Evaluating Domestic Water Heater Performance for NY Homes Draft Final Report Prepared for: New York State Energy Research and Development Authority Albany, NY Gregory Pedrick, Joseph Borowiec Project Managers Prepared by: Syracuse Center of Excellence in Environmental and Energy Systems Syracuse, NY and CDH Energy Corp. Cazenovia, NY Hugh I. Henderson, Jr., Edward Bogucz, Jeremy Wade NYSERDA Report xx-xx NYSERDA Contract 15606 April 2015 Notice This report was prepared by the Syracuse COE and CDH Energy Corp. in the course of performing work contracted for and sponsored by the New York State Energy Research and Development Authority (hereafter “NYSERDA”). The opinions expressed in this report do not necessarily reflect those of NYSERDA or the State of New York, and reference to any specific product, service, process, or method does not constitute an implied or expressed recommendation or endorsement of it. Further, NYSERDA, the State of New York, and the contractor make no warranties or representations, expressed or implied, as to the fitness for particular purpose or merchantability of any product, apparatus, or service, or the usefulness, completeness, or accuracy of any processes, methods, or other information contained, described, disclosed, or referred to in this report. NYSERDA, the State of New York, and the contractor make no representation that the use of any product, apparatus, process, method, or other information will not infringe privately owned rights and will assume no liability for any loss, injury, or damage resulting from, or occurring in connection with, the use of information contained, described, disclosed, or referred to in this report. NYSERDA makes every effort to provide accurate information about copyright owners and related matters in the reports we publish. Contractors are responsible for determining and satisfying copyright or other use restrictions regarding the content of reports that they write, in compliance with NYSERDA’s policies and federal law. If you are the copyright owner and believe a NYSERDA report has not properly attributed your work to you or has used it without permission, please email print@nyserda.ny.gov. ii Executive Summary This study evaluated a wide array of issues related to the performance of water heaters in New York homes. The study looked at the performance of water heater products ranging from standard gas water heater tanks through high efficiency gas-fired options. It also looked at solar and heat pump options as an alternative to standard electric water heaters. We used laboratory testing to make comparisons between different systems and to discern the impact of the new water use profiles in the forthcoming DOE Test Procedure. Because the water use pattern can have a significant impact on performance, we also measured hot water flow in several homes to understand the magnitude and timing of hot water use. Data were also collected to quantify hot water waste due to the distribution system in several homes. The findings of this research effort as well as more general guidance about water heating technologies are being communicated to a broad audience of homeowners, installers and other stakeholders via web site at http://dhw.syracusecoe.org/. Side-by-side laboratory testing evaluated the impact that different water use profiles have on water heater efficiency. The forthcoming UEF descriptor from the new test procedure will provide a more accurate rating of the performance of tankless water heaters; tankless unit performance had been slightly over predicted by the current EF test and rating procedure. High efficiency products such as the gas-fired condensing tanks and hybrid products – i.e., tankless units with a small amount of storage – will now be rated under the new UEF descriptor which will provide a much more accurate representation of actual efficiency. A side-by-side comparison of different solar hot water systems showed they had similar performance resulting in a solar fraction of 0.46 to 0.47 across the year – providing savings of about one half compared to a standard water heater. This performance was in line with the SRCC-predicted solar fraction of 0.56 for Syracuse. Field measurements of hot water flow in 18 homes determined the magnitude and timing of hot water use. The median hot water use was 45 gal/day, which was closely aligned with other national studies of hot water use. The median two-period household used 39 gallons per day and median 4-person household used 66 gallons per day. We found that hot water use varies by more than a factor of two on a day-to-day basis for any given house. Also, hot water use varies seasonally, especially for large households where showers become a large portion of the mix of total hot water use. Our measurement of hot water waste – that is, previously-heated water that is run down the drain waiting for an acceptable temperature at the fixture – was about 9% to 25% in five houses. In two houses we installed recirculation pumps with return lines to the tank inlet to reduce hot water waste. We found that, while these systems reduced hot water waste, they also increase thermal losses from the system and therefore increased energy use. iii Heat pump water heaters (HPWHs) are promising technology for hundreds of thousands single family NY homes that use electric water heating. Rural and suburban homes with basements are an especially good application. We found that the actual annual efficiency was much lower than the value predicted by the EF (or the forthcoming UEF) due to both relatively cold basement temperatures and occasional operation of resistance elements after a large water draw. However, the HPWH still reduced electric consumption by a nearly factor of two compared to a standard electric water heater. Product improvements are likely to further increase these energy savings. iv Acknowledgements We wish to acknowledge and thank several staff at the Syracuse Center of Excellence (COE) for contributing to this project. Thanks to Ana Fernandez for helping to indentify and recruit field test sites from the Near Westside neighborhood to participate in this study as well as Chris Straile who coordinated the installation of the DHW systems at the laboratory. Also thanks to James Alfiere and his team at the Syracuse University Construction Group for overseeing design and construction of the laboratory infrastructure. We also wish to thank several consultants who provided technical advice and assistance on the project including Thomas Butcher from Brookhaven National Laboratory, Carlos Colon from the Florida Solar Energy Center, and Pete Skinner of E2G Solar. Finally, thanks to the homeowners who agreed to participate in this field test study. v Table of Contents Notice ......................................................................................................................................... ii Executive Summary ....................................................................................................................iii Acknowledgements ..................................................................................................................... v Table of Contents........................................................................................................................vi List of Figures.............................................................................................................................ix List of Tables ..............................................................................................................................xi Acronyms and Abbreviations .....................................................................................................xii 1 2 Introduction ........................................................................................................................ 1 1.1 Background ..................................................................................................................................... 1 1.2 Goals .............................................................................................................................................. 1 1.3 Approach ........................................................................................................................................ 1 1.3.1 Technology Evaluation ............................................................................................................. 2 1.3.2 Laboratory Test ....................................................................................................................... 2 1.3.3 Field Testing ........................................................................................................................... 2 1.3.4 Communicating Results ............................................................................................................ 2 Water Heater Technologies .................................................................................................. 3 Descriptions of Water Heater Technologies ....................................................................................... 3 2.1 2.1.1 Standard Gas Storage ............................................................................................................... 4 2.1.2 High Efficiency (HE) Gas Storage: Non-Condensing .................................................................. 4 2.1.3 High Efficiency (HE) Gas Storage: Condensing ......................................................................... 5 2.1.4 Tankless Gas Water Heater ....................................................................................................... 5 2.1.5 Hybrid Gas .............................................................................................................................. 6 2.1.6 Standard Electric Storage ......................................................................................................... 6 2.1.7 Heat Pump Water Heaters ......................................................................................................... 7 2.1.8 Electric Tankless Water Heater ................................................................................................. 8 Other DHW Approaches .................................................................................................................. 8 2.2 2.2.1 Indirect Tank Systems .............................................................................................................. 8 2.2.2 Ground Source Heat Pump Systems .......................................................................................... 8 2.2.3 Solar Water Heaters ................................................................................................................. 9 Collector Type ..................................................................................................................................... 9 Circulation Approach ........................................................................................................................... 9 2.3 3 Systems Selected for Testing .......................................................................................................... 10 Test Approach and Monitoring Details ................................................................................12 vi Laboratory Test Approach and Setup ............................................................................................... 12 3.1 3.1.1 Laboratory Setup ................................................................................................................... 14 3.1.2 Instrumentation and Measurements ......................................................................................... 14 3.1.3 Data Analysis ........................................................................................................................ 16 Field Testing Approach .................................................................................................................. 17 3.2 3.2.1 Instrumentation and Measurements at Field Test Sites .............................................................. 18 Water-Use Only Sites ......................................................................................................................... 18 Detailed / BA Sites ............................................................................................................................ 19 3.2.2 4 Laboratory Test Results ......................................................................................................23 4.1 Comparing Measured Laboratory Performance to Energy Factor ....................................................... 23 4.2 Impact of NEW Proposed Hot Water Use Profiles ............................................................................ 27 4.2.1 Proposed Normal Use Draw Profile ......................................................................................... 28 4.2.2 Proposed Low Use Draw Profile ............................................................................................. 31 4.2.3 Proposed High Use Draw Profile ............................................................................................. 34 4.3 Comparing Performance with Different Usage Profiles ..................................................................... 39 4.4 Standby Losses and Parasitic Power ................................................................................................ 44 4.4.1 Standby Losses ...................................................................................................................... 44 4.4.2 Parasitic Electric Loads .......................................................................................................... 47 4.5 5 Data Analysis Procedures ....................................................................................................... 21 Comparing Performance of Solar Systems ....................................................................................... 48 4.5.1 Initial Performance Observations (September and October 2013) ............................................... 49 4.5.2 The Wagner Drain-Back System is Fixed ................................................................................. 54 Field Test Results................................................................................................................59 5.1 Characteristics of Field Test Sites .................................................................................................... 59 5.2 Hot Water Usage ........................................................................................................................... 62 5.2.1 Hot Water Use Profiles ........................................................................................................... 62 5.2.2 Average Daily Hot Water Use ................................................................................................. 66 5.3 Entering Cold Water Temperatures ................................................................................................. 74 5.4 Hot Water Draw Events.................................................................................................................. 76 5.5 Identifying Draws and Estimating Hot Water Waste ......................................................................... 79 5.6 Field Test Site 1 – HPWH Performance ........................................................................................... 82 5.6.1 Unexpected Aspects of HPWH Performance ............................................................................ 90 5.6.2 HPWH Interactions with the Space .......................................................................................... 92 5.6.3 Impact of Recirculation Pump on System Performance ............................................................. 99 5.7 Field Test Site 2 – Condensing Storage Tank ................................................................................. 100 vii Field Test Site 3 – Gas-Fired Condensing Tankless......................................................................... 104 5.8 6 Conclusions and Lessons ...................................................................................................106 Summary of Findings and Conclusions .......................................................................................... 106 6.1 6.1.1 Impact of Draw Profile on Efficiency .................................................................................... 106 6.1.2 Side-by-Side Solar Testing ................................................................................................... 107 6.1.3 Hot Water Use Patterns in Test Homes .................................................................................. 108 6.1.4 Disaggregating Hot Water Use and Estimating Hot Water Waste ............................................. 