costs are minimized. This reinforces the primary dependence of fuel cycle costs on bumup. Figures 4.1 9A and 4.1 9B revealed that one of the reasons the minimum COE for UZrH,.6 increases at larger P/D ratios is rising fuel cycle costs. Tracing the path of the minimum COE line in Figure 4.23A through the burnup curve in Figure 4.24C, it is evident that the burnup at the most economic geometries decreases as the P/D ratio increases. This is the reason for the rise in fuel cycle costs. The fuel cycle costs shown in Figure 4.21 B for 5% U0 2, however, do not experience an increase for larger P/D ratios because the burnup continues to increase, as shown in Figure 4.27C. Another feature in Figure 4.19 warrants explanation in this section. Unlike the UO2 costs, the overall COE and fuel cycle costs for UZrH1. 6 are minimized for higher enrichments. This is contradictory with industry experience and the COE results presented for UO2. From a cost perspective, increasing the enrichment does two things. First, it increases the front end enrichment costs (Refer back to Table 4.11). Second, it allows neutronically the attainment of higher bumups which, if not limited by fuel performance constraints, lowers the overall fuel cycle costs. The two effects therefore compete to drive changes in the fuel cycle cost. For UZrH1.6, the cost savings attributed to larger burnups at the higher enrichments outweigh the cost penalty at the enrichment plant. The same effect is not realized for UO 2 fuel, because the marginal gain in bumup 10 Recall, however, where limited by fuel performance constraints, the burnup does depend on power. 145 at higher enrichments is smaller due to more stringent fuel performance constraints (i.e, from considering the internal pressure limit). The added enrichment costs therefore outweigh the small savings attributed to increased energy production. Refer again to Figures 4.7 and 4.9 for proof of this. O & M Cost The C)& M costs, as detailed in Section 4.5.2, are comprised of both fixed and variable expenditures that are recurring in time. The fixed costs involve the salaries of plant personnel, which are constant each year and independent of the plant's operating performance. Their contribution to the lifetime levelized unit O & M cost, CevO&M, is therefore determined by the annual energy production from the plant, which is shown in Figure 4.24D to depend predominantly on power (This relationship was also established by equation (4.5)). The fixed O & M component and power are therefore inversely proportional. Annually, the variable O & M component involves costs associated with both forced and refueling outages. Unlike the fixed component, they depend on the plant's performance (i.e, the parameters that determine total annual outage length), as well as the annual energy production from the plant. For most reasonable cycle lengths (i.e., > 6 months), the fixed component comprises the majority of the annual O & M cost . It is therefore expected that the behavior of cZev,O&M will scale with the fixed component, which as just discussed is inversely proportional to power. The lifetime levelized unit O & M cost should therefore be lowest where the power is maximum, which is evident when comparing Figures 4.23C to 4.24A and Figures 4.26C to 4.27A. The annual outage lengths are plotted in Figures 4.25C and 4.28C. Note that ClevO&M is lowest where the outage lengths are longest, which would not be observed if the variable component had greater influence on the overall O & M costs. This fact therefore reinforces the primary dependence of l,,,O&M on its fixed component. " From Table 4.4, the annual fixed cost is 150,000/pers-yr x 600 pers = $90 million/year. The variable costs, assuming a 1 year cycle length, are approximately $800,000/day x 20days/cycle x 1 cycle/year + $150,000/day x .01 forced outage days/day x 365 days/year = $16.5 million/year. 146 Like the fuel cycle costs, Figure 4.19C shows that O & M costs are minimized for higher enrichments of UZrHl.6. This is once again a result of increased burnup in the fuel. As the burnup increases the capacity factor increases, and with it the annual energy production from the plant. This brings Zev,O&Mdown. This effect is not observed, however, for UO2 because the marginal gain in burnup for higher enrichments is much smaller. The O & M costs for U0 2 in Figure 4.21 C therefore appear independent of enrichment. Capital Costs The capital costs are unique among the COE components because they occur only once, at the time of the expenditure. The lifetime levelized unit capital cost, lev,cap, depends on the amount of this expenditure and the energy produced to recover it over the life of the plant. For the major backfit scenario, the capital costs depend on two conditions: (1) whether a geometry offers increased power relative to the reference core; and (2) if an increase is reported, its magnitude. lev,ca, is plotted in Figures 4.23D and 4.26D. Each cost figure is clearly divided into two sections per the conditions described above. In the region where the power is below the reference core power, the capital expenditure is fixed (replacement of core internals, vessel head, remaining value of lost fuel), and so lev cap depends solely on the power/energy production from the plant. This is evident when comparing Figure 4.23D to Figures 4.24A and 4.24D and Figure 4.26D to Figures 4.27A and 4.27D. For regions where the maximum power is greater than the reference core power, additional costs are incurred for replacement of the steam generators and upgrades to the turbine. lev,captherefore increases in this region where power increases are reported. The magnitude of the increase, however, is limited because the power and energy production in this region also increases, which in turn drives reductions in the O & M costs. If the power increase is large enough, the O & M reductions more than compensate for the added capital component and overall costs are lowered. This is the reason the minimum COE lines plotted in Figures 4.23A and 4.26A pass through the maximum power region, despite the increased capital costs. 147 In summary, the behaviors of each COE component can be explained by examining the operating parameters for the plant and the individual cost assumptions. It is believed that the tools needed to understand the COE curves have now been provided to the reader. Subsequent cost results will therefore not be examined in such detail as provided in this section, although sufficient information graphically will be provided for such an interpretation. Figure 4.23 COE Breakdown for Square Arrays of 12.5% UZrH1. 6 at 60 psia A: COE (mills/kW-hre) B: FCC (mills/kW-hre) 12 60 1 50 1 11 ,, -ff E E 40 - 30 El 10 -o 9 cz 8 20 7 1.3 1.4 1.5 P/D C: O & M (mills/kW-hre) 1.1 1.2 1.3 1.4 1.5 P/D D: Capital (mills/kW-hre) 1.1 40 1 1.2 12 5 11 1 30 E 20 (2 4 E10 E 9 3 8 2 10 1.1 1.2 1.3 P/D 1.4 1.5 7 1.1 1.2 1.3 P/D 1.4 1.5 148 Figure 4.24 Plant Operating Conditions for Square Arrays of 12.5% UZrH 1. A: Core Power (x 10 6 kWth) 6 B: Specific Power (kWth/kgHM) 140 12 12 4 11 E 10 E 120 11 100 10 3 80 g 60 8 7 at 60 psia 2 k,.J 1.3 1.4 1.5 P/D C: Burnup (MWD/kg u,,) 1.1 1.2 12 11 E 10 lO E 8 40 7 1 20 1.3 1.4 1.5 P/D D: Annual Energy Prod. (x 1010 kW-hre) 140 12 1.2 11 120 1 1.1 1.2 100 8 80 7 An vv 1.1 1.2 1.3 P/D 1.4 0.8 0 0.6 8 0.4 7 1.1 1.5 1.2 1.3 P/D 1.4 1.5 Figure 4.25 Plant Operating Conditions for Square Arrays of 12.5% tJZrH1. 6 at 60 psia A: Capacity Factor B: Cycle Length (yrs) 12 1 0.96 11 E E 1C 5 1 4 n1 0.95 - -O 9 7 3 2 0.94 J 1 1.3 1.4 1.5 P/D D: Planned Outage Length (days/cycle) - 1.3 1.4 1.5 P/D C: A,nnual Outage Length (days/yr) 1.1 1.2 1.1 20 12 11 18 11 E. 1C 16 E 1.2 40 35 E10 14 n 9 12 10 1.1 1.2 1.3 P/D 1.4 1.5 30 8 25 7 20 1.1 1.2 1.3 P/D 1.4 1.5 149 Figure 4.26 COE Breakdown for Square Arrays of 5% UO2at 60 psia B: FCC (mills/kW-hre) A: COE (mills/kW-hre) 12 1 80 1 30 10 60 E 40 11 ~... O g 40 20 8 10 7 20 1.1 1.2 P/D 1.4 1.5 40 1 5 1 1 EE 1.3 P/D 1 QI 30 E 1( 20 n 10 4 3 o l ] 1.1 1.2 P/D 1.3 PfD 1.4 1.5 2 Figure 4.27 Plant Operating Conditions for Square Arrays of UO2at 60 psia A: Core Power (x 106 kWth) B: Specific Power (kWth/kgHM) 12 12 50 11 4 11 ic 3 10 30 8 2 Q 8 20 7 10 3 1 11 12 13 14 15 40 11 12 P/D 1.3 14 P/D C: 15 . D: Anr V-hre) 12 1 50 11 40 -p10 30 9 c 0El 20 7 10 1.1 1.2 1.3 P/D 1.4 1.5 1.2 11 0.8 o8 0.6 0.4 7 1.1 1.2 1.3 P/D 1.4 1.5 150 Figure 4.28 Plant Operating Conditions for Square Arrays of UO2at 60 psia A: Capacity Factor B: Cycle Length (rs) 12 0.96 11 3 12 2.5 0.955 E 10 2 - 9 0.945 8 8 1.5 0.94 7 1 11 1.2 1.3 Pin | 1.4 1.5 1.1 1.2 1.3 1.4 15 Pin t Vcle) D: C::i 20 12 11 18 10 16 , 9 14 8 12 30 28 E 26 24 22 7 20 10 1.1 1.2 1.3 P/D 1.4 1.5 1.1 1.2 1.3 P/D 1.4 1.5 4.6.1.2 Final Comparison for Major Backfit: UZrH1. 6 and U0 2 at 60 psia The bottom line for the major backfit scenario is the COE, and how the cost performance of UZrH1. 6 compares with UO2. As discussed in Section 4.6.1, the honor of the lowest COE for the major backfit scenario is reserved for U0 2 at the geometry: P/D = 1.39, Drod =: 6.5 mm. The cost is 17.9 mills/kW-hre. The minimum cost for UZrHi.6 is slightly higher at 18.4 mills/kW-hre at a tighter configuration: P/D = 1.32, Drod = 9 mm. A large range of geometries remain, however, where cost savings may be realized for UZrH 1. 6 fuel. Figure 4.29A illustrates this as a plot of the difference in the minimum COE for UZrHI . 