109 6.1.5 HPWH Field Performance .................................................................................................... 109 6.1.6 Impact of Switching to Tankless Unit .................................................................................... 110 6.1.7 Field Performance of High Efficiency Condensing Tank ......................................................... 110 6.1.8 Recirculation Pumps to Reduce Hot Water Waste ................................................................... 110 Lessons Learned .......................................................................................................................... 110 6.2 7 6.2.1 One Water Use Profile May Not Fully Characterize Performance ............................................ 110 6.2.2 Controls and Tank Size Matter for HPWH ............................................................................. 111 6.2.3 HPWH is an Energy Efficient Option in Rural Homes ............................................................ 111 References ........................................................................................................................112 Appendix A Summary of Field Site Characteristics, Survey Responses, and Monitoring and Data Collection Details for 18 Filed Test Sites Sites Descriptions for Five Detailed Field Test Sites Appendix B Histograms of Water Use and Events per Day at each Site Histograms of Event Volume and Duration at each Site Appendix C Daily Hot Water Use Profiles for Each Site Based on 15-minute Data viii List of Figures Figure 1. Annual Trend of Cold Water Inlet Temperature in the City of Syracuse................................................ 13 Figure 2. Schematic Showing Sensor Locations ................................................................................................ 15 Figure 3. Schematic Showing Solar System on 4th Floor and Roof .................................................................... 15 Figure 4. Photo of Laboratory Test Setup on Fourth Floor of Syracuse COE ....................................................... 16 Figure 5. Schematic Showing Water Heater System and Distribution Piping ....................................................... 20 Figure 6. Profile for a Typical Water Draw Event (from Klein 2011) ................................................................. 22 Figure 7. Water Draw Profile Imposed on Water Heaters – CURRENT DOE Draw Profile .................................. 23 Figure 8. Comparing Measured Conversion Efficiency and Energy Factors – CURRENT Draw Profile ............... 25 Figure 9. Daily Hot Water Use and Supply Temperatures – CURRENT Draw Profile ........................................ 26 Figure 10. Useful Energy vs. Inlet Water Temperature – CURRENT Draw Profile ............................................. 26 Figure 11. Water Draw Profile Imposed on Water Heaters – Normal Use Profile ................................................ 28 Figure 12. Comparing Measured Conversion Efficiency and Expected Energy Factors – Normal Use Profile ....... 30 Figure 13. Daily Hot Water Use and Supply Temperatures – Normal Use Profile ............................................... 31 Figure 14. Water Draw Profile Imposed on Water Heaters – Low Use Profile ..................................................... 32 Figure 15. Comparison of Measured Conversion Efficiency and Expected Energy Factors – Low Use Draw Profile ....................................................................................................................................................... 33 Figure 16. Daily Hot Water Use and Supply Temperatures – Low Use Profile ................................................... 34 Figure 17. Water Draw Profile Imposed on Water Heaters – High Use Profile .................................................... 35 Figure 18. Comparison of Measured Conversion Efficiency and Expected Energy Factors – High Use Profile ...... 36 Figure 19. Daily Hot Water Use and Supply Temperatures – High Use Profile ................................................... 37 Figure 20. Impact of High Use Profile on HPWH Performance ......................................................................... 38 Figure 21. Impact of Draw Profile on Conversion Efficiency – Gas-STD........................................................... 40 Figure 22. Impact of Draw Profile on Conversion Efficiency – HE-PVNT (other) .............................................. 40 Figure 23. Impact of Draw Profile on Conversion Efficiency – SOLAR ............................................................ 41 Figure 24. Impact of Draw Profile on Conversion Efficiency – SOLAR-DRAIN ................................................ 41 Figure 25. Impact of Draw Profile on Conversion Efficiency – TANKLESS ...................................................... 42 Figure 26. Impact of Draw Profile on Conversion Efficiency – HE-Cond .......................................................... 42 Figure 27. Impact of Draw Profile on Conversion Efficiency – HYBRID .......................................................... 43 Figure 28. Impact of Draw Profile on Conversion Efficiency – HPWH.............................................................. 43 Figure 29. Daily Standby Gas Use for DHW1-GAS-STD ................................................................................. 44 Figure 30. Daily Standby Gas Use for DHW2-HE-PVNT ................................................................................. 45 Figure 31. Daily Standby Gas Use for DHW6_HE-Cond .................................................................................. 45 Figure 32. Daily Standby Gas Use for DHW7-HYBRID .................................................................................. 46 Figure 33. Daily Standby Electric Use for DHW8 ............................................................................................ 46 Figure 34. Trends of Electric Consumption versus Natural Gas Input ................................................................ 47 Figure 35. Solar Fraction vs. Solar Flux for Fall 2013 ....................................................................................... 49 Figure 36. Daily Electric Power vs. Solar Flux for Fall 2013 ............................................................................. 50 Figure 37. Direct Comparison of Rheem vs. Wagner Performance for Fall 2013 ................................................. 50 Figure 38. Performance Comparison for a Moderately Sunny Day (October 1, 2013) .......................................... 52 Figure 39. Performance Comparison for a Sunny Day (September 25, 2013) ...................................................... 53 Figure 40. Performance Comparison for a Sunny Day (May 20, 2014) ............................................................... 55 Figure 41. Solar Fraction vs. Solar Flux (before and after Wagner Fix) .............................................................. 56 Figure 42. Daily Electric Power vs. Solar Flux (before and after Wagner Fix) ..................................................... 56 Figure 43. Direct Comparison of Rheem vs. Wagner Performance (before and after Wagner Fix) ......................... 57 Figure 44. Duration of Field Monitoring Period at Each Test Site ...................................................................... 59 Figure 45. Average Monthly Occupancy at Each Test Site ................................................................................ 60 ix Figure 46. Hot Water Use Profile for 2-Person Home during a Cold Month (February 2013 & 2014) .................... 62 Figure 47. Hot Water Use Profile for 2-Person Home during a Swing Month (May 2013 & 2014) ........................ 63 Figure 48. Hot Water Use Profile for 2-Person Home during a Hot Month (August 2013 & 2014) ........................ 63 Figure 49. Hot Water Use Profile for 4-Person Home during a Cold Month (February 2013 & 2014) .................... 64 Figure 50. Hot Water Use Profile for 4-Person Home during a Swing Month (May 2013 & 2014) ........................ 65 Figure 51. Hot Water Use Profile for 4-Person Home during a Hot Month (August 2013 & 2014) ........................ 65 Figure 52. Median Hot Water Use at Each Site with a Range of Plus or Minus One Standard Deviation about the Mean ............................................................................................................................................... 68 Figure 53. Average Daily Hot Water Use for 2-Person and 4-Person Homes ....................................................... 69 Figure 54. Average Daily Hot Water Use for 2-Person Households Compared to the Average .............................. 70 Figure 55. Average Daily Hot Water Use for 2-Person Households .................................................................... 71 Figure 56. Average Daily Hot Water Use for 2-Person Households with Each Site Shown ................................... 71 Figure 57. Average Daily Hot Water Use for 4-Person Households Compared to the Average .............................. 72 Figure 58. Average Daily Hot Water Use for 4-Person Households .................................................................... 73 Figure 59. Average Daily Hot Water Use for 4-Person Household with Each Site Shown .................................... 73 Figure 60. Daily Minimum Entering Water Temperature vs. Daily Flow-Weighted Average EWT ....................... 74 Figure 61. Seasonal Variation in Entering Water Temperature ........................................................................... 75 Figure 62. Daily Hot Water Use vs. Entering Water Temperature ...................................................................... 76 Figure 63. Hot Water Use vs. Number of Draw Events (all days through December 2014) ................................... 78 Figure 64. Hot Water Use vs. Number of Draw Events (Median for Sites through December 2014) ...................... 78 Figure 65. A Sample Hot Water Draw is Identified and Evaluated at Site 1 ......................................................... 80 Figure 66. Conversion Efficiency (or COP) as a Function of Hot Water Use ....................................................... 83 Figure 67. HPWH Input Power as a Function of Hot Water Use ........................................................................ 83 Figure 68. Plot of HPWH Performance for a Day with Element Operation - April 10, 2013 ................................. 85 Figure 69. Plot of HPWH Performance for a Day with Element Operation - April 23, 2013 ................................. 86 Figure 70. Plot of HPWH Performance for a Day with Significant Element Operation - May 21, 2013.................. 87 Figure 71. Plot of HPWH Performance for a Day with Small Amounts of Element Operation - November 12, 2013 ....................................................................................................................................................... 88 Figure 72. Plot of Element Runtime as Function of Hot Water Draw Size ........................................................... 89 Figure 73. Shade Plot Showing Unexplained Periods When Lower Electric Element Runs a Small Amount .......... 90 Figure 74. Last Few Days of HPWH Compressor Operation .............................................................................. 92 Figure 75. Psychrometric Conditions in Basement – with and without HPWH Operation ..................................... 93 Figure 76. Wet Bulb and Dry Bulb in Basement – with and without HPWH Operation ........................................ 93 Figure 77. Basement Temperature and Humidity Shown with DH Operation – Entire Test Period ........................ 94 Figure 78. Basement Temperature and Humidity Shown with DH Operation – June 20, 2013 .............................. 95 Figure 79. Comparison of Daily Average Basement and Outdoor Humidity Ratios .............................................. 96 Figure 80. Effect of Outdoor Humidity Ratio on Dehumidifier Runtime ............................................................. 97 Figure 81. Shade Plot Showing Runtime of Recirculation Pump ........................................................................ 99 Figure 82. Shade Plot Showing When Recirculation Pump Operated ................................................................ 101 Figure 83. Plots of Daily Runtime for Recirculation Pump .............................................................................. 101 Figure 84. Impact of Recirculation Pump Operation on Water Heater Gas Use (when cold water is between 51 and 56°F) ............................................................................................................................................. 102 Figure 85. Variation of Efficiency with Hot Water Use for Period With Recirculation Pump Off ........................ 103 Figure 86. Comparing HW Use and Events for Conventional Tankless Systems ................................................ 104 Figure 87. Conversion Efficiency Versus Hot Water Use ................................................................................ 105 x List of Tables Table 1. Breakdown of Fuels Used for Water Heating in NY Homes .................................................................... 3 Table 2. High Efficiency Non-Condensing Gas Storage Units ............................................................................. 5 Table 3. High Efficiency Condensing Gas Storage Units ..................................................................................... 5 Table 4. Tankless Condensing Water Heaters ..................................................................................................... 6 Table 5. Hybrid (Small Storage) Water Heaters .................................................................................................. 6 Table 6. Heat Pump Water Heaters .................................................................................................................... 7 Table 7. DHW Systems Recommended for Testing .......................................................................................... 10 Table 8. List of Monitored Points and Instrumentation for Laboratory Testing .................................................... 16 Table 9. Summary of Testing at the Field Test Sites.......................................................................................... 18 Table 10. List of Monitored Points and Instrumentation .................................................................................... 21 Table 11. Summary of Water Heater Performance – CURRENT DOE Draw Profile ........................................... 24 Table 12. Summary New Hot Water Use Profiles for Proposed ASHRAE 118.2 Test Procedure.......................... 27 Table 13. Summary of Water Heater Performance – Normal Use Profile ........................................................... 29 Table 14. Summary of Water Heater Performance – Low Use Profile ................................................................ 32 Table 15. Summary of Water Heater Performance – High Use Profile ............................................................... 35 Table 16. Summary of Conversion Efficiencies with Different Draw Patterns .................................................... 39 Table 17. Summary of Water Heater Standby Losses ....................................................................................... 44 Table 18. Electric Use of Gas-Fired Systems .................................................................................................... 47 Table 19. Solar Systems Installed in the Laboratory .......................................................................................... 48 Table 20. Summary Impact of Fixing Wagner System....................................................................................... 57 Table 21. Monthly and Annual Performance Summary for Solar Systems ........................................................... 58 Table 22. Summary of 18 Field Test Sites ........................................................................................................ 61 Table 23. Beginning and Ending Dates for Data Collection at Sites with 15-minute Monitoring ........................... 66 Table 24. Impact of Including Vacation and Missing Days in Hot Water Use Calculation .................................... 67 Table 25. Beginning and End Dates for Event Data at Each Site with 5-second Monitoring.................................. 77 Table 26. Summary of Hot Water Draw Identification at Site 1 .......................................................................... 81 Table 27. Summary of Monthly HPWH Performance ....................................................................................... 84 Table 28. Summary of Days with Unexpected Element Operation...................................................................... 91 Table 29. Multi-linear Regression Results ........................................................................................................ 98 Table 30. Monthly Summary of Dehumidifier and HPWH Operation ................................................................. 98 Table 31. Impact of Recirculation Pump Operation on Standby Losses ............................................................. 103 xi Acronyms and Abbreviations ACEEE AHRI ASHRAE BA Btu COE COP DOE DH DHW EIA EPA EF °F FSEC gal gpm GSHP HE HPWH HW HX kW kWh MBtu NEEA NY/NYS NYSERDA PEX POU RH SEF SF SRCC TC TE UEF UL WH American Council for an Energy Efficient Economy Air Conditioning, Heating and Refrigeration Institute American Society of Heating Refrigerating and Air Conditioning Engineers Building America. Research program at DOE related to residential energy efficiency British Thermal Units Center of Excellence Coefficient of Performance. Same as conversion efficiency US Department of Energy Dehumidifier Domestic Hot Water Energy Information Agency (division of US DOE) Environmental Protection Agency Energy Factor (DOE rating for water heaters) Degrees Fahrenheit Florida Solar Energy Center gallons gallons per minute Ground Source Heat Pump High Efficiency Heat Pump Water Heater Hot Water Heat Exchanger kilowatt kilowatt-hours thousands of Btu Northwest Energy Efficiency Alliance New York / New York State New York State Energy Research and Development Authority Polyethylene Pipe Point of Use Relative Humidity Solar Energy Factor (SRCC rating for solar systems under OG-300) Solar Fraction. Portion of load met with solar energy Solar Rating and Certification Corporation Thermocouple Thermal Efficiency (efficiency rating for commercial water heater products) Uniform Energy Factor (new DOE rating for water heaters) Underwriters Laboratory Water Heater xii 1 Introduction 1.1 Background Water heating is the second largest energy expenditure in existing homes in the Northeast, after space heating (EIA, 2013). Historically, efforts to improve residential efficiency have focused on space conditioning, often neglecting water heating improvements. Several new or recently-refined water heating technologies are now available on the market including: solar water heaters; gas-fired, tankless units; and heat pump water heaters. Tax credits are currently available for some of these systems that boost consumer interest. Current DOE rating procedures to determine the Energy Factor (EF) 1 , or efficiency, of these systems may be a poor indicator of actual energy use, in part because the amount and timing of water use greatly impacts the performance and relative efficiency ranking of these systems. Robust measured data is needed to help consumers, manufacturers, and installers understand the efficiency, costs, and other impacts of both new and conventional domestic hot water systems. 1.2 Goals This research and demonstration project sought to answer the following questions: 1.3 How will the expected changes to the DOE Test Procedure affect published efficiency rating of water heaters? Will it provide a more realistic representation of actual performance in New York Homes? What is the magnitude and timing of water heating loads in NY Homes? How NY homes compare to the national market? What is magnitude of hot water waste in homes? Can distribution system improvements and technologies such recirculation pumps reduce this waste? How do the broad range the broad range of electric, gas-fired and solar water heating options compare in NY homes? What new technologies have the most potential in NY homes? How well do the newest energy-efficient water heating technologies work in actual homes? Approach To answer these questions we engaged in a research effort that included a survey of current technologies, a laboratory testing effort to assess the impact of load profile on water heater efficiency and to compare solar and conventional technologies, and a series of field tests to understand actual water heating loads in NY homes and test the newest technologies under actual conditions. The findings of this research effort as well as more general 1 As defined in 10CFR430 Subpart B, Appendix E and in ASHRAE Standard 118.2 1 guidance about water heating technologies are also being communicated to a broad audience of homeowners, installers and other stakeholders via web site. 1.3.1 Technology Evaluation To determine which water heating technologies were most important to New York State, we teamed with the American Council for an Energy Efficient Economy (ACEEE). ACEEE (2011) developed its “Emerging Hot Water Technologies and Practices for Energy Efficiency as of 2011” report which is available at http://aceee.org/researchreport/a112 . Using this ACEEE evaluation as a starting point, we focused in on the emerging technologies and approaches that were most appropriate for this NY-focused research effort. Section 2 of this report summarizes our evaluation of the technologies and lists the systems identified for laboratory testing. 1.3.2 Laboratory Test A side-by-side test laboratory was constructed at the Syracuse COE to test various standard and high efficiency water heating systems appropriate for northern climates such as New York. The laboratory setup allows the different units to be subjected to the same loads and environmental conditions to directly compare measured performance. This setup is similar to laboratory at the Florida Solar Energy Center (FSEC) that has focused on water heating technologies appropriate for that climate. The test setup also allowed us to study the impact of different water use profiles on efficiency and performance. Section 3.1 provides full details of the laboratory test setup and Section 4 presents and discusses the results. 1.3.3 Field Testing Field testing was conducted at 18 homes to measure the magnitude and timing of hot water use in NY households. Some sites also included enhanced data logging capabilities to capture detailed data about each hot water draw event. Five field test sites also included temperature sensors on the distribution piping to determine the path of each hot water draw to allow us to allocate it to each fixture or end use and ultimately determine the amount of hot water waste. At three sites we also installed high efficiency water heaters to evaluate their performance under actual conditions. Section 3.2 provides full details of the field test approach and Section 5 presents and discusses the field test results. 1.3.4 Communicating Results As a culmination of the project, we developed a web site to communicate key findings from this research as well as to provide general guidance to NY consumers and installers. This website is available at dhw.syracusecoe.org. 2 2 Water Heater Technologies Sixty one percent (61%) of households in the Northeast use natural gas fueled water heaters (EIA, 2013b). A more specific breakdown of water heating fuels for New York State households is given in the table below from the NYSERDA Patterns and Trends – New York State Energy Profiles: 1998-2012 document based on the 2009 RECS data (NYSERDA, 2014). The estimated average size of the heating load associated with each fuel is also given. Electric water heating accounts for 17% of households and is typically used in rural and suburban homes as well as apartments where loads are smaller (36 gallons per day). Natural gas is by far the most popular fuel, accounting for 61% of households. The average load size (56 gallons per day) is more in line with expectations for a single family home. Nearly every home where natural gas is available (and used for space heating) also uses this fuel for water heating. Fuel oil is used in 2.1 million homes for space heating, however only a portion of these homes (1.3 million) also use it for their water heating fuel, Fuel oil is less prevalent for water heating due to the high cost of these appliances. When fuel oil is used, it is most likely with a boiler that has an additional heat exchanger or indirect tank for domestic water heating. The remaining 700,000 homes with oil heat presumably use electricity for water heating. Propane is not widely used (only 3% of households) for water heating, perhaps only in cases when it is also used for cooking fuel in rural applications. Table 1. Breakdown of Fuels Used for Water Heating in NY Homes No of NY Households for Water Heating Avg Use / Cost Implied1 Hot Water Use (gal/day) No of NY Households for Space Heating Electricity 1,200,000 (17%) 2,333 kWh / $398 36 500,000 (7%) Natural Gas 4,400,000 (61%) 200 therms / $299 56 4,100,000 (57%) Fuel Oil 1,300,000 (18%) 120 gal / $305 55 2,100,000 (29%) Propane 200,000 (3%) 175 gal / $545 45 200,000 (7%) TOTAL 7,200,000 7,200,000 Notes: 1 – implied water use determined using fuel energy content, expected efficiency for each fuel and 70°F temp rise. 2.1 Descriptions of Water Heater Technologies Residential water heaters are classified by their input fuel and by the amount of storage capacity. The two primary fuels used for the US market are electric and natural gas. Most natural gas units can also be converted to propane. Oil-fired units are also available but are much less common (in New York State homes with indirect heat exchangers are thought to be more common than direct-fired tanks). The DOE rating procedure for Energy Factor (EF) applies to storage water heaters both gas and electric, as well as tankless units and heat pump water heaters. To be classified as tankless the burner input must be at least 50 MBtu/h and the storage capacity must be less than 2 gallons. EF is a measure of a water heater’s overall daily efficiency 3 based on the amount of hot water produced per unit of fuel consumed. The draw profile for the EF rating consists of six (6) consecutive draws of 10.7 gallons at the beginning of each hour, for a total of 64.3 gallons a day. 2.1.1 Standard Gas Storage Standard gas storage water heaters have an EF range of 0.56 to 0.62, an input rating of 30 to 75 MBtu/h, and a first hour rating between 48 and 114 gallons per hour (AHRI, 2011). A standard gas storage water heater burns fuel in the bottom of the tank and exhaust gases pass through a flue passage in the center of the storage tank. The water in the tank extracts the heat from the combustion gases in the combustion chamber and flue. Standard units have a standing pilot flame and controls that typically do not require electric power to operate. The installed cost of a 40 gallon standard gas storage water heater with an EF below 0.60 is typically in the range of $350 to $600 according to ACEEE (2011). 2.1.2 High Efficiency (HE) Gas Storage: Non-Condensing There are two types of high efficiency (HE) gas storage water heaters: non-condensing and condensing. According to the DOE (2010) a non-condensing HE gas storage unit can save as much as $246 a year with a simple payback in as little as 10 years. As of September 1, 2010 there were 60 models available that qualified for Energy Star certification (DOE, 2010). HE non-condensing gas storage water heaters are similar to standard gas storage units. These HE units meet the Energy Star criteria with an EF rating of 0.67 or greater, which is typically 12-16% more efficient than a standard gas-fired unit. The increased efficiency is typically obtained through: Electronic ignition: eliminating the continuous pilot light, Improved flue baffling: increasing the surface area and turbulence to improve heat exchange, Flue dampers: dampers close while the water heater is in standby mode; restricting off-cycle airflow that loses heat up the flue. Additional insulation: increasing the tank R-value to reduce heat losses to the surrounding space. Heat traps: one-way valves installed on the hot/cold outlet/inlet pipes to prevent convective heat and mass flow. Forced air intake systems and power venting: improves combustion efficiencies and heat exchange. The approximate installed cost of a HE non-condensing gas storage water heater is $1,300 (ACEEE, 2011). The four major manufacturers of HE non-condensing gas storage water heaters listed in the table below. 4 Table 2. High Efficiency Non-Condensing Gas Storage Units Manufacturer / Brand Storage Size (gal) Rating A.O. Smith Water Products 40, 50, and 75 EF = 0.67 to 0.70 American Water Heater Company 40 or 50 EF = 0.67 to 0.70 Bradford White Corporation 40 to 65 EF = 0.67 to 0.70 Rheem Manufacturing 29 to 50 EF = 0.67 to 0.70 2.1.3 High Efficiency (HE) Gas Storage: Condensing Condensing gas storage water heaters incorporate technology that captures latent heat of water vapor released during combustion. A coil-like flue that spirals up through the tank increases surface area for better heat exchange. According to ACEEE (2011) this helps to improve the efficiency a further 10% over the non-condensing units. A list of Energy Star qualified condensing gas storage units (with EF ratings) is not yet available. These units are generally considered by DOE to be commercial water heaters; however, smaller “commercial” condensing water heaters are available for residential applications. The approximate installed cost of a condensing gas storage water heater is $2,500 (ACEEE, 2011). There are currently four companies that offer condensing gas storage water heaters that are listed in the table below. Table 3. High Efficiency Condensing Gas Storage Units Manufacturer / Brand Storage Size Rating A.O. Smith (Vertex™) 50 gallons 90-96% thermal efficiency American Water Heater (Polaris®) 34 to 50 gallons 95+% thermal efficiency Bradford White (EFR) 60 gallons 95% thermal efficiency Heat Transfer Products (Phoenix®) 55 gallons 93.7-95.1% thermal efficiency Note: No EF rating is available for these units. 2.1.4 Tankless Gas Water Heater Tankless water heaters are currently installed in 1.4 million homes in the Northeast region, with 400,000 estimated to be in New York (EIA, 2013c). According to Energy Star yearly savings of up to $201 are possible with a simple payback of 7 to 19 years (DOE, 2010). Tankless gas water heaters have a large burner (and no storage) so that water is heated on demand. To be considered tankless by the Department of Energy the unit must have a storage capacity no greater than 2 gallons. Condensing Tankless Water Heater. Condensing tankless water heaters add additional heat exchanger surface to extract more heat from the combustion gases. These condensing units have EF ratings to 0.91, compared to 0.82 for non-condensing. The condensing tankless water heaters are approximately 37% more efficient than standard gas storage units. The approximate installed cost of a condensing tankless unit is $2,900 plus $85 for recommended 5 annual tankless maintenance (ACEEE, 2011). Energy Star and AHRI directory list five manufacturers of condensing gas tankless water heaters. Table 4. Tankless Condensing Water Heaters Manufacturer / Brand Input Rating A.O. Smith Water Products 180 MBtuh to 199 MBtuh EF = 0.91 Bosch Water Heating 175 MBtuh to 225 MBtuh EF = 0.92 to 0.98 Navien America Inc. 150 MBtuh to 199 MBtuh EF = 0.95 to 0.97 Noritz America Corp. 157 MBtuh to 199 MBtuh EF = 0.91 to 0.94 Rheem Manufacturing 157 MBtuh to 199 MBtuh EF = 0.92 to 0.94 2.1.5 Hybrid Gas Hybrid water heaters combine the large burner of a tankless heater with a small storage tank to overcome some of the performance short comings of tankless units. The large burner supplies a continuous supply of hot water reducing the standby losses of a storage water heater. The small storage helps to avoid the “cold water sandwich” problem commonly reported in tankless units and helps to eliminate the delay in hot water delivery as the system first activates and warms (ACEEE, 2011). Condensing hybrid units have higher thermal efficiency than noncondensing hybrid heaters. The estimated installed cost of a non-condensing hybrid water heater is $1,726 with an additional $85 a year for recommended tankless maintenance (ACEEE, 2011). The installed cost of a condensing hybrid unit is $2,300 (ACEEE, 2011). The current manufacturers are listed below. Table 5. Hybrid (Small Storage) Water Heaters Manufacturer / Brand Model Input EF or Efficiency A.O. Smith Water Products NEXT Hybrid® 100 MBtuh 90% Grand Hall USA Eternal Hybrid™ 100 MBtuh to 195 MBtuh EF = 0.94 to 0.96 2.1.6 Standard Electric Storage About 24.5% of households in the Northeast and 16.7% in New York State use electric storage tanks to meet their water heating needs (EIA, 2013c). Standard electric storage water heaters have an EF range of 0.81 to 0.95, power input of 1.5 kW to 5.5 kW, and a first hour rating of 17 to 120 gallons per hour (AHRI, 2011). Although electric storage water heaters are more efficient per unit of energy, the higher cost of electricity makes gas storage water heaters cheaper to own over the lifetime of the unit (assuming gas is available). An electric storage heater has a resistance element that directly heats the water in the tank. Electric water heaters are often used in apartments or other confined spaces where flue gas venting is difficult or impossible. 