1 6 and UO2 as a function of P/D ratio and rod diameter. Where the difference is positive, U0 2 offers the lowest COE. A black contour is provided to indicate where the cost difference is zero, and divides the plot into regions where each fuel provides the minimum COE. Figure 4.29B plots the enrichments that correspond to fuel providing the minimum cost at each geometry (i.e., the majority of the region where UO2 costs are lowest corresponds to 5% enrichment, although 7.5% UO2 is most economical in the top left portion of the figure). As expected, higher enrichments prevail 151 in the regions where UZrHi 6 is optimum, and in regions where UO2 is optimum, the enrichments are lower. Overall, Figure 4.29 shows that the costs are fairly comparable for the two fuels. The cost savings in the regions where UZrH 1.6 appears beneficial are not significant (< 2 mills/kW-hre), and the corresponding powers are typically lower than the reference core power. With this in mind, and recalling the uncertainties in the cost assumptions for UZrH 6 (i.e, fabrication cost), Figure 4.29 can hardly be used as a strong argument for a switch to hydride fuel. Figure 4.29 COE Difference and Fuel Enrichment for Major Backfit With UZrH1. 6 and UO2vs. P/D and Drodat 60 psia B: Enrichment 10 12 8 6 11 4 10 2 E E 9 0 E 1:g -2 8 -4 7 -6 6 -8 -10 5 "- P/D "- P/D 4.6.2 Results for Minor Backfit: UZrH1.6 and U0 2 at 60 psia For the minor backfit scenario, the design range is restricted to the reference core pitch. The fuel cycle and O & M costs are unchanged from the major backfit scenario, but the capital expenditure is reduced to reflect the use of the existing unit's vessel head and internals. Figures 4.30 and 4.31 plot the COE and its cost components as a function of P/D ratio for the minor backfit scenario employing UZrH 1. 6 and U0 2. Immediately obvious is that the minimum COE for each fuel occurs very close to the reference core geometry. For UZrH1.6, the minimum COE is 18.5 mills/kW-hre for 12.5% enriched fuel, and occurs at P/D - 1.30, Drod = 9.66 mm. This is almost identical to the major backfit minimum COE, which is marginally lower at 18.4 mills/kW-hre. For UO2, the minimum 152 COE is 19.7 mills/kW-hre for 5% enriched fuel, and occurs at P/D - 1.35, Drod = 9.33 mm. This is larger than the major backfit minimum COE, which is 17.9 mills/kW-hre. For utilities considering minor backfit, UZrH1. 6 may therefore offer an economic advantage at 60 psia. Because the minimum cost occurs very close to the reference core configuration, changing the existing core geometry may not be necessary. This would allow the incorporation of hydride assemblies into the existing core via the regular refueling outage schedule (i.e., replacing discarded U0 2 fuel assemblies with UZrHI.6 fuel assemblies for 3 successive outages until the core is operating entirely on hydride fuel). This would eliminate the capital cost penalty associated with the discarded UO2 fuel and improve the overall economics. As for major backfit, however, the magnitude of the cost advantage for UZrHt 6 is not large given the uncertainties in the overall economics analysis. Figure 4.30 Minor Backfit COE and its Components vs. P/D for UZrH1.6 at 60 psia A. COEvs P/D 0MCostvs P :C E7J;-1 -' B FCCvs Pr 2,~-.....:'Ets ~' 4 --- T ,, ! 1X 12 13 14 2 10 Enrichment : ?--~-i-,: o CapaCostvs - P: - -............ . ; .... ....................... ~s,-.....~..........c nictinent 1 51 no 7 5°%Q Ervtil en) ='%Eichmen ........... .......... ,t4-2r ------_ -: : - ---- --- .a...-: 014 ... .......... 1i.. ...... 2 - - ii - .-...... .-.- . 1- - --.. --.~ ......... .................. .1.5 .i..1 3 ___-_-_ 10 L------14 1.1 12 P.D .. 11 .......... ._._._ 12 .... ........ .. .. 13 P/D 14 1.5 153 Figure 4.31 Minor Backfit COE and its Components vs. P/D for UO2 at 60 psia A cOE .i PD *" 8 FCCvs PO 2(0 :i 3 -u J ------- -*i r -..,...........----I ::........... -........ - L E 12 c b Eu ' (2 -----,.- :. . . . .. . . . :/ ',y .__ __ 1 12 13 _ 14 : 1 5I 12 + C 0 & M ¢o;tvs O0Capltal cost; V( PO 2 ~ ~ .................... - ............... ,-. i,~ i --- ---------------i------- 1 :.................... <T> I I 15 Erllllcrenrl[t - Co: , 14 PD ; PO i- . l", : 1:3 5 % Erln: lrler el !o)5 Erlri: lrnerlt PiD IT ~ if : ' , ............ ............... . ......... -------1 P9D 1-6 - . ... .. .. . .. . .. = 11' ..... . ................. 1 ~ ... i3 1 - ------ . i 12. ---- 1 _: __-: PO 4.6.3 Results for Major Backfit: UZrHI.6 and UO2 at 29 psia The lifetime levelized unit cost of electricity for the major backfit scenario at 29 psia is shown in Figures 4.32 and 4.34 for different enrichments of UZrH1. 6 and U0 2. The minimum COE at each P/D ratio is fitted to a black contour on each plot. Figures 4.33A and 4.35A plot these lines independent of rod diameter to provide a clearer comparison of the COE among different enrichments and fuel types. Also shown in Figures 4.33 and 4.35 are the fuel cycle, O & M, and capital costs that comprise the minimum COE. The minimum COE for UZrHI 6 is 19 mills/kW-hre for 12.5% enriched fuel at: P/D = 1.37, Drod= 8.4 mm. The minimum COE for UO2 is lower at 18 mills/kWhre for 5% enriched fuel at: P/D = 1.47, Drod= 7.13 mm. The cost gap between the most economic UZrHI 6 and U0 2 geometries has therefore widened at 29 psia (1 mill/kW-hre at 29 psia vs. 0.5 mills/kW-hre at 60 psia). Like the 60 psia results, the minimum COE lines tend to follow the crest of the maximum power plots for both UZrH,. 6 and UO2 (compare with Figure 4.2). The costs again are minimized for UZrH. 6 at higher enrichments and for U0 2 at lower enrichments. The analysis provided in Section 4.6.1.1 154 to explain the behavior of the COE curves at 60 psia is not repeated here. Because the logic is similar, the figures for the COE breakdown and corresponding plant operating conditions for 12.5% UZrHi.6 and 5% U0 2 are presented in Appendix E. Figure 4.32 Lifetime Levelized Unit COE vs. P/D and Drodfor Square Arrays of UZrH.6 at 29 psia B. 7.5% UZrH 1 6 (mills/kW-hre) A: 5% UZrH 1 6 (mills/kW-hre) 12 70 E E10 II 60 50 50 9 U II 70 12 I 60 11 40 8 7 11 12 13 14 15 I 010 I 40 30 30 11 P/D C: 10% UZrH · - (mills/kW-hre) J 19 , 1.2 1.3 14 15 P/D I 17rH (m illkLAN-hr'· ^^ 1bU 12 70 11 I 60 c~ I 60 EjC 10 E 1 50 9 40 8 E E 40 30 7 I 20 1.1 1.2 1.3 P/D 1.4 1.5 7 20 _1.1 1.2 1.3 P/D 1.4 1.5 155 Figure 4.33 Minimum COE and its Components vs. P/D for Square Arrays of IZrH 6 at 29 psia A: Minimum COE vs F'D B: Minimum Fuel Cycle Costvs. P.D 13 9|5i 5 .... ........... ... . .. 40n ............ 12 - .. ..... 11 El! .. ..-. '! ......... .... ., 10 :. .. .. .. . 0a c 1i : 23 at·?S Si 00Lj 08 a - 7"ms J LL =· ,. - 12 13 P:D 14 1.1 15 C Mlnimtum i & M Co:lstvs o + P- PD J0) 12 5% Ennicrment 7 5% Enrichment 10% Enrichment 12 5% Enrichmenl , A, 3 L.. . . . . .. . . ... i...... 1 4 .. ...... .. ; 4 .. : O , 15 11 Figure 4.34 Lifetime Levelized Unit COE vs. P/D and , oi 13 P'D 12 Drod . * . : . .. , ', 14 15 . for Square Arrays of U0 2 at 29 psia B: 7.5% UO 2 (mills/kW-hre) A: 5% U0 2 (mills/kW-hre) I 80 -1 I 11 60 9 40 8 n 7 80 I 12 100 11 ... *i 2 P:D E El( E10 15 16 -15 1 14 . 25 1 .... . .. ... .. . . . - . . . ... . . ---- ; .. . . i ............ ~o o 13 P') ....... , _ -35 oi ------- C Minimum Capital Cost vs P) fit _ ............... ... 6 11 C -: o . 60 40 Q 7i 1.3 14 1.5 PID C: 10% UO, (mills/kW-hre) 1.1 1.2 I , 12 80 11 I 70 E10 60 7 20 1.1 1.2 1.3 P/D 1.4 1.5 50 40 8 30 7 1.1 1.2 1.3 P/D 1.4 1.5 i 156 Figure 4.35 Minimum COE and its Components vs. P/D for Square Arrays of U0 2 at 29 psia A: MinimumCOE vs. P:D , , , 8 MinimumFuel Cycle Costvs PD Zz I L. 45 . 40 . . * 35 7 . + E 30 0 ( , --- L] i 25 .+ . + * --- - 20 . ,e .-1 2 c 1 10 13 P."D 14 15 a , : 11 _ ,:-an9L22 _I8 - 12 _: - 5%Enrichment 7 5% Enrichment 0% Ennchment 1 PiD 14 ~ 15 C Minimum CapitalCostvs PD C MinimumO &M Cost vs P. D : ......... + A uAh + . ..... 0 000 : E 81 : a~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~ .............. cd o 10 ........ i.t= ~.2i... ..... .......... 11 12 1.3 14 15 PD 11 12 : : 13 P.D 14 :~~, 15 4.6.3.1 Final Comparison for Major Backfit: UZrH. 6 and UO2 at 29 psia The lowest COE for the major backfit scenario at 29 psia is achieved with oxide fuel, though as observed for major backfit at 60 psia, the costs are comparable for both fuels over most of the design range. Figure 4.36A plots the difference in the minimum COE for UZrHI 6 and UO2 as a function of P/D ratio and rod diameter. A black contour is provided to indicate where the cost difference is zero, and divides the plot into regions where overall costs are minimized with each fuel. Figure 4.36B plots the enrichments that correspond to the minimum cost fuel at each geometry. As expected, higher enrichments prevail in the regions where UZrHI.6 is optimum; the opposite is true in regions where costs are minimized with UO2. Though Figure 4.36A shows a large region where savings may be realized with UZrHI.6 (P/D < 1.35), the magnitude of the savings are not large enough to provide overwhelming approval for hydride fuel, particularly in light of the uncertainties in the economics analysis. 157 Figure 4.36 COE Difference and Fuel Enrichment for Major Backfit With UZrHI1 6 and U O2 vs. P/D and Drodat 29 psia A: UZrH. COE- UO, COE FB Enrichmant 10 12 12 12 8 11 6 11 11 4 2 E- 10 I 10 E- 10 0 C 9 -2 -4 F 9 9 8 8 7 -6 6 -8 5 -10 - P/D P/D 4.6.4 Results for Minor Backfit: UZrH1.6 and UO2 at 29 psia The minor backfit results are presented in Figures 4.37 and 4.38 for UZrHt 6 and UO2 at 29 psia. Like the higher pressure drop case, the minimum COE for each fuel occurs very close to the reference core geometry. For IJZrHI 6 the minimum COE is 19.2 mills/kW-hre at P/D - 1.3, Drod= 9.66 mm. For U0 2 the minimum COE occurs at the same geometry but its value is higher at 20 mills/kW-hre. Once again, UZrH. 6 appears to provide the best option for the minor backfit scenario, but not by a significant margin. 158 Figure 4.37 Minor Backfit COE and its Components vs. P/D for UZrH1. 6 at 29 psia A: COE vs. PtD B: FCCvs PD 40 11 A 105 10 :A 20 gA Z a 2i 95 A. 9 A ~~~~~~~~ 8rq LLIj 20 - - - -- -- -- j.., : ~ . .... :._~.......... ·--- '9 .....-....... .. --3 [+;A FJ [] [] _ _ __ _ i _ _ _ 12 14 13 Is -. . . . . C-" . . 7 _ 1 . . .7 15 11 5% Ennchment 7 5% Ennrichment 10% Enrichment A I~ I 12.1b%Enchmer ,t 2 PD c . P o 13 12 : ; ',, ,J~~~~~7 15 i 11 A < o o +, C A _ __ __ 14 15 P"D a u C & M CCostvs ) I D CaltalCost vs FD 18 .;: i&20 iA t I y A~~~ ~d 15 O 14 = 1 I1 AI 40 fE :1 I '~ 1.2 c) 1 A R 11 .......... . ....... ----------. -----.---- ---- - '~ 10 !-~ .--- 12 1.4 08 t 15 1.1 1.2 .~~9 1.3 14 15 PT) PT: Figure 4.38 Minor Backfit COE and its Components vs. P/D for UOz at 29 psia 8. FCCvs PD A.COE vs. PD 20 45 40 a~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~~ 18.--------- ~ ------------~ --- ·- · ------- --A:: .. ........... ' ,-----------...... :.. ------- .................... i 35 ~i 14 ...... -E 30 L'i 0 ( .a. 25 12 16 10 10 I- + ......... ............ ...... --.............. --"'---. - ,-r.. -...--.... ~--~ i--. 20 11 12 1. 14 15 P"D A A C 0 & M Costs vs P/D 20, ~ a 8 11 tr-----2 12 1.3 ~~ 1 14 A .. 1 15 P"D 5% Enrichment 7 5% Ennchment 10% Enrichment D CapitalCostvsPD 16 ! A 1 .. 43 1I a S? 15t·i--' ~ · a; ............ ............ ' ... I ....', ,a, !R a_ 1 -- lt lrl 11 12 13 P"D -. : :a 14 15 0.8 11 12 13 PD 14 15 159 160 5. Conclusions and Future Work This section summarizes the major findings from this report and discusses future work for subsequent researchers on the Hydride Fuels Project. The reader is encouraged to study both sections carefully, as several analyses that support the overall design optimization require modification and improvements in the near futurel2. These changes may affect the final results and conclusions drawn in this report, but their magnitude is unknown at this time. With this said, the framework for the overall optimization methodology laid out is correct, and will continue to be used for quantifying the performance of hydride fuels in PWRs. 5.1 Conclusions This report had three distinct goals: * Updating the steady-state thermal hydraulic analysis performed by J. Malen [1] incorporating recent changes to fixed operating parameters, and verifying the thermal hydraulic equivalence of square and hexagonal array PWR geometries at the same rod diameter and H/HM ratio; * Replacing the single thermal hydraulic design limit on axial velocity with more specific vibrations and wear design limits; * Combining the results from the steady-state and transient thermal hydraulic, neutronic, and fuel performance analyses into an economics model to optimize UZrH1. 6 and U0 2 geometries for incorporation into existing PWRs. 12 The key study that needs to be changed is the fuel performance analysis, which determines the maximum discharge burnup for hydride and oxide fuels subject to constraints on fission gas release and internal pressure, clad oxidation, and clad strain - See Future Work Section 5.2.1.5 for a list of the required modifications. 161 5.1.1 Steady-State Thermal Hydraulics for Square and Hexagonal Array PWR Geometries The methodology for performing the steady-state thermal hydraulic analysis was established by a recent MIT graduate student, J. Malen, who developed an interface between MATLAB and VIPRE to iteratively determine the maximum achievable power for a range of PWR geometries subject to user defined design limits. Design limits were placed on MDNBR, fuel bundle pressure drop, axial flow velocity, and fuel temperature. Recent project decisions to modify the axial power profile and core enthalpy rise used in this analysis required regeneration of J. Malen's maximum power results. These are presented for two pressure drop limits in Figure 5.1 for UO2 and UZrH1 6. Fuel temperature is the only limit that depends on the fuel type. Because it never constrains power, the maximum power plots are identical for UZrH1.6 and UO 2. Figure 5.1 Maximum Achievable Power vs. P/D and Drodfor Square Arrays of UZrH1.6 and UO2at 60 psia and 29 psia Maximum Achievable Power (x 106 kWV.: AP = 29 osia Maximum Achievable Power (x 106 kW. ): AP = 60 osia ___ - - -- - -t - 6 5.5 1 5 45 E 45 4 35 35 3 2*5 25 2*1 2 15 15 1 1 '1 1 3 a I 1 1z 13 14 1 I POD Power increases over the reference design are reported at both pressure drop limits. The maximum power at 60 psia is 5458 MWth at the geometry: P/D = 1.42, Drod = 6.8 mm. The maximum power at 29 psia is 4245 MWth at the geometry: P/D = 1.48, Drod = 6.5 mm. The steady-state thermal hydraulic analysis only considered square arrays, under the assumption that the results could be extended to hexagonal arrays for equivalent rod 162 diameters and H/HM ratios13 . For this condition, square and hexagonal arrays have the same flow area and heated and wetted perimeters and so the thermal hydraulic performance should be similar. A full core hexagonal VIPRE model was constructed at a single geometry for comparison with the square results and the predicted powers were within 1% of each other. The maximum power for hexagonal array geometries can therefore be inferred from the plots for square arrays at the same rod diameter and H/HM ratio. The H/HM ratios are identical when: (P/D)h =1.0746. (PD)s 5.1.2 Vibrations Analysis for Hydride and Oxide Fueled PWRs The steady-state thermal hydraulic analysis did not account for specific vibration and wear mechanisms; instead, a single limit on the axial flow velocity was imposed. The wide range of core geometries considered and the large power increases reported by the thermal hydraulic study makes it prudent to refine this single limit approach. Design limits were therefore developed for key flow-induced vibration and wear mechanisms, and incorporated into the existing thermal hydraulic codes for determining the maximum power. The mechanisms considered were: vortex-induced vibration, fluid-elastic instability, turbulence-induced vibration in cross and axial flow, fretting wear, and sliding (or adhesive) wear. The maximum achievable powers for square arrays of UZrH 1.6 at 60 and 29 psia with vibrations and wear imposed design limits are shown in Figures 5.2A and 5.2C. Figures 5.2B and 5.2D plot the power reductions accompanying the consideration of the additional vibrations and wear limits (i.e, Figure 5.2B is the difference between Figure 5.1A and 5.2A). 13 The same information is plotted in Figure 5.3 for UO 2. This refers to hexagonal geometries using grid spacers. Wire-wrapping was not considered in this report- see Section 5.2.2.2 163 Figure 5.2 Maximum Achievable Power and Power Reductions vs. P/D and Dr,d for Square Arrays of UZrH1 6at 60 and 29 psia with Vibrations and Wear Imposed Design Limits A: Max.Power(kWh,):AP = 60psia B: PowerDifference(kW,): AP= 60psia x1 P _ 1- 12 5 11 2 1 4 15 !I ,13 3 7 I I .5 1Ii 4 1 I I 1 I1 PfD Io PID C: Max.Power(kWh):AP = 29psia 14 19i I 05 0 v D: PowverDifference(kWt,): P = 29 psia Y 1 1) r] 5 2 4 g1 II 3 11 12 1 PlD 14 1s u-0 05 2 I 1 11 12 13 PID 14 " I n -J Figure 5.3 Maximum Achievable Power and Power Reductions vs. P/D and Drodfor Square Arrays of U0 2 at 60 and 29 psia with Vibrations and Wear Imposed Design Limits A: Max.Power (kW,,):AP= 60 psia B: PowerDifference(kW): AP= 60 psia x 10 r -i6 x5 ArV 1 5 lU 4 E 3 5 2 I I-I D: Power Dine (kW): P=29psia C: Max.Power(kW,,):AP= 29psia D: PowerDifference(kWh):AP= 29 psia xjLB -- l x 10 "- 1'1 12 12 11 11 I 10 iA 12 3 10 ?a9 5 2 I ,I z la PID i* I , I I I I P/D 164 The fluid-elastic instability and vortex-induced vibration design limits were not constraining for any geometries 4 . Sliding and fretting wear, however, limited large regions where the axial velocities were greatest, which correspond to the highest power designs. This is why the power reductions shown in Figures 5.2B and 5.2D, and 5.3B and 5.3D follow the crest of the maximum power plots. The peak power geometries at 60 psia for both UZrH. 6 and U0 2 were reduced by - 450 MWth (Refer to Figure 5.1). The peak power geometries at 29 psia, however, were unaffected because the flows in the core are lower. Note that the power reductions plotted in Figures 5.2 and 5.3 are larger for UZrHI.6 than for UO2, because the wear limits applied to UZrHi.6 were more stringent. The wear limits depend on cycle length, which varies by enrichment and fuel type. As revealed in Chapter 4, costs are minimized for 12.5% UZrH 1. 6 and 5% U0 2, and so the cycle lengths from these fuels were used to determine the wear limits. Because longer cycle lengths are achieved with 12.5% UZrH 1.6, the wear limits were stricter and resulted in larger power reductions than for U0 2. This approach ensured that the maximum power input to the economics analysis was specifically adapted to the lowest cost fuels, although ideally a separate vibrations analysis would be performed for each enrichment and fuel type (See Future Work). 5.1.3 Economic Optimization The Hydride Fuels Project aims to quantify the benefits of hydride fuel use in existing PWRs for two cases: major backfit, where the layout of fuel in the core can assume any combination of lattice pitch and rod diameter; and minor backfit, where new designs must maintain the existing core pitch. To this end, an economics analysis was performed to estimate the cost of electricity for retrofit and operation of existing PWRs using UZrH 1.6 and UO2 fuels. Cost estimates were provided for each backfit scenario over a range of core geometries. Fuel cycle, operations and maintenance, and capital costs were considered. The inputs to the economics model included the maximum power from the steady-state and transient thermal hydraulic analyses, and the maximum burnup from the neutronics and fuel performance studies. Recall from Section 3.6.1 that the vortex-shedding design limits were not maintained for P/D ratios < 1.2 because VIPRE experienced problems converging to cross-flow solutions. 14 165 A comparison of the minimum COE for the major and minor backfit scenarios as a function of P/D ratio is shown in Figure 5.4. Subplots A and B provide the major backfit COE for 12.5% UZrH .1 6 and 5% UO2 at 60 and 29 psia. Subplots C and D provide the minor backfit COE for 12.5% UZrH 1. 6 and 5% UO02 at 60 and 29 psia. The two enrichments are chosen because they provide the lowest minimum cost for each scenario5. The lowest COE is obtained for major backfit with UO2 and minor backfit with UZrH1 .6,though the respective cost advantage for each fuel is not greater than - 1 mill/kW-hre. Figure 5.5 shows the difference in the major backfit COE for UZrH1. 