6 2.1.7 Heat Pump Water Heaters Heat pump water heaters (HPWH) “concentrate” heat from the ambient air to the water in the storage tank using a vapor compression cycle. The heat pump extracts heat from the surrounding air, providing sensible cooling and dehumidification. The AHRI directory shows that HPWHs have EFs in the range of 2.00 to 2.51, inputs of 2.5 to 5.0 kW, and a first hour ratings of 56 to 84 gallons per hour. According to the DOE (2010) a HPWH can save homeowners around $234 a year in some climates compared to standard electric storage units, with a simple payback of 3 years. HPWHs are available as integrated units that include storage tank as well as add-on units that can be added to an existing tank. To have an acceptable first hour rating a resistance heating element is required. There are currently eight manufacturers of HPWHs. Table 6. Heat Pump Water Heaters Manufacturer / Brand Model Input Rating A.O. Smith Water Products Voltex® 4.5 kWh EF = 2.33 Airgenerate LLC AirTap™ 4.0 kWh to 5.0 kWh EF = 1.92 to 2.21 Bosch Water Heating HP 200-1 4.5 kWh EF = 2.20 General Electric GeoSpring™ 4.5 kWh EF = 2.35 to 2.40 Heat Transfer Products HTP Hybrid 4.0 kWh EF = 2.20 Rheem Manufacturing EcoSense 2.5 kWh to 4.0 kWh EF = 2.00 Stiebel Eltron Inc. Accelera® 300 2.2 kWh EF = 2.51 USI Green Energy Green Star 5 kWh EF = 2.39 to 2.40 An Energy Star HPWH must have an EF of at least 2.0, a first hour rating of at least 50 gallons per hour, a warranty of at least 6 years, and meet the required UL safety standards (Energy Star, 2011). Energy Star rates both integrated or drop-in HPWH configurations. The expected installed price of an Energy Star HPWH is $1,600 with over $300 in base savings over a standard electric storage water heater2. There is also an additional annual savings of $20 (annual cost of operating a standalone dehumidifier) due to the dehumidification capacities of the HPWH (ACEEE, 2011). Using a HPWH in a Northern climate often requires special considerations. Therefore, the Northwest Energy Efficiency Alliance (NEEA, 2011) has proposed a Northern HPWH specification that includes: 2 HPWH is Energy Star qualified (EF ≥ 2) First Hour Rating comparable to equivalent resistance water heater (60 gallons per hour) Additional safety and service parameters for condensate management, air filters, diagnostics, and freeze protection. Additional exhaust ducting and noise control features for units to be installed in living spaces. Assumed $0.1158/kWh, EF=0.90 and 4,878 kWh/yr for standard electric, EF=2.00 and 2,195 kWh/yr for HPWH 7 ACEEE estimates that the installed cost of this Northern HPWH is $1,700 (ACEEE, 2011). In our opinion some of these features (such as the existing ducting) may not be appropriate in a New York State application where units are likely to be mounted in a basement. Add-on HPWH. An add-on HPWH is a standalone air source heat pump that is separately connected to a third party tank via a pumping circuit. Cold water enters the heat pump where it is heated and pumped back to the tank. Addon heat pumps are not federally regulated. The Department of Energy does not consider them to be complete water heaters, because they rely on third party tanks with unknown thermal properties. Therefore, a recognized rating method does not yet exist, and have been excluded from the Energy Star Water Heater program. These units have an estimated installed price of $800 with an additional annual savings of $20 for no longer needing a standalone dehumidifier (ACEEE, 2011). 2.1.8 Electric Tankless Water Heater Electric tankless water heaters are smaller units that can be located at or near the end use location or point of use (POU), such as the sink or shower/tub. Electric POU water heaters can also be used to boost the hot water temperatures from a central storage system or solar storage. The increased efficiencies attributed to these units are primarily from the decrease in distribution losses of longer runs from a centralized heating system. Distribution losses are primarily a concern in commercial application but can also be an issue in larger residential applications. Standby losses from the tank are also eliminated. Eemax is the only manufacturer listed in the AHRI directory and a web search found Bosch Water Heating (Powerstar and Ariston), and Stiebel Eltron Inc. Rheem produces commercial models possibly suitable for residential applications. ACEEE estimated the installed cost of an electric tankless unit in a remote, but extensively used bathroom to be $1,700 (ACEEE, 2011). 2.2 Other DHW Approaches 2.2.1 Indirect Tank Systems In New York State 3.2 million households use natural gas or fuel oil boilers for space heating (EIA, 2013d). The boiler can also provide water heating via an internal heat exchanger or an indirect tank. The internal heat exchanger approach is a tankless approach where the boiler must fire on demand to provide tankless water heating. Indirect tanks add another circuit or zone to boiler to heat water in an insulated tank. These tanks provide water heating at the efficiency of the space heating boiler (excluding piping losses) and typically have internal controls to turn off the boiler-side pumps or valves. 2.2.2 Ground Source Heat Pump Systems Ground source heat pumps (GSHPs), also known as Geothermal or GeoExchange systems, provide space conditioning (heating and cooling). Many of these systems can also provide domestic hot water. There are two 8 common configurations for GSHP-based water heating systems: one is a desuperheater heat exchanger that is integrated into the GSHP unit, or the second is a triple-function GSHP unit that uses its full heating capacity to meet DHW loads. The desuperheater uses the hot gases from the heat pump’s compressor to assist in heating the water. During the cooling season the desuperheater provides “free” hot water, but during heating season water heating is provided at the space heating COP. A shortcoming of the desuperheater concept is that water heating is only provided as a consequence of space conditioning operation. The triple-function GSHP can use its full heating capacity to provide water heating. The unit includes different refrigerant valving and controls to enable compressor operation based on space heating, water heating, or cooling loads (thus the triple function). The estimated incremental cost of a triple-function heat pump is $900 more than the desuperheater unit, with little to no change to the installation costs; however other changes in the GSHP may increase the cost further (ACEEE, 2011). 2.2.3 Solar Water Heaters The solar heater market was the only area that saw a decline in Energy Star qualified shipments from 2006 to 2009. This is thought to be the result of overestimation of qualified products and the lack of engagement from some solar manufacturers becoming active within Energy Star. Solar with electric backup has an annual savings around $259 and an approximate payback period of 10 years (DOE, 2010). Solar water heaters consist of three components; collector, circulation, and storage. Collector Type There are three types of collectors used in solar water heating systems. 1. 2. 3. Batch or Integral Collectors. A batch collector, also known as an integrated collector-storage system, typically stores water in a tank attached to the collector. Heat transfer between the tank and collector is normally achieved by passive heat transfer via a thermosyphon. This system is normally unsuitable for northern climates where temperatures are frequently below freezing. Flat Plate Collectors. Flat plate collectors consist of tubes attached to absorber plates which are all contained within an insulated box. Evacuated Tube Collectors. Evacuated tube collectors are glass tubes containing water or heat transfer liquid inside a larger glass tube. The space between the tubes is at a vacuum and helps to improve efficiency. Evacuated tube collectors have been shown to work at -40°F and individual tubes can be replaced. Circulation Approach Solar systems can use two different water circulation approaches: 1. 2. Direct / Drain-back. Direct circulation approaches pump potable water directly through the collector where it is heated and sent back to the tank. Usually the water “drains-back” to the tank when solar heat is not available and when the risk of freezing is high. This approach is preferable for warmer climates where it rarely freezes, since heat transfer is better without an intermediate fluid. Closed Loop or In-direct. In a closed-loop system a non-freezing liquid flows through the collector and returns to a heat exchanger in or near the storage tank. This approach is common for cold climates where the risk of freezing is high. 9 A new in-direct, drain-back system is now available for northern climates from Wagner & Co (Secusol). The Secusol system has a drain-back glycol loop in an in-direct heat exchanger inside the water heating tank. The internal glycol heat exchanger has large enough volume to hold all the glycol needed to operate the system – and store it when the system is off. This system provides the freeze protection of a glycol system but eliminates the extra components and installation labor needed for closed loop, pressurized glycol system. It is also resistant to overheating and stagnation issues that can degrade the glycol fluid on a sealed system. 2.3 Systems Selected for Testing Based on the technology review above we recommended the systems listed in Table 7 for laboratory testing in this project. The systems were chosen based on their applicability and potential in New York State homes. Table 7 lists the characteristics for the recommended systems. Table 7. DHW Systems Recommended for Testing Location 1 Technology Classification Manufacturer and Model GAS-STD A.O. Smith Standard Gas Storage GCVX-50-100 GAS-HE-PVNT 2 Non-condensing Power Vent Gas Storage A.O. Smith GPVR-40 SOLAR Rheem 3 Flat Plate, Glycol Solar Hot Water SOLPAK 3.2 RS12064BP SOLAR-DRAIN 4a Drain-Back Solar Hot Water Wagner & Co SECUSOL 350-2 144014 28 ELECT-STD A.O. Smith Standard Electric Storage ECT-52 4b 5 TANKLESS-COD Rheem Condensing Gas Tankless RTGH-95DVLN GAS-HE-COND 6 7 8 HE Condensing Gas Storage A.O. Smith Vertex™ GDHE-50 HYBRID A.O. Smith Hybrid HE Small Storage NEXT HYB-90N HPWH GE Heat Pump Water Heater GEH50DEEDSC EF or SEF Input and Size 0.58 65 MBtu/h 50 gal 0.67 40 MBtu/h 40 gal 3.2 3.1 4.5 kW 120 gal 4.5 kW 92 gal .91 4.5 kW 52 gal 0.94 199 MBtu/h Not rated by EF (96% efficiency) 100 MBtu/h 50 gal not rated by EF (90% efficiency) 100 MBtu/h 2.35 0.55-4.5 kW 50 gal Notes: Location corresponds to the position in the laboratory. Location 1 and 2 on 1 st floor. Locations 3 to 8 on 4th floor from west to east. SOLAR-DRAIN (4a) and ELECT-STD (4b) are combined into one system. 10 We focused on gas and electric appliances even though oil-fired water systems are relatively prevalent in New York State. We believe that oil-fired systems are typically not stand-alone, direct-fired appliances but instead are more commonly part of the boiler system used for space heating. The majority of installed tankless units are non-condensing units. However, we recommend that a modern condensing unit be laboratory tested to understand the characteristics and performance of these more advanced units. While Heat Pump Water Heaters (HPWHs) are more widely used in southern climates they also have potential as an efficiency improvement in NYS homes with electric water heaters. Therefore this unit was included in the test program. Solar Hot Water Systems are not being directly funded by the NYSERDA portion of the project but are being separately funded by a separate DOE project at Syracuse University (DE-EE0002121). We selected two types of systems that are appropriate for cold climates: A conventional glycol-filled system with an indirect heat exchanger in the storage tank (Rheem) An innovative glycol-fired drain-back system that is simpler to install and has better performance (Wagner). 11 3 Test Approach and Monitoring Details The approach for this project was to test water heaters in the laboratory as well as in homes under actual operating conditions (i.e., field testing). The side-by-side laboratory testing is useful for making careful comparisons between different systems operating under the same operating conditions. The field testing is useful for understanding and characterizing the loads imposed on these appliances. 3.1 Laboratory Test Approach and Setup The laboratory test setup was designed provide head-to-head comparisons of different water heating (WH) systems under the same load conditions (i.e., hot water use patterns). The laboratory was built to include different test stations for eight different water heaters. The side-by-side setup allows weather-dependent systems – such as solar water heating systems and heat pump water heaters – to be directly compared to other systems on a daily basis under different load and weather conditions. This test setup is similar to a laboratory at Florida Solar Energy Center in Cocoa, Florida (http://infomonitors.com/hws/ and http://blog.floridaenergycenter.org/echronicle/tag/hot-watersystems-lab/). The FSEC laboratory is directly comparing WH system performance for southern climates. Our goal was to provide a similar side-by-side assessment of actual WH system performance under conditions that are representative of northeastern residential applications. The laboratory setup allows for any hot water use pattern to be simulated by each of the eight test stations. A datalogger/control system was programmed to initiate a water draw of any duration starting at any time (to the nearest minute) in a 24-hour period. The system allows for up to 100 draw events per day. The draw rate can be specified at 3 possible flow rates (e.g. 1, 2, or 3 gpm). This setup allows for: a standard simulated use test according to the DOE Test Procedure to determine Energy Factor (EF), i.e., six draws, one hour apart, each draw at 3 gpm for 214 seconds, or other arbitrary draw patterns to represent more typical use. The primary operating mode for laboratory is to allow entering cold water temperatures to float with seasonal conditions – in order to simulate actual conditions for a home in Syracuse. The plot in Figure 1 shows the typical annual profile of cold water temperatures from a Syracuse home; conditions at laboratory facility were found be similar. However, in order to complete a standardized test according to the DOE Test Procedure, we also added a mixing valve and buffering tank at the cold water inlet to the test setup. This allowed for some heated water from the tank to be blended in with the cold water stream to achieve the 58°F required by the DOE Test Procedure. This approach of blending in hot water allowed us to run a standardized test for about half the year (i.e., in the winter when the city water temperature is below 58°F). 12 Figure 1. Annual Trend of Cold Water Inlet Temperature in the City of Syracuse Cold Water Inlet - Syracuse Home 80 Temperature (F) 70 60 58°F required for DOE test procedure 50 40 30 January March April May June July August October 2010 2011 Instrumentation was installed to measure: The energy content of the delivered hot water from the system, The fuel and electric input into the water heating system. From these measurements the overall daily efficiency can be determined for various seasons. We also track various environmental and operating conditions such as: temperature and relative humidity in the space (or entering the heat pump water heater), and solar flux striking the collector surface, flue gas temperature for combustion appliances, temperature stratification in one of the hot water tanks, hot water temperature leaving each system. The laboratory setup has eight (8) separate stations to test nine (9) DHW systems. In Section 2 (Table 7) we identified the hot water heaters that were included in this test. 13 3.1.1 Laboratory Setup The laboratory was constructed at the Syracuse Center of Excellence (COE) in two locations. Two (2) gas-fired units are located in stations 1 and 2 on the first floor. The 1st floor location allows for a conventional natural-draft, gas-fired water heater, by using the existing flue in the space. The other six stations are located on the fourth floor. Three of the test stations allow for power-vented gas-fired units (stations 5, 6 and 7) and three other stations (stations 3, 4, and 8) can support electric units, including the conventional electric tank, two solar systems, and a heat pump water heater. The solar collectors are located on the roof of the building, which is above the 5th floor (see Figure 3). The tank-to-collector height is about 32 ft. 3.1.2 Instrumentation and Measurements Figure 2 schematically shows the location of the instrumentation for each water heating system. Each data point has a suffix of 1 through 8 corresponding to the station or system number. The environmental conditions are designated as “A” for the first floor and a “B” for the fourth floor. All the monitored points are listed in Table 8. For each system, the cold inlet temperature (TC), hot outlet temperature (TH), and water flow (FW) are measured to determine delivered energy (QH) from the water heater. The temperature sensors are low-mass thermocouples inserted in the piping in order to quickly respond to changes in temperature with transient flows. The total unit power use (WE) was measured for each electric unit. Units with a backup resistance heating element such as the solar systems and heat pump water heater had an additional power measurement (WRE). Gas use (FG) was measured for the gas units with a temperature-compensated gas meter (0.25 CF per pulse). The solar systems include measurements for exchanger inlet and outlet temperature (TEI, TEO) as well as the solar flux (IW5) striking the plane of the collector panel on the roof (see Figure 3). On one of the storage tanks on the fourth floor, an extended TC probe with 6 sensing points that can be inserted in the tank to measure the degree of stratification from top to bottom (TTa-TTf). The space conditions are separately measured at the first and fourth floor locations (TAIA, TAIB). On the fourth floor, relative humidity (RHIB) is measured for the heat pump water heater. The flue gas temperature (TFG) is measured for all the gas-fired units. Each test station is built around a metal and plywood frame for mounting the necessary utilities (cold water, hot water, gas, and electric) and as well as control wiring and instrumentation. A photo of the laboratory test setup is shown in Figure 4. 