6 and U0 2 at both pressure drops over the whole design range. Each region is labeled with the fuel that provides the lowest COE; the magnitude of the cost advantage can be read from the colorbar. Note that the enrichment (not shown) varies across each plot (i.e, even though the lowest cost geometries for each backfit scenario are obtained with 12.5% UZrH1. 6 and 5% UO2, costs are minimized at different enrichments for non-optimum geometries - See Figures 4.29 and 4.36). Overall, costs are fairly comparable for both fuels and neither provides a significant economic benefit for most of the design region (cost difference is typically < - 2 mills/kW-hre). The region where UZrH1. 6 does provide the lowest costs, however, corresponds to geometries with lower maximum powers than the reference core. In light of this, and recalling the uncertainties in the cost assumptions for UZrH 1.6 (i.e, fabrication cost), a strong argument cannot be economically for its use in either the major or minor backfit scenarios over UO.2 15 Note that this does not mean that costs are minimized over the entire design range with 12.5% UZrH 1.6 and 5% UO2. It means that the lowest cost (i.e., at the single optimum geometry) for each backfit scenario is obtained with 12.5% UZrH1. 6 and 5% U0 2. 166 Figure 5.4 Major and Minor Backfit COE vs. P/D for 1TZrH .6 1 and 45 ------------------40 -i· A: MajorBackfitCOEvs. P/D; AP = 60 psia B: MajorBackfitCOE vs.P/D;AP = 29 psia 4 40 "::-........ OM-17 ------..................... : ~-~·---- 35 ;UO 0.0~~~~ Min= 179 - . 18. .E _) i .l0 30 uJ at 29 and 60 psia U02 25 .. , . . ....L D ..... '...... ......-............... O2=-- ,'- UZrH6 Mm ;. 19 w 20 20 15 40 1.1 12 13 P:D 1.4 1.5 C: MinorBackfitCOE vs. P/D; AP = 60 psia "" _ . 13 P;D 12 O 12 5%UZrH16 5% U02 ........ 30 ,-- D: MinorBackfitCOE vs.P/D; AP = 29 psia - -. - - ............-- . - - . ...... . - 40 .. . . o 2 MIln - Il 35 185 E- 30 12 11 13 14 -,-O ---- UZrH16Mn. 19.2 o 25 - 8 6 \../. 20 4\..·.. 15 15 ....... . . .oL . o ......- ":... b - *~" \ ......- ............... ::.0.. . --·--% .... .:.? 20 .... UO Min.=20 / .------ .-----------. UZrH 6 Min E 15 15 45 35 Uj J ii 14 11 12 - -------- ............ ~.---... 13 14 1'5 PiD PiD Figure 5.5 Major Backfit COE Difference vs. P/D and Drod for UZrH1. 6 and UO2 at 60 and 29 psia lJZrH., 6 COE- UO2 COE: P 60 psia UZrH1.COE- UO2 COE:AP = 29 psia 10 10 8 8 6 6 4 4 2 2 E 0 0 -2 C) -2 -4 -4 -6 -6 -8 -8 -10 I I1 IZ P/D 14 I I 1 IJ. PiD Iq 1 -10 Note that all cost figures provided in this section are for square array geometries, but the costs for hexagonal designs can be inferred for the same rod diameters and H/HM ratios. 167 A final note is warranted on the economics results. As mentioned in the beginning of Section 5, the fuel performance limited burnups may not be accurate because of mistakes in the existing analysis. These mistakes will be corrected shortly, but not soon enough for incorporation in this report. The economic impact will most likely be limited, however, to UO2 because the achievable burnups for UZrH 1. 6 as presented in Section 4.4.2 are constrained primarily by neutronics limitations. 5.2 Future Work The issues that arose during this thesis requiring attention by subsequent researchers on the Hydride Fuels Project are discussed in this section. The future work is divided into two categories: methodology and new approaches. The methodology section provides suggestions for improving the existing analysis for the design and optimization of hydride fueled PWRs (i.e, as discussed in this report and shown in Figure 1.1). New approaches apply to changes in the underlying assumptions and structure for the analysis that may improve the project's ability to assess the feasibility of the use of hydride fuels in LWRs. 5.2.1 Methodology 5.2.1.1 Steady-State Thermal Hydraulic Analysis As discussed in Section 2.1.2.1, the MDNBR limit for the steady-state thermal hydraulic analysis was obtained by executing VIPRE for the reference core geometry and operating conditions. The W-3L correlation was adopted for predicting the critical heat flux (CHF). It is thought that this correlation may be limited for the large range of geometries considered in this study. More specifically, the applicability of the W-3L correlation for smaller rod diameter geometries has been questioned. Among other things, it is believed that the CHF depends on the spacing between mixing grids, L, and the equivalent diameter of the sub-channel, De. Quantified as an L/De factor, the effect reduces the critical heat flux for fixed operating conditions as the rod diameter decreases. There is no L/De factor in the W-3L correlation, and the large power estimates from the 168 steady-state thermal hydraulic analysis for small rod diameters may be too optimistic as a result. While the majority of CHF correlations are proprietary and cannot be released for academic pursuits, further discussion with industry may provide a reasonable approximation of the scaling law for an L/De factor in the W-3L correlation. 5.2.1.2 Vibrations and Wear Analysis 1) The dependence of the wear limits on the cycle length tie the vibrations analysis to the fuel burnup. As discussed in Section 3.4.5.1 and shown in Figure 1.1, the maximum achievable burnup subject to fuel performance constraints depends on the maximum power in the core. Due to this relationship, several iterations are required until both the fuel performance limited burnup and the steady-state power with vibrations and wear limits converge to constant values. Due to time constraints, this iteration was only performed once. Recent work, particularly the development of scripts that automate the generation and extraction of burnup from FRAPCON, will make this task more efficient for future users. 2) Based on results from the economic optimization, the wear limits for UZrH1.6 and U0 2 were determined for single enrichments (i.e, 12.5% UZrH 1. 6 and 5% U0 2). The optimization can be improved by applying enrichment specific wear limits to all fuels in the vibrations and wear analysis. The maximum power will therefore depend on fuel type and enrichment, instead of just fuel type as presented in this report. 3) As discussed in Section 3.6.1, VIPRE experienced difficulty converging to cross-flow solutions for tighter geometries, which precluded the inclusion of the vortex shedding design limits for P/D ratios less than 1.2 in the thermal-hydraulic analysis. Tighter cores are more susceptible to vortex shedding lock-in, and so this problem should be investigated more thoroughly, particularly if future recommendations for new hydride fueled designs fall into this range. It is hoped that an updated version of the VIPRE code will soon be available at MIT, and that the convergence problems will resolved. 169 5.2.1.3 Transient Thermal Hydraulic Analysis The results from the transient thermal hydraulic analysis are important to the overall optimization of hydride and oxide fueled PWRs. The reader is referred to J. Trant's report on transient design [3] for future work in this area. 5.2.1.4 Economics Analysis It is believed that the most reasonable estimates available for the fuel cycle, O & M, and capital cost components of the COE were provided in this analysis, but there is always room for improvement. Examples include: improving the estimate for UZrH1. 6 fabrication costs (or any hydride fuel being examined, for which little to no cost data is available); and solidifying the major plant components requiring modification or replacement for conversion to hydride fuel use and for operation at higher powers. This analysis assumed that the vessel head, core internals, and steam generators required replacement, but additional capacity could be extracted from the turbine with appropriate modifications. 5.2.1.5 Fuel Performance and Application of FRAPCON to Hydride Fuels 1) The FRAPCON code is used to simulate and model the thermal-physical properties of UO2 fuel pins during irradiation. As discussed in Section 4.4.2.2, several assumptions were made to extend its use to hydride fuels. For example, the fuels were assumed to behave identically during irradiation with respect to thermal expansion and fuel swelling. Additionally, the effect of fission gas release and the generation of helium from the use of burnable absorbers were not considered for the hydride case. For a more accurate picture of the achievable burnup in hydride fuel, these effects require consideration. This can be accomplished by incorporating thermal properties and correlations for fission gas release and swelling in hydride fuels directly into the FRAPCON code. 2) In the near future, several changes will be made to the FRAPCON analysis to correct existing mistakes, which will improve the estimates for the fuel performance limited burnups for both fuels. These changes are summarized below: 170 * The axial power profile used in the FRAPCON analysis was incorrect, and needs to be changed to the profile used in the thermal hydraulic analysis (chopped cosine) with the same peaking factor. * For conservatism, the fuel performance analysis assumed that all fuel assemblies in the core were subjected to the operating conditions for the peak pin over the entire operating cycle' 6. The burnup used in the economic optimization should therefore be the average burnup given by FRAPCON for this peak pin. The bumup in this report, however, was mistakenly taken from the peak fuel pellet in the peak pin, which is larger than the average bumup for the rod. Making this correction will have a greater impact on the U02 results because most of achievable bumups for the parametric design range were limited by fuel performance limits. 