14 Figure 2. Schematic Showing Sensor Locations Hot out Cold in TC TH Flow Limiters (1 & 2 gpm) TFG Solar Systems Only FW Solenoid Valves TEI, TEO Space Conditions WRE TAIA TAIB RHIB TTa - TTf WE Electric Natural gas FG DHW Tank or Unit Figure 3. Schematic Showing Solar System on 4th Floor and Roof IW3 Solar Collectors Roof 5th Floor Solar Tank th 4 Floor 15 Table 8. List of Monitored Points and Instrumentation for Laboratory Testing System: Eng Measurement Units Water Inlet Temperature °F Water Outlet Temperature °F Water Storage Temperature (6 pts) °F Water Use gal Flue Gas/Vent Temperature °F Electric Energy Use kWh Gas Use CF Discharge Air Temperature °F Exchanger Inlet Temperature °F Exchanger Outlet Temperature °F Resistance Element Energy Use kWh Solar Flux W/m2 Space Relative Humidity % RH Space Temperature °F Outdoor Temperature °F Instrumentation Station No: Watlow type-T 1/16" probe Watlow type-T 1/16" probe Watlow multi-pt TC Omega FTB4605 1/2" Watlow type-T 1/16" probe Wattnode MB WNB-3D-240-P Domestic Meter (0.25 CF/p) Watlow type-T 1/16" probe Watlow type-T 1/16" probe Watlow type-T 1/16" probe Wattnode MB WNB-3D-240-P Licor LI200x Vaisala HMD 60U Watlow type-T 1/16" probe CoE Weather Station GAS-HEPVNT GAS-STD SOLARDRAIN SOLAR / ELECT-STD TNKLSCOND GAS-HECOND HYBRID 1 2 3 4 5 6 7 8 TC1 TH1 TC2 TH2 TC3 TH3 TC5 TH5 TC6 TH6 TC7 TH7 TC8 TH8 FW1 TFG1 FW2 TFG2 WE2 FG2 FW3 TC4 TH4 TTa to TTf FW4 WE4 FW6 TFG6 WE6 FG6 FW7 TFG7 WE7 FG7 FW8 WE3 FW5 TFG5 WE5 FG5 TEI3 TEO3 WRE3 IW3 TEI4 TEO4 WRE4 FG1 WE8 TDIS8 WRE8 RHIB TAIB TAIA TAO Figure 4. Photo of Laboratory Test Setup on Fourth Floor of Syracuse COE 3.1.3 Data Analysis As described above, the thermal energy delivered to the water heater is calculated in the datalogger at the scan interval using the formula below: 𝑄𝐻 = 𝑘 ∙ 𝐹𝑊(𝑇𝐻 − 𝑇𝐶) where HPWH k - the product of density and specific heat (8.34 lb/gal∙Btu/(lb∙℉)) 16 Water consumption (FW) is measured in gallons by the datalogger. The calculation for QH (in Btu) is completed in the datalogger for each scan interval (3 seconds). Then the calculated values are summed over each logging interval to find the total Btu (e.g., per 15 minute interval). The low mass thermocouples are directly inserted in water to ensure a rapid response to temperature changes that occur during a flow event. The electric or fuel input is used to determine the total efficiency of the system. This calculation only has meaning over longer intervals – such as a day – since the energy associated with a water draw may not correspond in time to the subsequent fuel or power consumption as the water heater recovers. Fuel consumption is based on the higher heating value of the fuel. Therefore the conversion efficiency for a period is defined as: 𝐶𝑜𝑛𝑣𝑒𝑟𝑠𝑖𝑜𝑛 𝐸𝑓𝑓𝑖𝑐𝑖𝑒𝑛𝑐𝑦 = 𝐻𝐻𝑉 𝑄𝐻 𝑔𝑎𝑠 ∙𝐹𝐺+3412∙𝑊𝐸 where: QH - Heat Delivery (Btu) WE - Total Power Use (kWh) FG - Natural Gas Use (CF) HHV - Higher heating value for natural gas (1030 Btu per CF ) On units with multiple types of electric use (e.g., the heat pump water heater uses electricity for both the compressor and the resistance element) the efficiency can be calculated separately for each case. Similarly energy use and hours in each mode can be tracked. 3.2 Field Testing Approach One goal of the field testing is to measure the magnitude and timing of hot water loads in several New York State homes. At all the test sites the hot water use was measured on different time scales to understand the pattern of hot water use. Another goal of field test project is to measure the detailed performance of new DHW systems installed in an actual residence (i.e., at Sites 1, 2 and 3). Sensors were installed to quantify the energy input to these systems as well as the thermal energy outputs. Intermediate temperatures and component statuses were also tracked to understand system operation and diagnose any observed anomalies or shortfalls in performance. In addition, sensors were added at Sites 1 through 5 to determine the specific fixture or appliance associated with each particular hot water draw. Temperature sensors were installed to track the path (or paths) of each water draw. This testing provided crucial data to help understand the detailed makeup of water draws in a typical Northeastern home. This data helped estimate the magnitude of the distribution losses associated with a piping system by measuring the time delays for given water draw to reach a fixture. This effort to measure, analyze and understand distribution losses was jointly funded by NYSERDA and the US DOE’s Building America (BA) program (via the 17 ARIES Collaborative). The test efforts to measure distribution losses considered typical homes as well as homes where new systems and/or distribution and piping improvements were implemented. A total of 18 sites were included in this field test. Table 9 summarizes the type of retrofit and testing that was completed at each field site. Table 9. Summary of Testing at the Field Test Sites No NYSERDA Site ID Building America (BA) Designation Site/System Changes Monitoring Approach 1 Detailed #1 BA Group #3 “full retrofit” A new DHW system installed and distribution system improvements implemented. Monitoring both before and after changes/retrofit 2 Detailed #2 BA Group #3 “full retrofit” A new DHW system installed and distribution system improvements implemented. Monitoring both before and after changes/retrofit 3 Simple #1 BA Group #2 “New Tankless” A new tankless unit installed (no distribution changes) Monitoring both before and after changes/retrofit 4 Simple #2 BA Group #1 “existing” No changes Monitor existing system 5 Simple #3 BA Group #1 “existing” No changes Monitor existing system 6 to 18 Simple #4 to #16 - No changes Monitor existing system 3.2.1 Instrumentation and Measurements at Field Test Sites Water-Use Only Sites At the 13 sites (Sites 6 through 18) without additional BA monitoring, a flow meter was installed to measure the hot water flow rate. The hot water flow rate was measured with a high resolution Omega flow meter installed on the cold water inlet of the DHW system. The data were collected at 15-minute intervals using a Campbell Scientific datalogger. At 8 of these 13 sites, we used a Campbell Scientific CR200x datalogger that additionally collected flow data at 5-second intervals around each draw event. Short time step data collection was initiated once any flow occurs (i.e., when one or more pulses are detected) and then logging continued for at least 30-seconds after water flow subsides. At the other 5 sites, a Campbell Scientific CR10 or CR10X logger (with less memory capacity) was used to collect only 15-minute data. The data was manually collected (by visiting each site) every 2 to 3 months. For the dataloggers collecting short time step data, the datalogger memory was partitioned so that a continuous, uninterrupted stream of 15-minute data was always collected. The data were loaded into a database at CDH, checked for the validity, and summarized/analyzed in PDF reports. The reports for each site were updated and posted on the project website. At least 9 months of data was collected from each site. 18 Detailed / BA Sites At the five BA sites in Table 9 above (including the two sites designated as “NYSERDA Detailed Field” sites), a monitoring system was installed to measure the detailed performance of the water heating system as well as the hot water distribution system. Instrumentation was installed to measure: The energy content of the delivered hot water from the unit, The fuel and/or electric input into the water heating unit (only Sites 1 through 3), The environmental conditions (air temperature) near the water heater temperature and piping; the relative humidity was measured if the system is a heat pump water heater. Flue gas temperature for combustion appliances, The runtime or status of each component (e.g., resistance elements, fans, pumps, etc.) Key temperatures in the trunks and branches leading to each fixture A Campbell Scientific CR1000 datalogger was used to collect averaged or totalized data at 15-minute intervals for several months. The datalogger was programmed to sample each sensor at a scan rate of 5 seconds. Then several key data points were recorded at 5-second intervals when a draw is occurring (i.e., when one or more pulses were detected). Short time step data collection continued for 30 seconds after the water flow subsided. The collected data points required for the detailed sites are listed in Table 10. Figure 5 schematically shows the location of the instrumentation for each water heating system. The specific monitoring points installed at each site are given in Appendix A. For each system, the cold inlet temperature (TC), hot outlet temperature (TH), and water flow (FW) are measured to determine delivered energy (QH) from the water heater. The type-T thermocouples were attached to the outside of the copper pipe using thermally conductive paste and were well insulated to shield it from ambient conditions surrounding the pipe. The total unit power use (WE) was measured for each electric unit. Units with a resistance heating element such as electric tanks or a heat pump water heater had a status measurement to record the runtime of that component (SE1, SE2). Gas use (FG) was measured for the gas units with a temperature-compensated gas meter (0.25 CF per pulse). The flue gas temperature (TFG) was measured for all the gas-fired units. Ambient air temperatures around the water heater and in unconditioned areas with significant hot water piping runs were also measured. (TA1, TA2, etc.). Relative humidity (RHI) was measured at sites with a heat pump water heater. We also installed low mass thermocouples on the outside of the trunk, branch and fixture pipes (i.e., “twigs”) to determine the path of hot water flow during each draw. Where practical, we installed a thermocouple on the dedicated line or twig to each point of hot water use or fixture (TF1, TF2, etc.). Temperature sensors were installed on trunk or branch lines to major areas (kitchen, bath, etc.) to help determine the path of hot water flow (TT1, TT2, etc.). We used a wireless Campbell Scientific CR206X datalogger to take the temperature measurements in areas 19 that could not be reached with hard-wired sensors. Due to their higher cost, we purchased five of these wireless loggers to extend monitoring at the five detailed sites. We used two of these wireless loggers at Site 1, two at Site 4, and one at Site 5. The location of each fixture was surveyed to establish the effective pipe lengths and volume of the distribution system (see Appendix A). Figure 5. Schematic Showing Water Heater System and Distribution Piping sink dishwasher TF2 TF1 sink Kitchen TF3 bath TF4 Bath 1 TF5 TA2 TT3 TT2 TF6 TT4 TT1 TF7 TEX exhaust gas TF8 Utility sink Washing Machine TH TA1 SE1 SE2 DHW Unit WE electric TC FW sink Trunk FG natural gas 20 bath Bath 2 Table 10. List of Monitored Points and Instrumentation Detailed BA3 Detailed BA3 Simple BA2 Simple BA1 Simple BA1 Simple 1 2 3 4 5 6 to 18 Watlow type-T TC 1/16" probe TC1 TC2 TC3 TC4 TC5 °F Watlow type-T TC 1/16" probe TH1 TH2 TH3 TH4 TH5 gal Omega FTB4605 1/2" FW1 FW2 FW3 FW4 FW5 °F Watlow type-T TC Air TFG1 TFG2 TFG3 TFG4 TFG5 5-sec Data ? Eng Units Inlet Water Temperature Y °F Hot Water Oulet Temperature Y Hot Water Use Y Measurement Flue Gas/Vent Temperature Electric Energy Use Instrumentation kWh Wattnode MB WNB-3Y-208-P WE for applicable units Unit Gas Use CF Domestic Meter Pulser (0.25CF/p) Relative Humidity % Vaisala HMD60 Space Temperature near Unit °F Watlow type-T TC 1/16" probe TA1-1 TA1-2 TA1-3 TA1-4 TA1-5 Space Temperature near piping °F Watlow type-T TC 1/16" probe TA2-1 TA2-2 TA2-3 TA2-4 TA2-5 FG1 FG2 FG2 RH (only for HPWH site) Trunk Temperature - Location 1 Y °F Watlow type-T TC 1/16" probe TT1-1 TT1-2 TT1-3 TT1-4 TT1-5 Trunk Temperature - Location "n" Y °F Watlow type-T TC 1/16" probe TTn-1 TTn-2 TTn-3 TTn-4 TTn-5 "Twig" Temperature - Fixture 1 Y °F Watlow type-T TC 1/16" probe TF1-1 TF1-2 TF1-3 TF1-4 TF1-5 "Twig" Temperature - Fixture "n" Y °F Watlow type-T TC 1/16" probe TFn-1 TFn-2 TFn-3 TFn-4 TFn-5 °F CoE Weather Station Outdoor Temperature FW6 - FW18 TAO The first five test sites used CR1000 dataloggers that were connected to the wireless network in each home via a wireless bridge. The dataloggers were programmed to send data to the CDH servers each night. The data was verified and then sent to a custom website that summarizes the performance of each system. 3.2.2 Data Analysis Procedures The thermal energy delivered by the water heater was calculated in the datalogger at the scan interval using the same formulas described in the laboratory section above. The total conversion efficiency is also defined as the thermal delivered energy divided by the fuel and power inputs, all expressed in the same engineering units. Conversion efficiency is most meaningful on a daily, monthly or annual time scale. For each hot water draw event we detected the associated end use fixture using the temperature data. We developed automated analysis procedures similar to Barley et al (2010) in order to detect the fate of each draw by detecting a change in temperature at each fixture and trunk line. We developed a logic table for each site to assign draws based on the trunk and branch sensor(s) associated with each fixture. The time delay in hot water reaching each fixture was used to estimate the volume of water that is “wasted” during each draw event. Hot water waste is defined as 21 water leaving the fixture at less than 100°F or 105°F as suggested by Klein and Barley3. When water draws simultaneously occurred from multiple fixtures, we had hoped to develop procedures to apportion each draw volume to the active end uses. However, this provided to be impractical. Figure 6 shows a typical draw profile starting with cold pipes. Figure 6. Profile for a Typical Water Draw Event (from Klein 2011) In most cases it was possible to install a temperature sensor near the end use fixture; however, was still be possible to infer the water waste associated with each draw by installing a temperature sensor at an intermediate location (e.g., where a hot water line leaves the basement, heading towards a fixture). The Building America Report (Henderson and Wade 2014) fully presents the results using these analysis techniques. Section 5.5 in this report provides a summary of those results. 