5.2.2 New Approaches 5.2.2.1 New Fuels While this report focused on establishing a methodology for the design and optimization of hydride fueled PWR cores, results were only presented for UZrHI.6 and UO2 . As discussed in Section 4.4.2.1 none of the geometries in this study demonstrated acceptable moderator temperature coefficients, which will deter industry from its use unless resolved. Preliminary neutronics work indicate that other hydride fuels (i.e., UZrH,.6-ThH2) do not have this problem. The design and optimization should therefore be carried out for new hydride fuels. A list of candidate fuels being considered now by UC Berkeley include: UZrHI. 6, PuZrH. 6, PuH 2-ThH 2, UH 2 -ThH 2, UZrH. 6-ThH 2, and PuZrH1 .6 -ThH2. Note that the fuel performance, steady-state thermal hydraulics, and vibrations work can be performed for the new fuel types using the construct provided in this report. Minor modifications will be required to the economics analysis to estimate 16 The linear heat rate input to FRAPCON was the average linear heat rate given by the thermal hydraulic analysis multiplied by both the radial and axial peaking factors (i.e, x 1.65 x 1.55) 171 costs associated with: fuel fabrication, the use of thorium, and reprocessing to extract plutonium. 5.2.2.2 Hexagonal Arrays and Wire Wrap The square and hexagonal array PWR designs considered in this report employ grid spacers. The use of wire wrapping in hexagonal arrays, however, may improve the thermal hydraulic performance in the pressure drop limited regions (i.e, tighter geometries) because the pressure drop across the fuel bundle will be reduced. To quantify this benefit, the vibrations performance of wire wrapped fuel assemblies will need to be assessed, and new CHF correlations applicable to wire wrapped fuel rods will need to be adopted. J. Trant performed some preliminary work regarding the performance of wire-wrapped fuel assemblies; the reader is referred to [3] for this information. 5.2.2.3 Reference Core The reference core adopted for this analysis is the South Texas Plant, which is unique among current US LWRs because of its longer core length. The standard LWR core is 12', but South Texas is 14'. To better quantify the performance and benefits of hydride fuel use for the remaining US fleet, the project may consider changing the reference core to a more representative LWR. 172 Bibliography [1] J.A. MALEN, N.E. TODREAS, A. ROMANO, "Thermal Hydraulic Design of Hydride Fueled PWR Cores," MIT-NFC-TR-062, MIT, Department of Nuclear Engineering, March 2004. [2] M.S. KAZIMI, N.E. TODREAS, Nuclear Systems II, Elements ofThermal Hydraulic Design, Taylor & Francis, 1993. [3] J.M. TRANT,"TransientAnalysis of HydrideFueledPressurized WaterReactor Cores, " S.M Thesis, MIT, Department of Nuclear Engineering, August 2004. [4] M.S. KAZIMI, N.E. TODREAS, Nuclear Systems I, Thermal Hydraulic Fundamentals, Taylor & Francis, 1993. [5] S. BLAIR,"Thermal HydraulicPerformanceAnalysisof a SmallIntegralPWR Core," Engineers Thesis, MIT, Department of Nuclear Engineering, Sept. 2003. [6] M.K. AU-YANG,Flow-InducedVibrationof Power and Process Plant Components, pgs. 62, 141, 149, 166-167, 181, 259, 265-267, 308, 359, ASME Press, New York, 2001. [7] M.S. KAZIMI, "High Performance Fuel Design for Next Generation PWRs: Annual Report, " pg. 84, MIT-NFC-PR-048, MIT, Center for Advanced Nuclear Energy Systems, August 2002. [8] J.G.B. SACCHERI, "A Tight Lattice, Epithermal Core Design for the Integral PWR, " Ch. 4, PhD Dissertation, MIT, Department of Nuclear Engineering, August 2003. [9] NEA/OECD, The Economics of the Nuclear Fuel Cycle, OECD Publications, Paris, 1994. [10] DOE, NuclearEnergy CostData Base: A ReferenceData Basefor Nuclearand Coal Fired Powerplant Generation Cost Analysis, DOE/NE-0095, Washington, DC, Sept. 1988. 173 APPENDICES TABLE OF CONTENTS A NOMENCLATURE A. 1 A.2 .................................................................... GENERALNOTATION......................... ............................................ SUBSCRIPTS..................................................................... B LISTED ASSUMPTIONS OF VIPRE THERMAL HYDRAULIC ANALYSIS B. 1 B 1.1 B. 1.2 B. 1.3 B. 1.4 B. 1.5 B. 1.6 B. 1. 7 B. 1.8 B. 1.9 175 175 178 ............... ASSUMPTIONS COMMON TO FULL CORE SQUARE AND HEXAGONAL ARRAY ANALYSIS ........... onstraints.......................................................................................................................... Channel Geometry.............................................................................................................. Fuel Rod Geometry............................................................................................................. Operating Conditions ........................................ Grid Spacers .............................. Pressure Loss Correlations ........................................ NB, Heat Transfer Correlations............................. Material Properties ............................................................................................................. Radial Power Profile ........................................ B.1.10 LateralDrag.................................... 180 180 180 180 180 180 181 1......................................... 181 182 184 184 185 C VIPRE INPUT DECK .................................................................................................................... 186 D MATLAB TOOLS ....................................................................................................................... 199 D.1 D.2 D .3 'SQ CORE MAX VIBRATIONS".................................... 199 "VIBRATIONS"......................................................................................................................... "E ONOMICS ......................................................................................................................... 205 212 E COE COMPONENTS AND PLANT OPERATING CONDITIONS FOR 12.5% UZRH1.6 AND 224 5% U0 2 AT 29 PSIA FOR MAJOR BACKFIT.................................... 174 A NOMENCLATURE A.1 GENERAL NOTATION A: Ac,: Aflo,: ChannelArea CladdingArea ChannelFlow Area Afuet.' FuelArea Agrid. Wetted Area of Grid Ao. Arod.' Rod Area BOP. Wetted'Area of Rod at GridSpacer Balanceof Plant Bu. C: Burnup Unit Cost CB,.' CB,2: CF. Non Mixing Vane Drag Coefficient Mixing Vane Drag Coefficient Cash Flow Cf FrictionalDrag Coefficient C'ev": Lifetime Levelized Unit Cost Clev:' Lifetime Levelized Cost Cm.' CN C:.' Added Mass Coefficient Nth Cash Flow Initial Cash Flow cp. constantpressurespecific heat CR.' Random Lift Coefficient D.' Rod Diameter DJ.: Length Across Hexagon Flats Dh:.' HydraulicDiameter DI. Length of Hexagon Side Eannu,,a.Annual Energy Production EFPY.' Effective Full Power Years EFPYc. Effective Full Power Yearsper Cycle E.' Young's Modulus f ' FrictionFactor Feed Enrichment NaturalFrequency F.' Dimensionless Frequency FIM.' Fluid-ElasticInstabilityMargin FN.' FOR.' Normal Contact Force Forced Outage Rate Fq.: RadialPeakingFactor Fq a.ial. Axial Peaking Factor f: VortexSheddingFrequency g: Radial Gap Thickness EscalationRate 175 Rod to Duct Spacingfor HexagonalAssembly G: GF:. Mass Flux Random Force Power Spectral Density Gp. PressurePowerSpectralDensity h: Enthalpy Heat Transfer Coefficient Enthalpy Rise of Coolant # of Hydrogen Atoms Ah: H: GridSpacer Height HM: # of Heavy Metal Atoms H/HM. Hydrogen to Heavy Metal Ratio I: J: Momentof Inertia JointAcceptance Krod.' Material Wear Coefficient L.' Length Ls: CapacityFactor SpacingLengthfor GridSpacers L,: Total Fuel Rod Length L': l: Availability Loss Coefficientfor Front EndFuel CycleProcesses m: Capital Cost Component Scaling Factor LinearMass n: M.' Mass Flow Rate Mass Molecular Weight n: Mass Flowsfor Front and Back End of Fuel Cycle # of batches N: Vibration Mode # # of Rods NA: ng: n,: Npers: Nps: Avagadro's # # of GridSpacers # of RodSpans # of Plant Personnel # of Rods Per Side in HexagonalFuelAssemblies Nrigs: # of Rings in Hexagonal Fuel Assemblies p: ProductEnrichment P.' Lattice Pitch System Pressure AP: PressureDrop Pitch to DiameterRatio P/D: Heated Perimeter Wetted Perimeter Pw.' PVot,,,. Present Value of Costs Ph: q' .' CoreAverage LinearHeat Rate q" Heat Flux 0: CorePower 176 Q: ,.* R: r.· Re.' s: Volumetric Wear SpecificPower Radius Radial Location Nominal Interest Rate/Discount Rate Reynolds # Gap Width S.: Strouhal # Sd: t: Slip Ratio Sliding Distance Thickness Tails Enrichment T. Time TAV: Tc: Temperature Available Cycle Length Cycle Length TN: Timefor Nth Cash Flow Tant,: Plant Lifetime UC. Unit Cash Flow per Kg of HM in the Core v: Velocity V.. Velocity Volume PotentialFunctionfor SWU Calculations Vcri,icaI:Critical Velocity VSM: w. Vortex Shedding Margin Weight Percent Heavy Metal W.' wi: x: X: Wear Rate Mass Flow Rate Between Adjacent Channels i andj Quality # of Hydrogen Atoms Per Unit of the Fuel Element xe. Equilibrium Quality Y: yrms. Ymax: z: # of Heavy Metal Atoms Per Unit of the Fuel Element Root Mean Square Rod Response Maximum Rod Response Axial Position ZD: Axial Position for Onset of Significant Void Fraction a: VoidFraction f: Connors' Constant Mixing Coefficient Relative Plugging Ratio c: L/D Enrichment DampingRatio ll: p: ,u: Thermal Efficiency Density Coefficient of Friction 177 {o: Viscosity Axial Flux Distribution Pp%: twophasefriction multiplier a1: Mode Shape RadialPowerDistribution A.2 SUBSCRIPTS axial: b: cap. CB: Axial Direction bulk Property Capital Condie Bengston cl.' Clad CL. Centerline cli: CladInner clo: conv: core: Clad Outer Conversion Core cross: Cross/LaterialDirection DB.' disp: Dittus Boelter Waste .Disposal drag: DragDirection eff.' Effective enr: Enrichment fab: SaturatedLiquid Filmfor GroenveldCorrelation Fabrication fcc. fg.' Fuel Cycle Cost Latent Heat of Vaporization fl. Fluid/Coolant FO.' ForcedOutage form.' Form Loss fretting: Fretting Wear fric.' FrictionLoss g: Saturated Vapor Gap grid: Grid h: Heated hex: HexagonalArray H,O0. Water HM. Heavy Metal i: IncipientBoiling inlet: Core Inlet 1: LiquidPhase L: Laminar 178 lo: lift: Liquid Only Lift Direction MixtureProperty matrix: Fractionof Fuel That is Not HeavyMetal m: mv. Mixing Vane n. ModeShape # new. New Design/Geometry O&M. Opeationsand Maintenance ore. Mining/Ore pellet: Fuel Pellet pers: PlantPersonnel plant: Plant PowerPlant PP' ref: repl. RO. rod: Reference Core Replacement Energy Refueling Outage sat. Fuel Rod Saturation SG: Steam Generator sliding: Sliding Wear sq: SquareArray stor: Spent Fuel Storage t: T. Total Turbulent Thermal Turbine th: turb. vessel: Pressure Vesseland Head w. Wall 179 B LISTED ASSUMPTIONSOF VIPRE THERMAL HYDRAULIC ANALYSIS The thermal hydraulic assumptions are taken from [1], with appropriate updates for the changes discussed in this report. B.1 ASSUMPTIONS COMMON TO FULL CORE SQUARE AND HEXAGONAL ARRAY ANALYSIS B.1.1 CONSTRAINTS 1. UZrH 1. 6 fuel CL temperature limited to 750 0 C (1292°F) 2. UO2 fuel average temperature limited to 14000 C (2552°F) 3. MDNBR limit: 2.173 using W3-L DNB Correlation 4. Core average enthalpy rise: 204 kJ/kg B.1.2 1. 2. 3. 4. CHANNEL GEOMETRY Square and hexagonal Core height: 4.59m (181.1") Active fuel length: 4.267m (168") Axial nodes: 100 B.1.3 FUEL ROD GEOMETRY i. Clad/gap thickness ifDrod < 7.747 mm ifDr t,,= .508mm (B. 1) tg =.0635 mm (B. 2) :>7.747 mm t,l= .508 +.0362(D- 7.747) mm (B. 3) tg =.0635+.0108.(D-7.747) mm (B. 4) 2. Radial nodes: 6 3. Gap geat transfer coefficient (LM only): hg = kg/(Rfoln(Rci/Rfo)) 4. LM material properties are listed below B.1.4 OPERATING CONDITIONS 1. Axial power profile: chopped cosine curve 2. Radial Power Profile Peaking Factor: Fq' = 1.65 Peak/Average 3. Inlet Temperature: 294°C (561.2 °F) 4. Operating Pressure: 15.513 MPa (2250 psia) 180 5. Heat generated directly in the coolant scaled as Hc/(Hc+HF) where Hc is the amount of H in the coolant and HF is the amount of H in the hydride fuel. The reference case is 2.6% direct deposition B.1.5 GRID SPACERS 1. Square: 10 grids spaced axially at the following positions, subscript corresponds to loss coefficient used: 0.001, 0.0601, 0.1482, 0.5292, 1.0512, 1.5732, 2.3562, 2.8782, 3.1392, 3.6612, 4.1832 m (0.00001, 5.84001, 20.84002, 41.39002, 61.94002, 82.49002, 103.04002, 123.59002, 144.14002, 164.69002 inches) 2. CB,I for non mixing vane grids is evaluated from In Et Al. Arod 1 c (1 )2 fricrd A Agrid ) + Cfric,gridAiow (1 -)2 B,I = Cd,form (I Agridfrolfal((B-6) Ag= dfro Arod = Pw,rodH Agrid= HPw,grid (B-5) (B-6) flow (B- 7) H = 38mm tsacer =.5mm (B-8) Cd,form = 2.750- .27 log 10 ReD H Cfric,grid= CL,grid +CTgrid H LI Re, =,EG 30000,u 1.328 CL,gri d G Cfric,rod A Aflow CT,gid ReL, (B-9) H = f H =.184Re;2 DH .523 [1n(.06ReHL .2 )]2 (B-IO) (B-Hl) DH 3. CB,2for mixing vane grids included an additional term due to the additional flow constriction of mixing vanes. (B-12) CB,2 = CB,I + CB,mv V (CBmvCd mv 6 Cd,mv = 0.72 A (B-13) B.1.6 PRESSURE LOSS CORRELATIONS The Cheng-Todreas for friction in square and triangular rod bundles was chosen. The coefficients are listed in Table B-l: Coefficients for Cheng Todreas Friction Loss Correlation fL = Re Cf => CfL = a + b (P/D -1)+ b2(P/D - 1)2 (B-14) = a+b(P/D -1)+ Re.'"~~~+b -) (P/D (B-15) frT = Re, 8 =C b2 1) 181 Table B-1: Coefficients for Cheng Todreas Friction Loss Correlation 1.1 < P/D < 1.5 1.0 < P/D < 1.1 b2 bl -493.9 374.2 a bl b2 35.55 263.7 -190.2 -.09926 Square Laminar a 26.37 Square Turbulent .09423 .5806 -1.239 .1339 .09059 Triangular Laminar 26.00 888.2 -3334 62.97 216.9 -190.2 .03632 -.03333 Triangular Turbulent .1458 -8.664 1.398 .09378 B.1.7 DNB, HEAT TRANSFERCORRELATIONS 1. Flow Correlations a. Subcooled void: Levy X(Z) = Xe (Z)- x Xe (ZD ) exp X e (' qt :>ATd = hfg ph, zO) YB<O PhhDB Xe(ZD) = - (B-16) ( (z) -1 -5QPr O<Y_<5 YB (B-1 7) p.'-~nn-5Q Pr+1n[+Pr(YB5 -1)11 phhDB-5QPr+n[1+5Pr]+.5n(YB30)} C gcDe YB 0.015 #.f Vf 2 Q= q'lP Re hDB = .023 '8 Pr .4 f = CD Re - -' 8 (B-18) Gcp(.125f)Y2 b. Bulk void/quality: homogeneous a(z) = =>S = 1 +I-x(Z)p, 1+ -SS x(z) p, (1 -19) c. Two phase friction multiplier: homogeneous ?-20) Pm (Z) [( /lr : )P Pm(Z)= a(z)Pv +(1- (z))p] ( ?-21) 2. Heat Transfer Correlations a. Single phase forced convection: Dittus-Boelter for turbulent flow 8 hDB =.023 Re- Pr' 4 ( B-22) b. Subcooled nucleate boiling: Thom w/ Dittus- Boelter for single phase c. Saturated nucleate boiling: Thom w/ Dittus - Boelter for single phase 182 hThom= [(T w - Tsa,)exp(p/1260)12 .0722 (T - Tb) T,,t = Fluid Saturation Temp (F) Tb = Bulk Fluid Temp (F) T = Wall Temperature (F) (B-23) p = system pressure (psia) d. CHF Correlation: W3-L (L-grid factor = .042, grid spacing factor =.066, L-grid coefficient = 1.0) q 'cri, =[( -b2p) + (b3 b4 p)e(b 5 b6P) e ][(b 7 - b8e + bgXe IXe)G + 0 ] 74) -b l [b11- b52Xe][b 3 + bl4e De][b16 + b7 (hf - hinet)] :>f (p,G,e,De,hf ,hinet ) / = 2.022 b7 =.1484 b13 =.2664 b2 =.0004302 4 = 1.596 44 =.8357 = b5 bg .1729 b3 =.1722 = bo 1.037 b4 =.0000984 b5= 18.177 = 3.151 25) = b 16 .8258 b,7 = .000794 1 = 1.157 b12 =.869 b6 =.004129 e. Transition Boiling: Condie-Bengston q"cB = C 1 (T - Tsa ) exp C,= exp[In (q"chf q"b ) + 0.5(Twchf Tsat)I/2 -In (Tw-chfq"chf = q"j Tsat)] (B-27) criticalheatflux = film boiling heatflux q "chf = h (T-chf - Tf ) f. (B-26) 2 ,,at)/2 (T (B-28) **.qcB = qchf - q jb Film boiling: Groeneveld 5.7 q "b = hfb (Tw - Ta k hfb = 0.052k Re. DH 68 8 (B-29) ) Pr' 26 Ho f y,.06 (B-30) 1 (B-31) Y = 1.0-0.1 (I-x) (P1 SCp-vv ) ReHom =GxD ga (B-32) (B-33) 3. DNB Correlation: W3-L, see Heat Transfer Correlations, 2.d 183 B.1.8 MATERIAL PROPERTIES The material properties are organized in Table B-2. Table B-2: Material Properties used for the Parametric Study P Cp k UZrHi 6 17.6 W/m-K (10.169 Btu/hr-ft-F) UThH2 Same as UZrHi. 6 Same as UZrH6 -3 +3.3557E-6T 1.2058E-3 2 VIPRE lookup table Zirc~ 2 3218E-(T Cp(u) (1.305E-4)T+O. 1094 J/g-C J/g-C (.06976T+33.706)/92.83 Cp(zrH1.6) Cp(UZrHI.6)= .45 Cp¢(L)+ .55CP(ZrHI.6) +1.2315E-12*T 3/ft3 (515.4 ibm/f) 10.852 g/cm 3 (677.46 bm/f 33)) (677.46 lbm/ft 6.55 g/cm 3 3 (409.7 Ibm/ft ) (409.7 lb 7.968 g/cm 3 Btu/s-ft-F 9.01748+1.62997E-2T- SS 8.256 g/cm 3 (515.4 3 18422E-9T 4.80329E-6T2+2. (497.4 bm/ft3) Not Provided W/m-k 9.049 g/cm 3 173.4 J/kg-K 35 W/m-K (564.9 Ibm/ft3 ) (0.0414 Btu/lbm-F) (20.222 Btu/hr-ft-F) *indicates that VIPRE defaults were used instead of values from Reference Database LM B.1.9 RADIAL POWER PROFILE The radial power profile, shown in Figure B-l has the following properties: core core = j2 0J r = 3" > =O dr (B-34) (r)rdrdO R V(r)=Fq, (B-35) = 1.65 Figure B-l: Radial Peaking Factor vs. Core Radius 1 T- T- I I 16 I - --- -- -- T I .. I I - - -- T I I I I I 15 14 ~~ I~ - ---- I I ! 13 I-l-- I . -1 C-I- ~ ~~~~~ 11 I I I 1 I I 1 09 08 3 Fql= 8 8628e-O36*r-0 00081337'r +0 0657179r+1 Q402 A . S 0 10 A I 20 L 1 30 I I 40 radius r (rches) 50 -L I I 60 70 B.1.9.1 Mixing Coefficient for Internal Subchannel: Rogers-Tahir /3 = frod 184 + fSgrid (B-36) IProds W (B-37) s=P-D (B-38) Gs square arrays: w hex. arrays: 9 = .005 uRe 1 wiu= .0018Re9 (B-39) S 0.(B-40) a conservative estimate for the total mixing coefficient for the reference core is .038, and the grid component is found using equation (B-36) /Jgrid = .038- rods-ref = .0 33 5 (B-41) the mixing coefficient between lumped channels equals the mixing coefficient between individual subchannels divided by the centroid to centroid distance of the lumped channels (B-42) Flumped i-lumped B.1.10 LATERAL DRAG VIPRE default of uniform lateral resistance factor multiplied by centroid to centroid distance divided by the pitch CD-_ateral =.5 P (B-43) 185 C VIPRE INPUTDECK * Input for Hydride Core With Hexagonal Arrays * Drod = 6.5 mm, P/D = 1.3866 * VIPRE CASE CONTROL * VIPRE.1: KASE, IRSTRT, IRSTEP 1,0,0 Hydride Core Hexagonal Subchannel * CHANNEL GEOMETRY * ____ = _____ =------- ____ * GEOM.1 geom, ?* INFLAG 91, ?* NCHANL, # of channels***************** 0, ?* NCARD, 0 for compressed geometry option 48, ?* NDX, # of axial nodes 0, ?* NAZONE, 0 for uniform axial node length 12, ?* NCTYP, # of channel types 0 * MBWR, 0 for non-BWR geometry * GEOM.2 181.10, ?* ZZ, bundle length (inches) 0.0, ?* THETA, bundle orientation 0.0 * SL, gap/length parameter * GEOM.5 57, ?* MCHN, # of channels of this type 0.028804, ?* CAREA, channel flow area (inA2) 0.401975, ?* CPW, channel wetted perimeter (in) 0.401975 * CPH, channel heated perimeter (in) * * GEOM.6 1,2,3,4,5,6,10,11,12,16,20,21,22,23,24,25 26,30,31,32,33,34,35,36,37,38,39,40,41,42,43,44 48,49,50,51,55,56,57,58,62,63,64,65,66,67,71,72 73,74,75,76,77,78,79,80,81 24,0.021796,0.448625,0.267984 7,8,9,13,14,15,17,18,19,27,28,29,45,46,47,52 53,54,59,60,61,68,69,70 186 1,0.264293,3.751771,3.751771 * 1st lumped subchannel - outer edge of 1/6th 82 1,7.287642,112.29415,99.28794 * 1/2 of assembly 83 1,29.15058,449.1766,397.1518 * 2 assemblies 84 1,48.5843,748.62767,661.91967 * 3.33 assemblies 85 1,68.018,1048.0787,926.6875 * 4.67 assemblies 86 1,87.45174,1347.5298,1191.4554 * 6 assemblies 87 1,106.885,1646.979,1456.223 * 7.33 assemblies 88 1,126.3192,1946.4319,1720.9911 * 8.67 assemblies 89 1,145.7529,2245.883,1985.759 * 10 assemblies 90 1,444.546,6849.94,6056.5639 * 30.5 assemblies 91 *GEOM.7 126, ? * NK, number of gaps 0, ? * NGTYP, gaps are input individually 1, ? * NGAP, gaps are input individually 0, ? * NROW, gaps are input individually 0, ? * ISYM, gaps are input individually 0 * NSROW, gapas are input individually *GEOM. 11 1, ? * K, gap indentification number 1, ? * I, lower channel connected 3, ? * J, upper channel connected 0.09894, ? * WIDTH, width of gap 0.20487 * CENT, centroid distance for gap * 187 2,2,3,0.09894,0.20487 3,2,6,0.09894,0.20487 4,3,4,0.09894,0.20487 5,4,8,0.09894,0.20487 6,5,6,0.09894,0.20487 7,5,11,0.09894,0.20487 8,6,7,0.09894,0.20487 9,7,8,0.0544,0.20487 10,7,13,0.0544,0.20487 11,8,9,0.0544,0.20487 12,9,15,0.0544,0.20487 13,10,11,0.09894,0.20487 14,10,18,0.09894,0.20487 15,11,12,0.09894,0.20487 16,12,13,0.09894,0.20487 