3 Hot water is only deemed “useful” once it reaches this temperature threshold 22 4 Laboratory Test Results 4.1 Comparing Measured Laboratory Performance to Energy Factor The first testing conducted in the laboratory was to duplicate the current DOE Test Procedure, as defined in 10CFR430 Subpart B, Appendix E and in ASHRAE Standard 118.2. This procedure consists of six draws one hour apart. Each draw is 10.7 gallons at 3 gpm for a daily total of 64.2 gallons. After the initial shakedown and verification in March and early April 2013, the DHW systems started to operate on April 10, 2013 with this standard draw profile used in the DOE Test Procedure. Figure 7 and Figure 9 shows that there were still variations in the water draws and total HW use per day that were caused by problems with the flow limiters. Table 11 shows that the average water use for each system ranged from 60 to 75 gallons per day. Figure 7. Water Draw Profile Imposed on Water Heaters – CURRENT DOE Draw Profile 04/11/13 14 Water Use: 72.4 gal/day 12 HW Use (gal) 10 8 6 4 2 0 22: 0: 10 11 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 12 Figure 8 and Table 11 summarize the conversion efficiencies measured for each system and compare them to the rated EF. The standard efficiency gas tank (Gas-STD) and the high-efficiency power vented unit (HE-PVNT) are both in very good agreement with the measured EF. The conversion efficiency for the tankless water heater (TANKLESS) is also within 5% of the rated EF. The measured efficiency for the heat pump water heater (HPWH) actually exceeds the rated value by 5% because the space conditions were slightly warmer than the rated conditions of 68°F and 50% RH. This standard water use profile did not induce any resistance element operation for the HPWH. The solar system (SOLAR) had an effective conversion efficiency of 2.3 for this spring period, which is 23 lower than the SEF from the OG-300 rating from SRCC. The glycol-filled drain back system (SOLAR-DRAIN) was not properly commissioned in this period so it did not function as expected (see Section 4.5). The tankless unit with a small tank (HYBRID) locked out whenever the HPWH ran. This problem was fixed around April 26, but the overall efficiency only improved slightly. The HYBRID system efficiency was still well below expectations. The condensing tank had an efficiency about 10% below the rated thermal efficiency (TE). Field testing by the manufacturer had similarly shown applied efficiencies of 0.81 for earlier versions of this unit (Adams 2008). Field testing in California (Hoeschele and Brand 2013) also showed that efficiency for this unit was about 80% of the TE. Canadian field testing (Neale 2013) also measured efficiencies of 0.83 for this unit. Table 11. Summary of Water Heater Performance – CURRENT DOE Draw Profile April 10 to May 20, 2013 Rated Efficiency Ratio HW Use (gal/day) Supply Temp (F) Inlet Temp (F) Name Conversion Efficiency (-) Gas STD 0.58 0.58 EF 99.8% 71.1 135.8 52.8 HE-PVNT 0.68 0.67 EF 100.9% 71.6 131.9 49.5 SOLAR 2.32 3.20 SEF 72.4% 75.3 132.0 55.6 SOLAR-DRAIN 1.11 61.0 116.6 54.4 TANKLESS 0.90 0.94 EF 95.2% 61.0 117.6 59.9 HE-Cond 0.86 0.96 TE 89.5% 64.7 134.9 58.9 HYBRID 0.70 0.90 TE 77.6% 62.3 133.5 71.2 HPWH 2.53 2.40 EF 105.3% 59.7 128.0 57.3 Notes: The solar system has a Solar Energy Factor (SEF) instead of an Energy Factor (EF). Similarly, the High Efficiency Condensing Tank (HE-Cond) and the HYBRID unit (with a small tank) are rated as commercial units with a thermal efficiency (TE) instead of an EF. The test conditions were not fully consistent with those specified in the DOE Test Procedure, but were usually close. For instance the inlet water temperature is specified as 58°F in the procedure. The actual lab test conditions, shown in Figure 10 and Table 11, vary slightly from that specified value. Similarly, the supply temperature from the water heater is specified in the procedure as 135°F. Most systems were near that point for this test with the exception of the SOLAR-DRAIN and the TANKLESS units. 24 Figure 8. Comparing Measured Conversion Efficiency and Energy Factors – CURRENT Draw Profile 04/10/13 to 05/20/13 6 Conversion Efficiency (-) 5 4 SEF=3.2 SEF=3.1 3 EF=2.4 2 1 8 April Gas STD 15 22 6 29 May Solar Drain Tankless HE-PVNT Solar HE-Cond 20 13 Hybrid HPWH 04/10/13 to 05/20/13 1.0 TE=0.96 EF=0.94 Conversion Efficiency (-) TE=0.90 0.8 EF=0.67 0.6 EF=0.58 0.4 8 April Gas STD 15 HE-PVNT Solar 22 29 6 May Solar Drain Tankless HE-Cond 25 13 Hybrid 20 HPWH Figure 9. Daily Hot Water Use and Supply Temperatures – CURRENT Draw Profile 04/10/13 to 05/20/13 HW Use (gal/day) 80 60 40 8 15 22 29 April 6 13 20 6 13 20 May Supply Temperature (F) 04/10/13 to 05/20/13 140 120 100 8 15 April Gas STD 22 HE-PVNT Solar 29 May Solar Drain Tankless HE-Cond Hybrid HPWH Figure 10. Useful Energy vs. Inlet Water Temperature – CURRENT Draw Profile 04/10/13 to 05/20/13 60 Useful Energy (MBtu/day) 50 40 30 20 55 Gas STD 60 HE-PVNT Solar 65 70 Inlet Temperature (F) Solar Drain Tankless HE-Cond 26 Hybrid 75 HPWH 4.2 Impact of NEW Proposed Hot Water Use Profiles The proposed ASHRAE Standard 118.2 test procedure proposed three more realistic HW usage profiles to represent low, normal, and high use (ARHI 2013). Each profile has 12 events that are spread across the 24 hour period with most events in the morning or evening. Table 12 lists the events in these three profiles along with the total daily use4. Table 12. Summary New Hot Water Use Profiles for Proposed ASHRAE 118.2 Test Procedure Normal Use High Use Low Use Time Rate (gpm) Time (minutes) Volume (gallons) Rate (gpm) Time (minutes) Volume (gallons) Rate (gpm) Time (minutes) Volume (gallons) 6:00 1 2 2 1 2 2 1 2 2 6:30 1.7 9 15.3 3.4 8 27.2 1.5 9 13.5 7:40 1.7 8 13.6 1.7 9 15.3 1 1 1 16:30 1 4 4 1 4 4 1 4 4 16:45 1 3 3 1 3 3 1 3 3 17:30 1 3 3 1.7 2.5 4.25 1 3 3 18:00 1 1 1 1.7 9 15.3 1 1 1 18:45 1 1 1 1 1 1 1 1 1 18:50 1 1 1 1 1 1 1.5 1 1.5 22:15 1.7 8 13.6 1 2 2 1 2 2 22:45 1.7 1 1.7 1.7 1 1.7 1 2 2 23:00 1 5 5 1 6 6 1.5 4 6 64.2 82.75 40 The specified draw rates of 1, 1.7 and 3.4 gpm in the table are different than the capabilities of the laboratory test setup, which was designed to provide rates of 1, 2 or 3 gpm. To further complicate matters the flow limiters installed on each test station provided a slightly different flow than the nominal value. For example the 1 gpm flow limited allowed from 1 to 1.4 gpm of actual flow depending on the flow station, while the 2 gpm limiters provided 1.7 to 2.2 gpm of actual flow. Correction factors were applied to each station to determine the required solenoid runtime to achieve the desired total volume for each event. 4 The final test procedure issued by DOE in July 11, 2014 actually used slightly different water use profiles then the proposed ASHRAE 118.2 profiles from March 2013, which are included in Table 12. The final low, medium and high use profiles had total water use of 38, 55, and 84 gallons per day with 11, 12, draw events, respectively. The final test procedure is available at http://www.regulations.gov/#!docketDetail;D=EERE-2011-BT-TP-0042. 27 4.2.1 Proposed Normal Use Draw Profile The proposed “Normal Use” pattern is a more realistic draw profile made up of 12 events with a total water use of 64.2 gallons. The resulting draw profile for Unit 1 is shown in Figure 11 below (the variation from the desired 64.2 gallons per day was due to flow limiter variations). This profile was imposed on all the systems starting in September 18, 2013. The supply temperature was also lowered to 120°F on some units in order to reflect more realistic use patterns (except the SOLAR system, which remained at 135°F). Figure 11. Water Draw Profile Imposed on Water Heaters – Normal Use Profile 09/19/13 20 Water Use: 65.2 gal/day HW Use (gal) 15 10 5 0 22: 0: 18 19 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 20 Table 13 and Figure 12 show the measured conversion efficiency for these slightly different operating conditions. Similar overall performance was observed with this new use pattern compared to the CURRENT profile. The conversion efficiency for the solar systems are slightly lower since the weather was slightly cloudier in this early fall test period. The lockout problem with the HYBRID system was corrected in this period so the efficiency is slightly higher – but still is much lower than the value implied by the thermal efficiency. This water use profile also did not induce any resistance element operation for the HPWH unit. 28 Table 13. Summary of Water Heater Performance – Normal Use Profile September 18 to October 31, 2013 Rated Efficiency Ratio HW Use (gal/day) Supply Temp (F) Inlet Temp (F) Name Conversion Efficiency (-) Gas STD 0.56 0.58 EF 96.7% 64.90 119.5 65.9 HE-PVNT 0.66 0.67 EF 98.8% 81.80 125.2 65.5 SOLAR 1.90 3.20 SEF 60.90 130.7 68.1 SOLAR-DRAIN 1.39 63.80 117.4 66.9 TANKLESS 0.86 0.94 EF 91.3% 67.00 119.5 67.1 HE-Cond 0.85 0.96 TE 88.9% 64.70 122.7 67.8 HYBRID 0.73 0.90 TE 81.3% 60.30 114.8 66.0 HPWH 2.70 2.40 EF 112.5% 62.20 120.0 67.7 Notes: The solar system has a Solar Energy Factor (SEF) instead of an Energy Factor (EF). Similarly, the High Efficiency Condensing Tank (HE-Cond) and the HYBRID unit (with a small tank) are rated as commercial units with a thermal efficiency (TE) instead of an EF. 29 Figure 12. Comparing Measured Conversion Efficiency and Expected Energy Factors – Normal Use Profile 09/18/13 to 10/31/13 6 Conversion Efficiency (-) 5 4 SEF=3.2 SEF=3.1 3 EF=2.4 2 1 16 23 September Gas STD HE-PVNT Solar 30 7 14 October Solar Drain Tankless HE-Cond 21 Hybrid 28 HPWH 09/18/13 to 10/31/13 1.0 TE=0.96 EF=0.94 Conversion Efficiency (-) TE=0.90 0.8 EF=0.67 0.6 EF=0.58 0.4 16 23 September Gas STD HE-PVNT Solar 30 7 14 October Solar Drain Tankless HE-Cond 30 21 Hybrid 28 HPWH Figure 13 shows the daily variations as well as the supply temperatures for each system. Figure 13. Daily Hot Water Use and Supply Temperatures – Normal Use Profile 09/18/13 to 10/31/13 HW Use (gal/day) 80 60 40 16 23 September 30 7 14 21 28 21 28 October Supply Temperature (F) 09/18/13 to 10/31/13 140 120 100 16 23 September Gas STD HE-PVNT Solar 30 7 14 October Solar Drain Tankless HE-Cond Hybrid HPWH 4.2.2 Proposed Low Use Draw Profile The proposed “Low Use” pattern is a more a realistic draw profile for a small household made up of 12 events with a total water use of 40 gallons. The resulting profile for one of the stations is shown in Figure 14 below (the slightly different use for this day was due to flow limiter variations). This profile was imposed on several systems starting on June 18, 2014. Operation of standard water heater (Gas-STD) was stopped for this test due to problems keeping the pilot lit. Unreliable solenoid operation also caused us to stop operation on Test Station 2 (HE-PVNT) and Test Station 6 (HE-Cond). The supply temperature was set near 120°F for all systems except the SOLAR-DRAIN as shown in Figure 16. This water use profile did not induce any resistance element operation for the HPWH unit. 31 Figure 14. Water Draw Profile Imposed on Water Heaters – Low Use Profile Unit 5 07/05/14 15 Water Use: 44.3 gal/day HW Use (gal) 10 5 0 22: 0: 4 5 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 6 Table 14 and Figure 15 show the measured conversion efficiency for with this Low Use profile. Similar overall performance was observed with this new use pattern. The SOLAR system conversion efficiency is higher for this summer period (as expected). Several units were not operating due to solenoid problems. The efficiency of the HYBRID system and the TANKLESS unit is still much lower than the value implied by the thermal efficiency or energy factor. The EF for HPWH is very close to rated performance. Table 14. Summary of Water Heater Performance – Low Use Profile July 4 to September 22, 2014 Name Conversion Efficiency (-) Rated Efficiency Gas STD 0.58 EF HE-PVNT 0.67 EF 3.20 SEF SOLAR 794 SOLAR-DRAIN 117 TANKLESS 0.81 HE-Cond 0.94 EF 0.96 TE HW Use (gal/day) Supply Temp (F) Inlet Temp (F) 39.90 123.7 71.1 41.30 118.0 70.4 86.2% 39.30 116.6 71.2 Ratio HYBRID 0.65 0.90 TE 72.2% 41.90 115.3 71.2 HPWH 2.46 2.40 EF 102.5% 41.70 117.3 70.7 Notes: The solar system has a Solar Energy Factor (SEF) instead of an Energy Factor (EF). Similarly, the High Efficiency Condensing Tank (HE-Cond) and the HYBRID unit (with a small tank) are rated as commercial units with a thermal efficiency (TE) instead of an EF. 32 Figure 15. Comparison of Measured Conversion Efficiency and Expected Energy Factors – Low Use Draw Profile 07/04/14 to 09/22/14 6 Conversion Efficiency (-) 5 4 SEF=3.2 SEF=3.1 3 EF=2.4 2 1 30 7 July Gas STD 14 21 28 4 11 HE-PVNT Solar 25 18 August Solar Drain Tankless 1 8 September HE-Cond Hybrid 15 22 HPWH 07/04/14 to 09/22/14 1.0 TE=0.96 EF=0.94 Conversion Efficiency (-) TE=0.90 0.8 EF=0.67 0.6 EF=0.58 0.4 30 7 July Gas STD 14 21 HE-PVNT Solar 28 4 11 18 August Solar Drain Tankless 33 25 1 8 September HE-Cond Hybrid 15 HPWH 22 Figure 16. Daily Hot Water Use and Supply Temperatures – Low Use Profile 07/04/14 to 09/22/14 HW Use (gal/day) 50 45 40 35 30 30 7 14 21 28 July 4 11 18 25 August 1 8 15 22 15 22 September Supply Temperature (F) 07/04/14 to 09/22/14 140 120 100 30 7 July Gas STD 14 21 HE-PVNT Solar 28 4 11 18 August Solar Drain Tankless 25 1 8 September HE-Cond Hybrid HPWH 4.2.3 Proposed High Use Draw Profile The proposed High Use pattern is a more realistic profile for a large family made up of 12 events with a total water use of 82.8 gallons per day. The resulting profile for one of the stations is shown in Figure 17 below (the slightly different use for on this day was due to flow limiter variations). This profile was imposed on several systems starting on January 15, 2015. The supply temperature was set near 120°F for all systems. Not all the systems were operating this point due to flow limiter problems and solenoid failures. 34 Figure 17. Water Draw Profile Imposed on Water Heaters – High Use Profile Unit 5 01/17/15 30 Water Use: 84.4 gal/day 25 HW Use (gal) 20 15 10 5 0 22: 0: 16 17 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 18 Table 15 and Figure 18 show the measured conversion efficiency for the units with this High Use profile. The SOLAR system conversion efficiency is lower for this winter period (as expected). Several units were not operating due to solenoid problems. The efficiency of the HYBRID system and the TANKLESS unit are still lower than the value implied by the thermal efficiency or energy factor, but are higher than was observed with the lower usage profiles. Table 15. Summary of Water Heater Performance – High Use Profile January 15 to March 29, 2015 Name Conversion Efficiency (-) Gas STD 0.58 EF HE-PVNT 0.67 EF 3.20 SEF SOLAR 1.15 SOLAR-DRAIN 1.30 TANKLESS 0.88 HE-Cond Ratio HW Use (gal/day) Supply Temp (F) Inlet Temp (F) 36.0% 77.00 119.5 47.9 75.10 118.1 45.0 94.0% 83.30 117.6 52.2 Rated Efficiency 0.94 EF 0.96 TE HYBRID 0.78 0.90 TE 86.1% 77.70 113.7 48.8 HPWH 1.77 2.40 EF 73.8% 79.30 114.0 47.2 Notes: The solar system has a Solar Energy Factor (SEF) instead of an Energy Factor (EF). Similarly, the High Efficiency Condensing Tank (HE-Cond) and the HYBRID unit (with a small tank) are rated as commercial units with a thermal efficiency (TE) instead of an EF. 35 Figure 18. Comparison of Measured Conversion Efficiency and Expected Energy Factors – High Use Profile 01/15/15 to 03/29/15 5 Conversion Efficiency (-) 4 SEF=3.2 SEF=3.1 3 EF=2.4 2 1 12 19 26 2 9 16 2 23 9 March February January Solar Drain Tankless HE-Cond Gas STD HE-PVNT Solar 16 Hybrid 23 HPWH 01/15/15 to 03/29/15 1.0 TE=0.96 EF=0.94 Conversion Efficiency (-) TE=0.90 0.8 EF=0.67 0.6 EF=0.58 0.4 12 19 26 2 9 16 23 2 9 January February March Gas STD HE-PVNT Solar Solar Drain Tankless HE-Cond 36 16 Hybrid 23 HPWH Figure 19. Daily Hot Water Use and Supply Temperatures – High Use Profile 01/15/15 to 03/29/15 HW Use (gal/day) 100 90 80 70 60 12 19 26 January 2 9 16 23 2 February 9 16 23 9 16 23 March Supply Temperature (F) 01/15/15 to 03/29/15 140 120 100 12 19 26 2 9 16 23 2 January February March Gas STD HE-PVNT Solar Solar Drain Tankless HE-Cond Hybrid HPWH The conversion efficiency for HPWH is 1.77 compared to the rated EF of 2.4, because this water use profile induced resistance element operation after the larger draw. The performance of the HPWH unit over one day (February 15, 2015) is shown by Figure 20. The morning draw of 25 gallons induces the resistance elements to come on. The upper element comes on for 12.5 minutes followed by 40.5 minutes of lower element operation. Note that the control logic of the unit attempts to recover as quickly as possible, so compressor operation is locked out until the bottom element in the tank can fully bring the tank back to temperature. Similar performance for the same HPWH unit was observed in the field as discussed in Section 5.6. 37 Figure 20. Impact of High Use Profile on HPWH Performance 02/12/15 HPWH HW Use (gal) FW= 79.2 gal/day 25 2.0 13.0 20 25.0 DRAW= 25.0 gal 4.7 2.0 6.516.3 7.7 2.0 15 10 5 0 22: 0: 11 12 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 13 UPPER= 12.5 min, LOWER= 40.5 min ON LOWER OFF ON UPPER OFF 22: 0: 11 12 WE8= 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 13 02/12/15 7.0 kwh/day 5 Power (kW) 4 3 2 1 0 22: 0: 11 12 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 13 February 2015 38 4.3 Comparing Performance with Different Usage Profiles The measured conversion efficiencies with the different draw profiles are summarized in Table 16. As mentioned above, not all the profiles were run for each system due to problems with solenoids and pilot lights. A series of plots also shows the impact of each usage profile on conversion efficiency for each system: The standard water heater (Gas-STD) in Figure 21 shows that the conversion efficiency was always in line with the EF. The data show a slight efficiency increase with water use, as would be expected for a storage tank. Similarly, the power vented higher efficiency water heater (HE-PVNT) in Figure 22 shows that the conversion efficiency was also close to the EF and also showed a slight efficiency increase with water use. The SOLAR (Figure 23) and SOLAR-DRAIN (Figure 24) systems were more affected by differing performance on sunny days and cloudy days (Section 4.5 discusses solar performance in greater detail). The tankless unit in Figure 25 shows that the conversion efficiency always fell short of the 0.94 EF. Some efficiency improvement with greater water use was apparent. The large draws of the current procedure results in the best conversion efficiency – implying that the efficiency predicted by the current procedures overstates actual performance. The High Efficiency Condensing (HE-Cond) unit in Figure 26 always had conversion efficiencies that fell short of the TE of 0.96. While tests were not run for all the draw profiles, the efficiency does modestly increase with flow rate. The HYBRID unit in Figure 27 also had conversion efficiencies that fell short of the TE of 0.90. This unit showed more variation with water use than the other systems. The HPWH unit data in Figure 28 confirm the strong impact that usage profile has on the conversion efficiency. At the normal and low use profiles the unit runs without resistance element operation and the conversion efficiency is in good alignment with the EF (the variations are mostly due to changing space conditions). For the High Use case, the element comes on and reduces the conversion efficiency by 75%. Table 16. Summary of Conversion Efficiencies with Different Draw Patterns Name Rated Efficiency Current Pattern Normal Use Low Use High Use 64.2 gpd 64.2 gpd 40 gpd 82.8 gpd Gas STD 0.58 EF 0.58 0.56 HE-PVNT 0.67 EF 0.68 0.66 SOLAR 3.20 SEF 2.32 1.90 794 1.15 1.11 1.39 117 1.30 0.81 0.88 SOLAR-DRAIN TANKLESS 0.94 EF 0.90 0.86 HE-Cond 0.96 TE 0.86 0.85 HYBRID 0.90 TE 0.70 0.73 0.65 0.78 HPWH 2.40 EF 2.53 2.70 2.46 1.77 39 Figure 21. Impact of Draw Profile on Conversion Efficiency – Gas-STD Gas-STD - EF=0.58 0.8 Conversion Efficiency (-) Current Pattern Normal Use Low Use High Use Rating 0.6 0.4 20 40 60 80 100 Hot Water Use (gal/day) Figure 22. Impact of Draw Profile on Conversion Efficiency – HE-PVNT (other) HE-PVNT - EF=0.67 0.8 Conversion Efficiency (-) Current Pattern Normal Use Low Use High Use Rating 0.6 0.4 20 40 60 80 Hot Water Use (gal/day) 40 100 Figure 23. Impact of Draw Profile on Conversion Efficiency – SOLAR Solar - SEF=3.2 3.0 Conversion Efficiency (-) 2.5 2.0 Current Pattern Normal Use Low Use High Use 1.5 1.0 0.5 20 40 60 80 100 Hot Water Use (gal/day) Figure 24. Impact of Draw Profile on Conversion Efficiency – SOLAR-DRAIN Solar Drain 3.0 Conversion Efficiency (-) 2.5 Current Pattern Normal Use Low Use High Use 2.0 1.5 1.0 0.5 20 40 60 80 Hot Water Use (gal/day) 41 100 Figure 25. Impact of Draw Profile on Conversion Efficiency – TANKLESS Tankless - EF=0.94 1.0 Conversion Efficiency (-) Rating Current Pattern Normal Use Low Use High Use 0.8 0.6 20 40 60 80 100 Hot Water Use (gal/day) Figure 26. Impact of Draw Profile on Conversion Efficiency – HE-Cond HE-Cond - TE=0.96 1.0 Conversion Efficiency (-) Rating Current Pattern Normal Use Low Use High Use Rating 0.8 0.6 20 40 60 80 Hot Water Use (gal/day) 42 100 Figure 27. Impact of Draw Profile on Conversion Efficiency – HYBRID Hybrid - TE=0.90 Conversion Efficiency (-) 1.0 Rating 0.8 Current Pattern Normal Use Low Use High Use Rating 0.6 20 40 60 80 100 Hot Water Use (gal/day) Figure 28. Impact of Draw Profile on Conversion Efficiency – HPWH HPWH - EF=2.4 Conversion Efficiency (-) 3.0 2.5 Rating 2.0 Current Pattern Normal Use Low Use High Use 1.5 20 40 60 80 Hot Water Use (gal/day) 43 100 4.4 Standby Losses and Parasitic Power 4.4.1 Standby Losses From May 22 to June 27, 2013 the water heaters in the laboratory ran in standby mode with no hot water use. This provided an indication of the standby losses from each system. The air temperature on 1st floor (for DHW1 and DHW2) was 70°F. The air temperature for the other units on the 4 th floor was 75°F. The measured standby losses are summarized in Table 17. The figures show the variations in losses over the period. Table 17. Summary of Water Heater Standby Losses Unit Gas Use (MBtu/day) Electric Use (kWh/day) DHW1 – GAS-STD ~10 - DHW2 – HE-PVNT 6.3 0.135 DHW6 – HE-COND 6.9 0.228 DHW7 – HYBRID 8.3 Not measured DHW8 – HPWH - 0.688 For DHW1 (AO Smith GCVX-50-100), the conventional, natural-draft water heater, the standby losses showed much more fluctuation than expected, as shown in Figure 29. The variation may indicate significant differences in the amount of draft induced through the unit on windy and calm days. The average was 23.2 MBtu/day while the most common minimum value was just over 10 MBtu/day. The hot water set point was 130-135°F. Figure 29. Daily Standby Gas Use for DHW1-GAS-STD DHW1 Daily Gas Use (MBtu/day) 80 60 40 AVG = 23.2 20 0 20 May 27 3 10 17 June 2013 44 24 For DHW2-HE-PVNT (Rheem 43VP40SE2), the power vented unit with an EF of 0.67, the average standby losses were 6.3 MBtu/day Figure 30). The hot water set point as about 130°F. Figure 30. Daily Standby Gas Use for DHW2-HE-PVNT DHW2 12 Daily Gas Use (MBtu/day) 10 8 6 4 AVG = 6.3 2 0 20 27 May 3 10 17 24 June 2013 Average gas use is 6.9 MBtu/day with no water use for the DHW6-HE-Cond (AO Smith Vertex), as shown in Figure 31. Standby losses reported on AHRI certificate are 499 Btu/h, or 12.0 MBtu/day. Tank set point is 135°F. Figure 31. Daily Standby Gas Use for DHW6_HE-Cond DHW6 Daily Gas Use (MBtu/day) 15 10 5 AVG = 6.9 0 20 May 27 3 10 17 June 2013 45 24 For the DHW7-HYBRID the tank set point is 130°F. Average gas use is 8.3 MBtu/day with no water use (Figure 32). Standby losses reported on AHRI certificate are 378 Btu/h, or 9.0 MBtu/day. Figure 32. Daily Standby Gas Use for DHW7-HYBRID DHW7 12 Daily Gas Use (MBtu/day) 10 8 6 4 AVG = 8.3 2 0 20 27 May 3 10 17 24 June 2013 Standby losses for DHW8-HPWH (Geospring™ GEH50DEEDSC) are 0.69 kWh/day. The hot water set point was 130°F. Figure 33. Daily Standby Electric Use for DHW8 DHW8 Daily Electric Use (kWh/day) 1.0 0.8 0.6 0.4 AVG = 0.69 0.2 0.0 20 May 27 3 10 17 June 2013 46 24 4.4.2 Parasitic Electric Loads All the higher efficiency gas-fired systems also use electricity in addition to natural gas. Figure 34 shows the trend of daily electric consumption versus daily gas consumption for these four systems. As would be expected all the system consume electricity even with little or no gas use (the y-intercept). Then electricity increases linearly with gas use. Table 18 summarizes the standby loss term, the slope of the electric-to-gas and lists the power use with a normal water use pattern (64.2 gal/day). The Stand loss term varies from 0.1 to 0.3 kWhday. The slope is high for the power-vented unit (HE-PVNT), which makes sense given relatively large fan on that unit. The other higher efficiency units generally have a smaller slope, except for the HYBRID. All these uses use less than 0.5 kWh per day under normal HW use profile. Figure 34. Trends of Electric Consumption versus Natural Gas Input HE-PVNT Tankless 0.25 Electric (kWh/day) Electric (kWh/day) 0.4 0.2 kWh/therm: 0.358 kWho= 0.10 0.0 0.20 0.15 0.10 0.05 kWh/therm: 0.109 kWho= 0.13 0.00 0.0 0.2 0.4 0.6 0.8 1.0 0.00 0.10 0.20 0.30 0.40 0.50 0.60 Gas (therm/day) Gas (therm/day) HE-Cond HYBRID 0.50 Electric (kWh/day) Electric (kWh/day) 0.8 0.6 0.4 0.2 0.0 kWh/therm: 0.141 kWho= 0.23 0.0 0.2 0.4 0.6 0.40 0.30 0.20 0.10 kWh/therm: 0.333 kWho= 0.30 0.00 0.8 0.0 0.2 Gas (therm/day) 0.4 0.6 0.8 Gas (therm/day) Table 18. Electric Use of Gas-Fired Systems System Standby Losses (kWh/day) Slope (kWh/therm) Electricity w/ Normal Use (kWh/day) HE-PVNT 0.10 0.358 0.32 Tankless 0.13 0.109 0.17 HE-Cond 0.23 0.141 0.27 HYBRID 0.30 0.333 0.41 47 4.5 Comparing Performance of Solar Systems The COE laboratory has two different solar systems installed (see Table 19). The Rheem unit is a conventional system with a charged glycol loop. This type of system is widely used in New York State. The Wagner is a new German design that is a drain back system using glycol. Drain back systems are widely used in southern climates because they offer superior thermal performance. However, the application of drain back systems in colder climates has been limited due to fear of collector freeze damage. This new design uses a glycol fluid with a combined reservoir/heat exchanger/pump assembly built into the solar storage tank. This simplifies the installation of the system and provides freeze protection. Table 19. Solar Systems Installed in the Laboratory Collector Area Rheem (System 3) 6.10 m2 Wagner (System 4a/4b) 5.22 m2 System Arrangement Single tank 120 gal with internal glycol HX and two electric elements Two Tank 92 gal glycol drain back (internal reservoir & HX) 52 gal std electric tank SRCC Solar Fraction 0.71 0.80 The Wagner system controller has an option to include booster pump to help overcome the static head on a drain back system where the collector is much higher than the tank. The system was initially installed without a booster pump. In an effort to improve on poor performance, a booster pump was added on July 3, 2013 in series with the main pump to help overcome the initial static head. The Wagner controller only ran the booster pump during the first 4-5 minutes of main pump operation. Both solar systems included instrumentation to determine key performance parameters. QU is useful heat delivered to the load (it is integrated every 3 seconds by the data logger). QSL is the standby losses for the 52 gallon electric tank. Testing for standby losses in February 2014 showed that this tank required 1 kWh per day to maintain temperature with no hot water use 5. QE is the supplemental electric energy used to heat the tank as well as the power for the solar pumps (91 Watts for the Rheem; 85 Watts for 1 pump on the Wagner; and 160 Watts for two pumps after May 9, 2014). From these values delivered solar energy (QS), solar fraction (SF) and COP were determined using the equations below. 5 The standby losses for the 120 gallon Rheem tank actually approached 2 kWh/day on cloudy days, but smaller losses for the 52 gallon tank were still assumed since this is a more appropriate base case. 48 QU = k x FW x (TH – TC) QS = QU + QSL - QE COP = QU / QE SF = 1 - QE / (QU + QSL) 4.5.1 Initial Performance Observations (September and October 2013) The initial data collected in September and October 2013 showed that the two solar systems behaved as expected on cloudy days (the Wagner was slightly better). However, the performance of the Wagner system degraded on clear, sunny days (with high solar flux). Figure 35 and Figure 36 compare the daily performance of the two solar systems in that period in terms of solar fraction (SF) and electric element/pump operation (QE). Figure 37 directly compares the solar fraction and the normalized electric input for the two systems and shows that the Wagner has better performance on less sunny days while the Rheem is better on clear sunny days. Figure 35. Solar Fraction vs. Solar Flux for Fall 2013 09/19/13 to 10/31/13 1.0 Rheem: 0.38 SF Wagner: 0.32 SF Solar Fraction (-) 0.8 0.6 0.4 0.2 0.0 0 2 4 6 Daily Solar Flux (kWh/m^2) 49 8 Figure 36. Daily Electric Power vs. Solar Flux for Fall 2013 09/19/13 to 10/31/13 12 Rheem: 6.8 kWh/day Wagner: 6.4 kWh/day Daily Power Input (kWh/day) 10 8 6 4 2 0 0 2 4 6 8 Daily Solar Flux (kWh/m^2) Figure 37. Direct Comparison of Rheem vs. Wagner Performance for Fall 2013 Electricity Wagner Power (kWh/gal) Solar Fraction Wagner Fraction (-) 1.0 0.8 0.6 0.4 0.2 0.0 0.0 0.2 0.4 0.6 0.8 1.0 Rheem Fraction (-) COP Wagner COP (-) 3 50 1 0.15 0.10 0.05 0.00 0.00 0.05 0.10 0.15 Rheem Power (kWh/gal) 4 2 0.20 0.20 The two sets of plots below illustrate the Wagner performance issue by showing detailed performance on two different days. Figure 38 shows a moderately sunny day (October 1) when the total flux for the day was 3.4 kWh/m2. The fluid temperatures to and from the solar collector are similar for the two systems. Figure 39 shows a clear, sunny day (September 25) when the total flux for the day was 6.6 kWh/m 2. In this case the collector temperatures on the Wagner system (as measured near the tank) started the day increasing as expected, but at about 10 am the temperatures suddenly dropped. Temperatures remained low until about 4 pm, even though the pump remained running the entire time. This anomaly was due to the pump’s inability to overcome both the high static head AND the vapor pressure that builds up in the collector as the fluid gets hot. As a result the flow for the drain back collector stops because the fluid in the return line back to the tank vaporizes and breaks the siphon when fluid gets too hot (i.e., the system becomes “vapor-locked”). For this installation, the height from the tank (4th floor) to the collector (roof or 6th floor) was higher than for than most residential single applications (the height of two commercial stories is 32 ft). The length of 3/8 inch piping from the tank to the collector also created more pressure drop to overcome. 51 Figure 38. Performance Comparison for a Moderately Sunny Day (October 1, 2013) 10/01/13 Solar Flux (W/m^2) 1200 1000 800 3.4 kWh/day 600 400 200 0 22: 0: 30 1 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 2 Rheem Pump = 4.8 hr/day, Wagner Pump = 6.6 hr/day ON One Pump Wagner Pump OFF ON Rheem Pump OFF 22: 0: 30 1 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 2 10/01/13 Rheem Collector Outlet Rheem Collector Inlet Wagner Collector Outlet Wagner Collector Inlet Rheem Solar Frac: 0.52 Wagner Solar Frac: 0.35 150 100 50 22: 0: 30 1 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 2 52 Figure 39. Performance Comparison for a Sunny Day (September 25, 2013) 09/25/13 Solar Flux (W/m^2) 1200 1000 800 6.6 kWh/day 600 400 200 0 22: 0: 24 25 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 26 Rheem Pump = 7.6 hr/day, Wagner Pump = 8.1 hr/day ON One Pump Wagner Pump OFF ON Rheem Pump OFF 22: 0: 24 25 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 26 09/25/13 Rheem Collector Outlet Rheem Collector Inlet Wagner Collector Outlet Wagner Collector Inlet Rheem Solar Frac: 0.64 Wagner Solar Frac: 0.28 150 100 50 22: 0: 24 25 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 26 53 4.5.2 The Wagner Drain-Back System is Fixed To solve the problem identified above, we wired the two pumps to operate together on May 9, 2014. This forced the two pumps to always operate together (previously the second pump had been connected to R2 on the controller and only ran during the first few minutes of startup). Figure 40 is a daily plot that shows the Wagner System started to work properly on a sunny day after this fix was implemented. Figure 41 and Figure 42 show the same daily trends as before, but with different symbols for both before and after the Wagner system was fixed. All data in the plots below correspond to the hot water use of 68-70 gallons per day for both systems. 