17,12,20,0.09894,0.20487 18,13,14,0.0544,0.20487 19,14,15,0.0544,0.20487 20,14,22,0.09894,0.20487 21,15,16,0.09894,0.20487 22,16,24,0.09894,0.20487 23,17,18,0.0544,0.20487 24,17,27,0.0544,0.20487 25,18,19,0.0544,0.20487 26,19,20,0.09894,0.20487 27,19,29,0.0544,0.20487 28,20,21,0.09894,0.20487 29,21,22,0.09894,0.20487 30,21,31,0.09894,0.20487 31,22,23,0.09894,0.20487 32,23,24,0.09894,0.20487 33,23,33,0.09894,0.20487 34,24,25,0.09894,0.20487 35,25,35,0.09894,0.20487 36,26,27,0.09894,0.20487 37,26,38,0.09894,0.20487 38,27,28,0.0544,0.20487 39,28,29,0.0544,0.20487 40,28,40,0.09894,0.20487 41,29,30,0.09894,0.20487 42,30,31,0.09894,0.20487 43,30,42,0.09894,0.20487 44,31,32,0.09894,0.20487 45,32,33,0.09894,0.20487 46,32,44,0.09894,0.20487 47,33,34,0.09894,0.20487 188 48,34,35,0.09894,0.20487 49,34,46,0.09894,0.20487 50,35,36,0.09894,0.20487 51,36,48,0.09894,0.20487 52,37,38,0.09894,0.20487 53,37,51,0.09894,0.20487 54,38,39,0.09894,0.20487 55,39,40,0.09894,0.20487 56,39,53,0.09894,0.20487 57,40,41,0.09894,0.20487 58,41,42,0.09894,0.20487 59,41,55,0.09894,0.20487 60,42,43,0.09894,0.20487 61,43,44,0.09894,0.20487 62,43,57,0.09894,0.20487 63,44,45,0.09894,0.20487 64,45,46,0.0544,0.20487 65,45,59,0.0544,0.20487 66,46,47,0.0544,0.20487 67,47,48,0.09894,0.20487 68,47,61,0.0544,0.20487 69,48,49,0.09894,0.20487 70,49,63,0.09894,0.20487 71,50,51,0.09894,0.20487 72,50,66,0.09894,0.20487 73,51,52,0.09894,0.20487 74,52,53,0.0544,0.20487 75,52,68,0.0544,0.20487 76,53,54,0.0544,0.20487 77,54,55,0.09894,0.20487 78,54,70,0.0544,0.20487 79,55,56,0.09894,0.20487 80,56,57,0.09894,0.20487 81,56,72,0.09894,0.20487 82,57,58,0.09894,0.20487 83,58,59,0.09894,0.20487 84,58,74,0.09894,0.20487 85,59,60,0.0544,0.20487 86,60,61,0.0544,0.20487 87,60,76,0.09894,0.20487 88,61,62,0.09894,0.20487 89,62,63,0.09894,0.20487 90,62,78,0.09894,0.20487 91,63,64,0.09894,0.20487 92,64,80,0.09894,0.20487 93,65,66,0.09894,0.20487 189 94,65,82,0.09894,1.4307 95,66,67,0.09894,0.20487 96,67,68,0.09894,0.20487 97,67,82,0.09894,1.0793 98,68,69,0.0544,0.20487 99,69,70,0.0544,0.20487 100,69,82,0.09894,0.73215 101,70,71,0.09894,0.20487 102,71,72,0.09894,0.20487 103,71,82,0.09894,0.39786 104,72,73,0.09894,0.20487 105,73,74,0.09894,0.20487 106,73,82,0.09894,0.17994 107,74,75,0.09894,0.20487 108,75,76,0.09894,0.20487 109,75,82,0.09894,0.39786 110,76,77,0.09894,0.20487 111,77,78,0.09894,0.20487 112,77,82,0.09894,0.73215 113,78,79,0.09894,0.20487 114,79,80,0.09894,0.20487 115,79,82,0.09894,1.0793 116,80,81,0.09894,0.20487 117,81,82,0.09894,1.4307 118,82,83,3.39,1.7076 119,83,84,6.79,4.567 120,84,85,13.56,5.743 121,85,86,20.34,5.817 122,86,87,27.12,5.842 123,87,88,33.9,5.8535 124,88,89,40.68,5.8593 125,89,90,47.46,5.863 126,90,91,54.24,9.74 * FLUID PROPERTIES * PROP.1 prop, ? * INFLAG 0, ? * NPROP,# of entries in fluid properties table 0, ? * ISTEAM, 0 for no superheated steam properties 2, ? * NFPROP, 2 for EPRI water properties 1 * IPVAR, 1 for property evaluation at local pressure * 190 * ROD INPUT * RODS.1 rods, ? * INFLAG 1, ? * NAXP, # of axial power profiles 60, ? * NROD, # of rods 1, ? * NC, 1 to use conduction model 2, ? * NFUELT, # of rod geometry types 1, ? * NMAT, # of rod/wall properties to be input 0, ? * IGPFF, 0 - no gap conductance forcing fct. 0, 0, 0, 0, 0 ? * NGPFF, 0 - no gap conductance forcing fct. ? * NOPT, 0 - normal rod layout ? * IPOWV, 0 - constant axial power profiles w/ time ? * ICPR, 0 - no CPR calculations * IRFF, 0 - cst. radial power factors w/ time * RODS.2 168, ? * ZZH, heated length (inches) 3.5, ? * ZSTRT, beginning of heated profile (inches) 0, ? * NODALS, 0 - default 0 * NODALT, 0 - default * RODS.3 -1 * NAXN, # of points in axial power profile table, -1 for chopped cosine * RODS.5 1.55 * PSTAR, Peak/Average axial power * RODS.9 1, ? * I, rod ID # 1, ? * IDFUEL, rod geometry type 1.6402, ? * RADIAL, rod radial power factor 1, ? * IAXP, axial power profile table flag for rod I 1, ? * LRDUM, enter the channel number that receives heat from rod I 0.1666 * PHIDUM, fraction of rod outside perimeter facing channel LRDUM 2,1,1.6421,1,*,0.1666,3,0.1666,2,0.1666 3,1,1.6421,1,1,0.1666,3,0.1666,4,0.1666 4,1,1.6438,1,2,0.1666,6,0.1666,5,0.1666 5,1,1.6434,1,2,0.1666,3,0.1666,4,0.1666,6,0.1666,7,0.1666,8,0.1666 6,1,1.6438,1,4,0.1666,8,0.1666,9,0.1666 7,1,1.6453,1,5,0.1666,11,0.1666,10,0.1666 8,1,1.6448,1,5,0.1666,6,0.1666,7,0.1666,11,0.1666,12,0.1666,13,0.1666 191 9,1,1.6453,1,9,0.1666,15,0.1666,16,0.1666 10,1,1.6466,1,10,0.1666,18,0.1666,17,0.1666 11,1,1.6461,1,10,0.1666,11,0.1666,12,0.1666,18,0.1666,19,0.1666,20,0.1666 12,1,1.6459,1,12,0.1666,13,0.1666,14,0.1666,20,0.1666,21,0.1666,22,0.1666 13,1,1.6461,1,14,0.1666,15,0.1666,16,0.1666,22,0.1666,23,0.1666,24,0.1666 14,1,1.6466,1,16,0.1666,24,0.1666,25,0.1666 15,1,1.6477,1,17,0.1666,27,0.1666,26,0.1666 16,1,1.647,1,19,0.1666,20,0.1666,21,0.1666,29,0.1666,30,0.1666,31,0.1666 17,1,1.647,1,21,0.1666,22,0.1666,23,0.1666,31,0.1666,32,0.1666,33,0.1666 18,1,1.6473,1,23,0.1666,24,0.1666,25,0.1666,33,0.1666,34,0.1666,35,0.1666 19,1,1.6477,1,25,0.1666,35,0.1666,36,0.1666 20,1,1.6485,1,26,0.1666,38,0.1666,37,0.1666 21,1,1.6482,1,26,0.1666,27,0.1666,28,0.1666,38,0.1666,39,0.1666,40,0.1666 22,1,1.6479,1,28,0.1666,29,0.1666,30,0.1666,40,0.1666,41,0.1666,42,0.1666 23,1,1.6479,1,30,0.1666,31,0.1666,32,0.1666,42,0.1666,43,0.1666,44,0.1666 24,1,1.6479,1,32,0.1666,33,0.1666,34,0.1666,44,0.1666,45,0.1666,46,0.1666 25,1,1.6482,1,34,0.1666,35,0.1666,36,0.1666,46,0.1666,47,0.1666,48,0.1666 26,1,1.6485,1,36,0.1666,48,0.1666,49,0.1666 27,1,1.6492,1,37,0.1666,51,0.1666,50,0.1666 28,1,1.6489,1,37,0.1666,38,0.1666,39,0.1666,51,0.1666,52,0.1666,53,0.1666 29,1,1.6487,1,39,0.1666,40,0.1666,41,0.1666,53,0.1666,54,0.1666,55,0.1666 30,1,1.6486,1,41,0.1666,42,0.1666,43,0.1666,55,0.1666,56,0.1666,57,0.1666 31,1,1.6486,1,43,0.1666,44,0.1666,45,0.1666,57,0.1666,58,0.1666,59,0.1666 32,1,1.6489,1,47,0.1666,48,0.1666,49,0.1666,61,0.1666,62,0.1666,63,0.1666 33,1,1.6492,1,49,0.1666,63,0.1666,64,0.1666 34,1,1.6497,1,50,0.1666,66,0.1666,65,0.1666 35,1,1.6495,1,50,0.1666,51,0.1666,52,0.1666,66,0.1666,67,0.1666,68,0.1666 36,1,1.6492,1,54,0.1666,55,0.1666,56,0.1666,70,0.1666,71,0.1666,72,0.1666 37,1,1.6492,1,56,0.1666,57,0.1666,58,0.1666,72,0.1666,73,0.1666,74,0.1666 38,1,1.6492,1,58,0.1666,59,0.1666,60,0.1666,74,0.1666,75,0.1666,76,0.1666 39,1,1.6493,1,60,0.1666,61,0.1666,62,0.1666,76,0.1666,77,0.1666,78,0.1666 40,1,1.6495,1,62,0.1666,63,0.1666,64,0.1666,78,0.1666,79,0.1666,80,0.1666 41,1,1.6497,1,64,0.1666,80,0.1666,81,0.1666 42,1,1.6499,1,65,0.1666,82,0.33333 43,1,1.6498,1,65,0.1666,66,0.1666,67,0.1666,82,0.5 44,1,1.6497,1,67,0.1666,68,0.1666,69,0.1666,82,0.5 45,1,1.6497,1,69,0.1666,70,0.1666,71,0.1666,82,0.5 46,1,1.6496,1,71,0.1666,72,0.1666,73,0.1666,82,0.5 47,1,1.6496,1,73,0.1666,74,0.1666,75,0.1666,82,0.5 48,1,1.6497,1,75,0.1666,76,0.1666,77,0.1666,82,0.5 49,1,1.6497,1,77,0.1666,78,0.1666,79,0.1666,82,0.5 50,1,1.6498,1,79,0.1666,80,0.1666,81,0.1666,82,0.5 51,1,1.6499,1,81,0.1666,82,0.33333 52,2,1.6491,1,83,123.5 53,2,1.6271,1,84,494 54,2,1.5633,1,85,823.33 192 55,2,1.4674,1,86,1152.67 56,2,1.3495,1,87,1482 57,2,1.2208,1,88,1729 58,2,1.0917,1,89,2140.67 59,2,0.97321,1,90,2470 60,2,0.82846,1,91,7533.5 * not positive about the centroid location in this outer lumped channel 0 * 0 terminates rod layout input RODS.62 1, ? * I, rod geometry type # nucl, ? * FTYPE, rod type 0.2559, ? * DROD, rod outside diameter 0.2194, ? * DFUEL, fuel pellet diameter 6, ? * NFUEL, number of radial nodes in fuel pellet 0.0, ? * DCORE, central void diameter 0.0154 * TCLAD, cladding thickness * RODS.63 0, ? * IRADP, 0 - uniform radial power profile in pellet 1, ? * IMATF, use fuel properties stored in table 1 0, ? * IMATC, 0 - use VIPRE zircaloy tables for cladding * 0, ? * IGPC, 0 - uniform gap conductance 0, ? * IGFORC, 0 - gap conductance is constant in time 86184.361, ? * HGAP, constant gap conductance 0.9550, ? * FTDENS, fuel theoretical density 0.0000 * FCLAD, fraction of applied power generated in clad RODS.68 2, ? * I, rod geometry type # dumy, ? * FTYPE, rod type 0.2559, ? * DROD, rod outside diameter 0.0, ? * DFUEL, 0 if FTYPE not a tube 0 * NFUEL, 0 - if DUMY type rod * RODS.70 1, ? * N, material type # 140, ? * NNTDP, number of entries in material properties table 515.4 * RCOLD, cold state density of material (lbm/ftA3) * RODS.71 *32.0, ? * TPROP, temperature F *0.05985, ? * CPFF, specific heat (Btu/lbm-F) *10.16909, ? * THCF, thermal conductivity (Btu/hr-ft-F) 32.0,0.05985,10.16909, 77.0,0.06228,10.16909 122.0,0.06468,10.16909, 167.0,0.06707,10.16909 * 193 212.0,0.06943,10.16909, 257.0,0.07178,10.16909 302.0,0.07411,10.16909, 347.0,0.07642,10.16909 392.0,0.07872,10.16909, 437.0,0.08100,10.16909 482.0,0.08326,10.16909, 527.0,0.08552,10.16909 572.0,0.08776,10.16909, 617.0,0.09000,10.16909 662.0,0.09222,10.16909, 707.0,0.09444,10.16909 752.0,0.09665,10.16909, 797.0,0.09885,10.16909 842.0,0.10105,10.16909, 887.0,0.10324,10.16909 932.0,0.10543,10.16909, 977.0,0.10762,10.16909 1022.0,0.10981,10.16909, 1067.0,0.11200,10.16909 1112.0,0.11419,10.16909, 1157.0,0.11638,10.16909 1202.0,0.11858,10.16909, 1247.0,0.12078,10.16909 1292.0,0.12299,10.16909, 1337.0,0.12520,10.16909 1382.0,0.12742,10.16909, 1427.0,0.12965,10.16909 1472.0,0.13189,10.16909, 1517.0,0.13414,10.16909 1562.0,0.13641,10.16909, 1607.0,0.13868,10.16909 1652.0,0.14097,10.16909, 1697.0,0.14328,10.16909 1742.0,0.14560,10.16909, 1787.0,0.14794,10.16909 1832.0,0.15030,10.16909, 1877.0,0.15268,10.16909 1922.0,0.15508,10.16909, 1967.0,0.15750,10.16909 2012.0,0.15994,10.16909, 2057.0,0.16241,10.16909 2102.0,0.16490,10.16909, 2147.0,0.16742,10.16909 2192.0,0.16996,10.16909, 2237.0,0.17254,10.16909 2282.0,0.17514,10.16909, 2327.0,0.17777,10.16909 2372.0,0.18043,10.16909, 2417.0,0.18313,10.16909 2462.0,0.18586,10.16909, 2507.0,0.18863,10.16909 2552.0,0.191.43,10.16909, 2597.0,0.19426,10.16909 2642.0,0.19714,10.16909, 2687.0,0.20005,10.16909 2732.0,0.20300,10.16909, 2777.0,0.20600,10.16909 2822.0,0.20903,10.16909, 2867.0,0.21211,10.16909 2912.0,0.21524,10.16909, 2957.0,0.21840,10.16909 3002.0,0.22162,10.16909, 3047.0,0.22488,10.16909 3092.0,0.22819,10.16909, 3137.0,0.23155,10.16909 3182.0,0.23496,10.16909, 3227.0,0.23842,10.16909 3272.0,0.24194,10.16909, 3317.0,0.24551,10.16909 3362.0,0.24913,10.16909, 3407.0,0.25281,10.16909 3452.0,0.25655,10.16909, 3497.0,0.26034,10.16909 3542.0,0.26420,10.16909, 3587.0,0.26811,10.16909 3632.0,0.27209,10.16909, 3677.0,0.27612,10.16909 3722.0,0.28022,10.16909, 3767.0,0.28439,10.16909 3812.0,0.28862,10.16909, 3857.0,0.29292,10.16909 3902.0,0.29728,10.16909, 3947.0,0.30172,10.16909 3992.0,0.30622,10.16909, 4037.0,0.31079,10.16909 4082.0,0.31544,10.16909, 4127.0,0.32016,10.16909 4172.0,0.32495,10.16909, 4217.0,0.32982,10.16909 4262.0,0.33477,10.16909, 4307.0,0.33979,10.16909 194 4352.0,0.34489,10.16909, 4397.0,0.35007,10.16909 4442.0,0.35533,10.16909, 4487.0,0.36067,10.16909 4532.0,0.36609,10.16909, 4577.0,0.37160,10.16909 4622.0,0.37719,10.16909, 4667.0,0.38287,10.16909 4712.0,0.38864,10.16909, 4757.0,0.39449,10.16909 4802.0,0.40043,10.16909, 4847.0,0.40647,10.16909 4892.0,0.41259,10.16909, 4937.0,0.41881,10.16909 4982.0,0.42512,10.16909, 5027.0,0.43152,10.16909 5072.0,0.43802,10.16909, 5117.0,0.44461,10.16909 5162.0,0.45131,10.16909, 5207.0,0.45810,10.16909 5252.0,0.46499,10.16909, 5297.0,0.47198,10.16909 5342.0,0.47908,10.16909, 5387.0,0.48627,10.16909 5432.0,0.49357,10.16909, 5477.0,0.50098,10.16909 5522.0,0.50849,10.16909, 5567.0,0.51611,10.16909 5612.0,0.52384,10.16909, 5657.0,0.53167,10.16909 5702.0,0.53962,10.16909, 5747.0,0.54768,10.16909 5792.0,0.55585,10.16909, 5837.0,0.56414,10.16909 5882.0,0.57254,10.16909, 5927.0,0.58105,10.16909 5972.0,0.58968,10.16909, 6017.0,0.59843,10.16909 6062.0,0.60730,10.16909, 6107.0,0.61629,10.16909 6152.0,0.62540,10.16909, 6197.0,0.63463,10.16909 6242.0,0.64399,10.16909, 6287.0,0.65347,10.16909 * OPER.1 oper, ? * INFLAG 1, ? * IH, inlet condition specified as uniform inlet temperature 2, ? * IG, inlet flow condition specified by mass flux 0, ? * ISP, 0 - equal mass flux per channel at inlet 0, ? * NPOWR, 0 - power specified in units (kW/ft) 0, ? * NDNB, 0 - no MDNBR iteration 0, ? * IRUN, 0 - run only one case 0, ? * IFCVR, 0 - constant direct heat generation in coolant 0, ? * LUF, 0 - no forcing functions 0 * IHBAL, 0 - specify inlet enthalpy directly OPER.2 0.0, ? * DPS, 0 - use inlet flow BC specified by IG and ISP 0.0, ? * DNBRL, 0 - 0 if NDNB = 0 1.9597, ? * FCOOL, percent of heat generated in coolant 0.001, ? * DNBRC, convergence factor for CHF iterations 0 * IHROD, 0, if NDNB = 0 * OPER.5 2250.0, ? * PREF, operating system pressure (psia) 561.2, ? * HIN, enter average inlet temperature (F) 3.2746, ? * GIN, average inlet mass flux (Mlbm/hr-ft2) * 195 2.4637, ? * PWRINP, core average power (kW/ft) 0 * HOUT, 0 - since exit flow don't reverse OPER.12 0,0,0,0,0,0 * * CORR.1 corr, ? * INFLAG 2, ? * NCOR, # of CHF correlations to use for DNBR calculations 1, ? * NHTC, use correlations for single-phase convection and nucleate boiling only 0 * IXCHF, 0 ifNHTC = 1 * CORR.2 levy, ? * NSCVD, subcooled void correlation homo, ? * NBLVD, bulk/void quality correlation homo, ? * NFRML, two-phase friction multiplier none * NHTWL, no hot wall correction factor * CORR.6 ditb, ? * NFCON, single phase forced convection correlation thsp, ? * NSUBC, subcooled nucleate boiling correlation thsp, ? * NSATB, saturated nucleate boiling correlation epri, ? * NCHFC, critical heat flux correlation cond, ? * NTRNB, transition boiling correlation g5.7 * NFLMB, film boiling correlation * CORR.9 w-31,? * NCHF, DNB correlation epri * NCHF, DNB correlation * CORR.11 0.042, ? * TDCL, L-grid mixing factor * 0.0660, ? * SPK, grid spacing factor 1.0 * FLGRD, L-grid factor converted to R-grid factor * CORR.16 0, ? * KBWR, 0 for no cold wall correction factor 0, ? * NUC, 0 for no nonuniofrm axial flux correction factor 0.85 * CGRID, grid loss coefficient for mixing grids * * MIXX.1 mixx, ? * NFLAG 0, ? * NSCBC 0, ? * NBBC, 0 if 2 phase mixing computed as for single phase 1 * MIXK, 1 if a pair of coefficients entered for each gap * 196 * MIXX.2 0.0000, 0.0000, 0.0000 * MIXX.3 0.061634, 0.0000, 0.061634, 0.061634, 0.0000, 0.061634, 0.061634, 0.0000, 0.061634, 0.061634, 0.0000, 0.061634, 0.061634, 0.0000, 0.061634, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000 0.0000, 0.061634, 0.0000, 0.061634, 0.0000 0.0000, 0.061634, 0.0000, 0.061634, 0.0000 0.0000, 0.061634, 0.0000, 0.061634, 0.0000 0.0000, 0.061634, 0.0000, 0.061634, 0.0000 0.0000, 0.061634, 0.0000, 0.061634, 0.0000 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000, 0.061634, 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.061634, 0.0000, 0.008826, 0.0000, 0.0616, 0.0000, 0.0616, 0.0000 0.0117, 0.0000, 0.0616, 0.0000, 0.0616, 0.0000, 0.0172, 0.0000 0.0616, 0.0000, 0.0616, 0.0000, 0.0317, 0.0000, 0.0616, 0.0000 0.0616, 0.0000, 0.0701, 0.0000, 0.0616, 0.0000, 0.0616, 0.0000 0.0317, 0.0000, 0.0616, 0.0000, 0.0616, 0.0000, 0.0172, 0.0000 0.0616, 0.0000, 0.0616, 0.0000, 0.0117, 0.0000, 0.0616, 0.0000 0.0088, 0.0000, 0.0074, 0.0000, 0.0028, 0.0000, 0.0022, 0.0000 0.0022, 0.0000, 0.0022, 0.0000, 0.0022, 0.0000, 0.0022, 0.0000 0.0022, 0.0000, 0.0013, 0.0000 * DRAG.1 drag, ? * INFLAG 1, ? * NCHTP, # of axial friction correlations to be specified 0, ? * NGPTP, 0 - apply constant loss coefficients to all gaps 1 * KIJOPT, lateral resistance option * DRAG.2 0.1541, ? * ATF, coefficient in turbulent rod friction factor correlation -0.1800, ? * BTF, constant in turbulent rod friction factor correlation 197 0.0, ? * CTF, constant in turbulent rod friction factor correlation 118.396, ? * ALF, coefficient in laminar rod friction correlation -1.0, ? * BLF, constant in laminar rod friction correlation 0.0 * CLF, constant in laminar rod friction correlation DRAG.5 0.5, ? * DUMKIJ, lateral resistance factor applied to all gaps 0.35484 * PPITCH, rod pitch (in) * GRID. 1 grid, ? * INFLAG * 0, ? * KOPT, 0 - constant local loss coefficients 2 * NKCOR, # of correlation sets to be supplied GRID.2 1.4, ? * CDK(1), loss coefficient for non-mixing grid 1.625 * CDK(2), loss coefficient for mixing grid * GRID.4 -1, ? * NCI, all NCHANL channels are in this location set 10 * NLEV, enter number of axial locations * GRID.6 0.0000,1,5.8400,1,20.8400,2,41.3900,2,? 61.9400,2,82.4900,2,103.0400,2,123.5900,2 144.1400,2,164.6900,2, * 0 endd 0 198 0 0o H 0. - m rX Z H UD .O, E .(d U 0 _ I- -e0 *. 3 4_4 o 3op ., H o~O 0 Ez 0 0 ^ Z 04 - ED O 0Z U OEolo co -H W04 H acn OH U C a) F -H Ea H ~4C1 I0H - HZH H C) 103 I o3 C0 4r, cn UC, 0M OH-H -H C H/H020 H 0 024 ' E) I 0) P 4)H En IU i--I I IZ UH a 1 H 4 )k OHz zH 0 0 QWi n t4i 4-I a4 H Cd a U I 0)CxZ uO 0 0 0 :: r.J i 44 UeqW 0 0 Q) W >0 0)02-04 l4 IO - O O I I UE 024 H -H-r) H U) a.._ P 0H 0) '- la 0 (4~ ll J* m , Oz AAN 11H 0 03 IZ HZ H 030 4 44 zoo II I U 2 04H 3P -a) >o0 I ri) ' IIE X= 4x 4C0za HZ I0 4 01 . 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U- , w o NOU -N >-H U N _ ) - 4 XI E El) A S co' I -4Q Q w -H -H 4-, w a) 4 H Q w ww w*HH(U(U( N J) H o\o ¢) aw 'Ul ¢0 ¢U w E COE COMPONENTS AND PLANT OPERATING CONDITIONS FOR 12.5% UZRH,.6 AND 5% UO2 AT 29 PSIA FOR MAJOR BACKFIT Figure E-I COE Breakdown for Square Arrays of 12.5% UZrH1.6 at 29 psia A: COE (mills/kW-hre) 80 12 - 12 11 11 60 E10 9 40 8 E E 10 l E 8 20 1.3 1.4 1.5 P/D C: 0 & M (mills/kW-hre) 1.1 1.1 I 11 7 1.3 1.4 15 P/D D: Capital (mills/kW-hre) 1.2 12 1.2 7 50 I 40 E10 I f 8 20 7 I 10 1.1 1.2 1.3 P/D 1.4 1.5 6 5 E 30 9 224 9 4 3 1.1 1.2 1.3 PID 1.4 1.5 I 2 Figure E-2 Plant Operating Conditions for Square Arrays of 12.5°/, UiZrH.6at 29 psia A: Core Power (x 106 kWth) B: Specific Power (kWth/kgHM) A 12 I 11 10 C 1' I 100 3 E 1 80 2 02 I 12 11 I 604( 7- 1 1.3 1.4 1.5 P/D C: Burnup (MWD/kgHM) 11 120 ._P 8 7 12 11 3 I 7 i 1.2 2( 1.3 1.4 15 P/D ): Annual Enerav Prod. x 10 10 kW-hre) 1.1 140 12 I 120 11 1 0. 8 E E C c 100 I 1.1 1.2 1.3 PID 1.4 0. 6 70' 0.'4 80 7 1.5 0.2 1.2 1.1 1.3 P/D 1.4 1.5 Figure E-3 Plant Operating Conditions for Square Arrays of 12.5% UZrHI.6 at 29 psia B: Cycle Length (vrs) A: Capacity Factor 0.97 12 8 11 0.96 E E 6 1( 0.95 CI r"' -B. F 4 0.94 1.1 1.2 1.3 1.4 1.5 2 1.1 1.3 1.4 1.5 P/D D: Planned Outage Length (days/cycle) P/D C: Annual Outage Length (days/yr) 1.2 20 12 61i 11 15 Et: 1 F 5' -o 0 n2 4 9 E' C1 C .. D9 10 990 3' 0 1 0 21 1.1 1.2 1.3 P/D 1.4 1.5 1.1 1.2 1.3 P/D 1.4 1.5 225 Figure E-4 COE Breakdown for Square Arrays of 5% U0 2 at 29 psia A: COE (mills/kW-hre) B: FCC (mills/kW-hre) 12 11 E 1 100 40 11 80 30 10 60 O1( 40 7 20 8 10 20 1.3 1.4 15 P/D D: Capital (mills/kW-hre) 1.3 1.4 1 5 PID C: O & M (millsIkW-hre) 1.1 1.1 1.2 12 I 11 E10 E 1.2 1 50 I 1 40 4 3 20 7 1.1 1.2 1.3 P/D 1.4 1.5 I 6 5 E 30 Q8 7 I 10 2 P/D Figure E-5 Plant Operating Conditions for Square Arrays of 5% UO2 at 29 psia B: Specific Power (kWth/kgHM) A: Core Power (x 106 kWth) 14 II 3 tf. ~._. ,C: I 50 11 10 9 40 30 2 9 1 8 20 1 7 10 1.3 1.4 1.5 P/D D: Annual Energy Prod. (x 10 10 kW-hre) 1.1 1.3 1.4 1.5 PID C: Burnup (MWDkg,,,) 1.1 E 12 1.2 1.2 12 12 1 50 11 E F 40 10 0.8 E10 ._ E3c 30 9 0.6 8 20 8 0.4 7 1.1 226 11 I 1.2 1.3 1.4 P/ID 1.5 l 10 0.2 1.1 1.2 1.3 1.4 P/ID 1.5 Figure E-6 Plant Operating Conditions for Square Arrays of 5%/1l102 at 29 psia A: Capacity Factor B: Cycle Length (yrs) 12 12 0.96 11 3 11 0.955 E Ei_ 109 2.5 E10 2 0.95 8 0.94' 7 0.94 1.5 7 1.1 1.3 1.4 1.5 PID D: Plainned Outage Length (days/cycle) 1.3 1.4 1.5 P/D C: Annual Outage Length (days/yr) 1.1 8 1.2 1.2 12 18 12 30 11 I 16 11 28 10 26 EE-10 14 24 C 12 8 7 I 10 1.1 1.2 1.3 P/D 1.4 1.5 28 22 20 7 1.1 1.2 1.3 1.4 1.5 P/D 227 Room 14-0551 77 Massachusetts Avenue Cambridge, MA 02139 MITLibraries Document Services Ph: 617.253.5668 Fax: 617.253.1 690 Email: docs@mit.edu http: //libraries. mit.edu/docs DISCLAIMER OF QUALITY Due to the condition of the original material, there are unavoidable flaws in this reproduction. 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