54 Figure 40. Performance Comparison for a Sunny Day (May 20, 2014) 05/20/14 Solar Flux (W/m^2) 1200 1000 800 7.2 kWh/day 600 400 200 0 22: 0: 19 20 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 21 Rheem Pump = 8.0 hr/day, Wagner Pump = 8.0 hr/day ON Two Pumps Wagner Pump OFF ON Rheem Pump 22: 0: 19 20 OFF 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 21 05/20/14 Rheem Collector Outlet Rheem Collector Inlet Wagner Collector Outlet Wagner Collector Inlet Rheem Solar Frac: 0.70 Wagner Solar Frac: 0.70 150 100 50 22: 0: 19 20 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 21 55 Figure 41. Solar Fraction vs. Solar Flux (before and after Wagner Fix) 03/03/14 to 06/17/14 1.0 Rheem: 0.49 SF Wagner: 0.42 SF Wagner: 0.72 SF (fixed) Solar Fraction (-) 0.8 0.6 0.4 0.2 0.0 0 2 4 6 8 Daily Solar Flux (kWh/m^2) Figure 42. Daily Electric Power vs. Solar Flux (before and after Wagner Fix) 03/03/14 to 06/17/14 12 Rheem: 5.9 kWh/day Wagner: 6.8 kWh/day Wagner: 3.4 kWh/day (fixed) Daily Power Input (kWh/day) 10 8 6 4 2 0 0 2 4 6 Daily Solar Flux (kWh/m^2) 56 8 Figure 43. Direct Comparison of Rheem vs. Wagner Performance (before and after Wagner Fix) Electricity Wagner Power (kWh/gal) Solar Fraction Wagner Fraction (-) 1.0 0.8 0.6 0.4 0.2 0.0 0.0 0.2 0.4 0.6 0.8 1.0 0.20 0.15 0.10 0.05 0.00 0.00 Rheem Fraction (-) 0.05 0.10 0.15 0.20 Rheem Power (kWh/gal) COP Table 20 4 below summarizes the overall impact of the fixing Wagner System (i.e., operating two pumps together). Wagner COP (-) The solar fractions for the two systems were within 0.02, but this difference increased to 0.05 when the second pump was3added. Similarly, before the fix, the amount of electric use was lower for the Wagner system by 0.2 kWh/day. After the fix, the Wagner was lower by 0.6 kWh/day. The imposed draw profile both before and after the 2 fix was 60 gallons per day. 1 Table 20. Summary Impact of Fixing Wagner System 0 0 1 2 3 4 Rheem System Wagner System Difference Before Fix (March 3 to May 9) 0.40 0.42 +0.02 After Fix (May 9 to June 17) 0.67 0.72 +0.05 Rheem System Wagner System Difference Before Fix (March 3 to May 9) 7.0 6.8 -0.2 After Fix (May 9 to June 17) 4.0 3.4 -0.6 Rheem COP (-) Solar Fraction (-) Electric Use (kWh/day) The analysis above focused on short periods in the spring season with the same water use pattern. Table 21 compares the monthly data for the two solar systems from August 2013 through to February 2015, showing the monthly values for solar fraction, electric use and hot water use. Some of the more subtle differences discussed in 57 the previous sections did not have a significant impact on the overall monthly numbers. Water use varied across the period as different water use profiles were imposed on the systems in the laboratory. Table 21. Monthly and Annual Performance Summary for Solar Systems Solar Fraction (-) Electric Use (kWh) HW Use (gal/day) Month Solar Flux (kWh/m2) Rheem Wagner Rheem Wagner Rheem Wagner Aug-13 159.7 0.65 0.43 123.9 157.9 66.1 70.7 Sep-13 143.1 0.57 0.35 142.1 175.9 59.6 64.7 Oct-13 90.0 0.29 0.30 239.1 206.6 60.5 63.6 Nov-13 74.1 0.24 0.25 220.7 234.5 54.8 62.7 Dec-13 34.6 0.08 0.13 301.3 291.9 61.2 61.2 Jan-14 68.9 0.13 0.15 316.0 308.4 64.4 62.9 Feb-14 58.5 0.09 0.14 215.5 206.1 43.8 42.7 Mar-14 113.5 0.29 0.26 241.3 252.3 67.4 65.1 Apr-14 133.7 0.48 0.53 182.6 166.3 70.6 68.8 May-14 169.4 0.65 0.71 131.9 111.4 70.0 68.0 Jun-14 160.2 0.75 0.74 86.9 87.6 56.7 56.5 Jul-14 164.1 0.98 0.84 34.8 55.2 40.6 41.9 Aug-14 152.8 0.95 0.82 39.0 58.0 39.9 41.4 Sep-14 143.4 0.91 0.80 43.2 57.9 39.4 40.7 Oct-14 90.9 0.54 0.49 101.4 111.8 40.6 41.3 Nov-14 60.2 0.23 0.25 154.3 157.7 40.1 41.1 Dec-14 32.3 0.08 0.13 199.0 198.7 40.1 41.3 Jan-15 76.0 0.15 0.19 300.1 290.4 61.5 61.2 Feb-15 20.4 0.05 0.11 387.4 359.8 76.8 74.5 0.47 0.46 1,746 1,771 51.1 51.0 2014 The overall annual solar fractions for 2014 were 0.47 for the Rheem and 0.46 for the Wagner, with average water use of 51 gallons per day. The overall annual electric use for electric elements and the solar pumps was 1,746 kWh for the Rheem and 1,771 kWh for the Wagner. The Wagner has a better solar fraction in the winter months primarily because the second 92 gallon tank in this two tank system gains heat from the surrounding room air even when the solar input to the tank is zero. When we bias the 12 month period to end in February 2015, relative differences between the two systems were not significantly affected. 58 5 Field Test Results 5.1 Characteristics of Field Test Sites The domestic hot water (DHW) systems were monitored in eighteen (18) homes with one to five permanent occupants per household (2.7 occupants on average as of January 2013). At households with variable occupancy, we were able to identify the actual occupancy down to a monthly or daily basis. Figure 44 shows the monitoring period for each site. Figure 44. Duration of Field Monitoring Period at Each Test Site DHW Monitoring by Site Jun-12 Sep-12 Dec-12 Mar-13 Jun-13 Sep-13 Dec-13 Mar-14 Jun-14 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 Sep-14 Dec-14 Previous Owners Completed Monitoring Figure 45 shows the average monthly occupancy for all 18 sites from December 2012 through December 2014. Several sites had a consistent household occupancy, as shown by the horizontal lines on the plot. Interviews and surveys allowed us to pinpoint household occupancy at sites where the number of occupants varied over the course of the year. There were a handful of sites with college-age occupants, one site where an adult traveled for work on a weekly basis, and another site that added a new member to the household. 59 Figure 45. Average Monthly Occupancy at Each Test Site Average Monthly Occupancy by Site 6 Site 1 Site 2 5 Number of Occupants Site 3 Site 4 4 Site 5 Site 6 3 Site 7 Site 8 2 Site 9 Site 10 1 Site 11 Site 12 0 Site 13 Site 14 Month Site 15 The houses ranged in size from 940 to 2,926 square feet (average of 1,936 sq ft), with between two to four bedrooms and one to three bathrooms. Fourteen of the sites are serviced by public water supplies, while four sites have private wells. 60 Table 22 summarizes the type and size of DHW system in use at each site as well as the water supply source and the number of occupants. More details for each field test site can be found in Appendix A. Table 22. Summary of 18 Field Test Sites No. Identifier DHW System Size Water Supply Occupants 1 Ballina Rd, Cazenovia GE HPWH with Recirculation Loop Installed 4/10/2013 50 gal Well 2 to 5 2 Gifford St, Syracuse HE Condensing Gas Storage WH Installed 5/1/2013 50 gal Public 3 3 Brickyard Falls Rd, Manlius Tankless Gas Water Heater Installed 3/18/2013 Tankless Public 2 4 Burton St, Cazenovia Tankless with Manifold and PEX and Standard Gas Storage with copper 40 gal Public 4 to 5 5 Hornady Dr, Syracuse Gas Storage 40 gal Public 2 6 Carrys Hill Rd, Chittenango Boiler with Indirect Tank Well 4 to 5 7 Rathbun Rd, Cazenovia AO Smith Electric Storage 40 gal Well 2 to 4 8 Astilbe Path, Liverpool Rheem Condensing Tankless DHW and Solar Hydronic Heating 120 gal Public 1 9 Bunker Hill Way, Syracuse (A) Power Vent Tank 40 gal Public 2 10 Bunker Hill Way, Syracuse (B) Power Vent Tank 40 gal Public 2 11 Bunker Hill Way, Syracuse (C) Power Vent Tank 40 gal Public 1 to 2 12 Burton St, Cazenovia (B) Standard Gas Storage 40 gal Public 4 13 Tipp Hill, Syracuse Standard Gas Storage 40 gal Public 2 14 Fay Lane, Minoa Power Vent Tank 40 gal Public 2 15 Marcellus St, Syracuse (A) Power Vent Tank 40 gal Public 2 to 3 16 Tioga St, Syracuse Rinnai Gas Tankless Tankless Public 2 17 Marcellus St, Syracuse (B) Quiet Side Combi System HW and Infloor heating Tankless Public 3 to 4 18 Ridge Rd, Cazenovia Boiler with Indirect Tank & small Elec. Tankless 40 gal Well 3 As discussed above in Section 3.2, there were three different types of datalogger systems installed at the 18 sites. Details about the data loggers used at each site are given in Appendix A. A Campbell CR1000 datalogger was installed at Sites 1 to 5. A Campbell CR200x datalogger was installed at eight sites to measure hot water use at 1561 minute intervals as well as at 5-second intervals during hot water draws. The other five sites used a Campbell CR10 or CR-10x datalogger to collect hot water flow data at 15-minute intervals. 5.2 Hot Water Usage 5.2.1 Hot Water Use Profiles The total hot water use for each 15-minute interval was collected at all 18 sites. The plots below show the average profiles at sites only during periods when the household had two occupants (this includes sites 1, 3, 5, 7, 9, 10, 11, 13, 14, 15 and 16). The daily profiles in Figure 46, Figure 47, and Figure 48 show hot water use profiles for a cold month (February), a swing month (May), and a hot month (August), respectively. The average profile for each site is plotted with a colored line while the overall average is shown with a thick black line. Data from days with no recorded hot water use for the entire day (i.e., vacations) were excluded. Additional plots for individual sites are available in Appendix C. Figure 46. Hot Water Use Profile for 2-Person Home during a Cold Month (February 2013 & 2014) 15-Minute Daily Profile for 2-Person Home in February 0.50 Site Site Site Site Site Site Site Site Site Site Site Flow (gpm) 0.40 11 Sites Average Daily Total: 40.8 gal/day Daily Range: 0.0 to 258.0 gal/day 1 3 5 7 9 10 11 13 14 15 16 0.30 0.20 0.10 0.00 0 2 4 6 8 10 12 14 Hour of Day 62 16 18 20 22 24 Figure 47. Hot Water Use Profile for 2-Person Home during a Swing Month (May 2013 & 2014) 15-Minute Daily Profile for 2-Person Home in May 0.50 Site Site Site Site Site Site Site Site Site Flow (gpm) 0.40 9 Sites Average Daily Total: 35.8 gal/day Daily Range: 0.0 to 153.1 gal/day 1 3 5 9 10 11 13 14 15 0.30 0.20 0.10 0.00 0 2 4 6 8 10 12 14 16 18 20 22 24 Hour of Day Figure 48. Hot Water Use Profile for 2-Person Home during a Hot Month (August 2013 & 2014) 15-Minute Daily Profile for 2-Person Home in August 0.50 Site Site Site Site Site Site Site Site Site Site Flow (gpm) 0.40 10 Sites Average Daily Total: 31.7 gal/day Daily Range: 0.0 to 138.7 gal/day 1 3 7 9 10 11 13 14 15 16 0.30 0.20 0.10 0.00 0 2 4 6 8 10 12 14 Hour of Day 63 16 18 20 22 24 The plots below show the average profiles at sites when the household had four occupants for all or part of the time (this includes sites 1, 4, 6, 7, 12, 17, and 18). The daily profiles in Figure 49, Figure 50, and Figure 51 show hot water use profiles for a cold month (February), a swing month (May), and a hot month (August), respectively. The average profile for each site is plotted with a colored line while the overall average is shown with a thick black line. Data from days with no recorded hot water use for the entire day (i.e., vacations) were excluded. Additional plots for individual sites are available in Appendix C. Figure 49. Hot Water Use Profile for 4-Person Home during a Cold Month (February 2013 & 2014) 15-Minute Daily Profile for 4-Person Home in February 0.50 Site Site Site Site Site 5 Sites Average Daily Total: 84.6 gal/day Daily Range: 1.3 to 251.5 gal/day 4 7 12 17 18 Flow (gpm) 0.40 0.30 0.20 0.10 0.00 0 2 4 6 8 10 12 14 Hour of Day 64 16 18 20 22 24 Figure 50. Hot Water Use Profile for 4-Person Home during a Swing Month (May 2013 & 2014) 15-Minute Daily Profile for 4-Person Home in May 0.50 Site Site Site Site Site 5 Sites Average Daily Total: 79.8 gal/day Daily Range: 0.0 to 186.5 gal/day 1 4 7 17 18 Flow (gpm) 0.40 0.30 0.20 0.10 0.00 0 2 4 6 8 10 12 14 16 18 20 22 24 Hour of Day Figure 51. Hot Water Use Profile for 4-Person Home during a Hot Month (August 2013 & 2014) 15-Minute Daily Profile for 4-Person Home in August 0.50 Site Site Site Site Site 5 Sites Average Daily Total: 52.9 gal/day Daily Range: 0.0 to 191.3 gal/day 1 6 7 17 18 Flow (gpm) 0.40 0.30 0.20 0.10 0.00 0 2 4 6 8 10 12 14 Hour of Day 65 16 18 20 22 24 5.2.2 Average Daily Hot Water Use Using the 15-minute data we were able to calculate the average HW use for each site for individual days when the home was occupied. Table 23 shows the beginning and ending dates of data collection for all 18 field sites, along with the average, median, and standard deviation of HW use (gal/day) at each site. Table 23. Beginning and Ending Dates for Data Collection at Sites with 15-minute Monitoring Site Occupancy Data Start Date Data End Date Average HW Use (gal/day) Median HW Use (gal/day) St Dev HW Use (gal/day) Site 1 Variable (1-5) 12/1/2012 12/31/2014 50.2 45.5 34.9 Site 2 3 12/14/2012 5/25/2014 75.8 67.0 48.8 Site 3 2 12/13/2012 12/31/2014 30.8 28.4 18.1 Site 4 Variable (4-5) 12/10/2012 7/18/2014 124.0 125.5 38.4 Site 5 2 12/14/2012 12/31/2014 55.6 54.6 22.9 Site 6 Variable (4-5) 1/24/2013 1/3/2014 24.9 23.8 14.1 Site 7 Variable (2-4) 1/24/2013 2/21/2014 42.5 40.7 23.3 Site 8 1 12/1/2012 2/4/2013 48.2 47.1 17.5 Site 9 2 1/19/2013 2/3/2014 21.7 20.6 10.8 Site 10 2 12/1/2012 2/19/2014 46.7 44.9 17.7 Site 11 Variable (1-2) 1/19/2013 11/27/2014 27.8 27.1 13.7 Site 12 4 12/1/2012 4/5/2013 77.3 76.9 24.3 Site 13 2 1/10/2013 2/20/2014 54.1 52.0 16.2 Site 14 2 12/1/2012 2/4/2014 56.5 56.4 17.7 Site 15 Variable (2-3) 12/14/2012 12/4/2014 25.9 23.4 18.9 Site 16 2 6/18/2013 2/19/2014 12.6 10.4 7.9 Site 17 Variable (3-4) 1/24/2013 2/25/2014 81.0 74.3 41.1 Site 18 Variable (3-4) 12/14/2012 2/21/2014 49.2 50.3 18.4 2-person 2 12/1/2012 12/31/2014 39.9 38.9 23.8 4-person 4 12/1/2012 5/10/2014 73.8 66.2 45.9 All Sites Variable (1-5) 12/1/2012 12/31/2014 51.7 45.2 37.5 Table 23 above calculates average hot water use excluding days where there was no hot water use (i.e., vacation or vacant days). Table 24 determines the average hot water use including these vacant or no-water-use days. The overall average hot water use decreases by 0.5 gallons per day when vacant days are included. The sites with more vacant days saw larger changes in the average daily use, as would be expected. All other plots and graphs in this report using 15-minute data are based on averages that exclude these vacant days and correspond to Table 23. 66 Table 24. Impact of Including Vacation and Missing Days in Hot Water Use Calculation Site Occupancy Occupied Days Vacant Days Excluding Vacant Days: Average HW Use (gal/day) Including Vacant Days: Average HW Use (gal/day) Site 1 Variable (1-5) 697 33 50.2 47.9 Site 2 3 528 2 75.8 75.5 Site 3 2 693 25 30.8 29.7 Site 4 Variable (4-5) 569 1 124.0 123.8 Site 5 2 709 9 55.6 54.9 Site 6 Variable (4-5) 315 1 24.9 24.9 Site 7 Variable (2-4) 394 1 42.5 42.5 Site 8 1 66 1 48.2 48.2 Site 9 2 381 1 21.7 21.7 Site 10 2 439 7 46.7 46.0 Site 11 Variable (1-2) 568 10 27.8 27.3 Site 12 4 119 1 77.3 77.3 Site 13 2 402 6 54.1 53.3 Site 14 2 424 7 56.5 55.5 Site 15 Variable (2-3) 695 5 25.9 25.7 Site 16 2 245 2 12.6 12.5 Site 17 Variable (3-4) 398 1 81.0 80.8 Site 18 Variable (3-4) 421 14 49.2 47.7 67 Figure 52 uses the 15-minute data to show the median hot water daily use as a symbol with plus-or-minus one standard deviation about the average shown by the vertical line. The aggregate 2-person house had an average, median, and standard deviation of 39.9, 38.9, and 23.8 gallons per day, respectively. For the 4-person data set, the average, median, and standard deviation were 73.8, 66.2, and 45.9 gallons per day, respectively. Figure 52. Median Hot Water Use at Each Site with a Range of Plus or Minus One Standard Deviation about the Mean Median Daily Volume (+/- Std Dev) By Site 150 2-Person Data 4-Person Data Mixed/Other Data HW Use (gal/day) 100 Average 4-Person 50 Average 2-Person 0 1 2 3 4 5 6 7 8 9 10 11 Site Number 68 12 13 14 15 16 17 18 Daily average hot water use for all households with two occupants and for households with four occupants is shown in Figure 53. The average value was calculated independently based on each valid day of data for each site with the correct number of occupants on a given day during each month. Days with zero hot water use were excluded from the calculations. Figure 53 clearly shows that hot water use varies seasonally for both the 2-person and 4-person households. This trend is primarily due to occupants (or machines) mixing in more hot water when the incoming ground or city water is colder in the winter. The amount of hot water required to reach 100°F temperature at the shower head is greater when cold water is at a lower temperature in the winter. Seasonal cold water trends are shown later in this document. Figure 53. Average Daily Hot Water Use for 2-Person and 4-Person Homes Average Daily Hot Water Use 250 2-Person Households (11 Sites) 4-Person Households (7 Sites) Hot Water Use (Gal/Day) 200 150 100 50 0 Jan Feb Mar Apr May Jun Jul 69 Aug Sep Oct Nov Dec Figure 54 compares the average water use for each two-person household to the overall average. The plot confirms there is significant variation between two-person households. Figure 54. Average Daily Hot Water Use for 2-Person Households Compared to the Average Average Daily Hot Water Use for 2-Person Household (11 Sites) 250 Site Site Site Site Site Site Site Site Site Site Site Hot Water Use (Gal/Day) 200 1 Av erage 3 Av erage 5 Av erage 7 Av erage 9 Av erage 10 Av erage 11 Av erage 13 Av erage 14 Av erage 15 Av erage 16 Av erage Overall Average 150 100 50 0 Jan Feb Mar Apr May Jun Jul Aug Sep Oct Nov Dec Besides household-to-household variation, occupants in a given house use different amounts of hot water on a dayto-day basis. This can be explained by the different activities that occupants engage in on different days. Figure 55 shows the data for sites with two occupants. For each month the overall average, plus-or-minus one standard deviation, is shown as a blue line for the month. The median, maximum, and minimum are shown in black. The data for each month on the plot only includes days where hot water use was greater than zero and the number of occupants was equal to two. The average number of sites included in each monthly calculation is shown at the top of the plot. For some months, days were excluded because they did not have two occupants or because usage was zero. Each monthly value is based on data from 5 to 7 sites (out of a possible 11 sites). The variation in average daily hot water use between sites is again shown in Figure 56 in a slightly different way. In this case the average for each site for each month is shown as a colored symbol and a colored vertical line represents the minimum and maximum daily hot water use in the month for that site. The black trend line super imposes the overall average for all the two-person sites. 70 Figure 55. Average Daily Hot Water Use for 2-Person Households Average Daily Hot Water Use for 2-Person Household (11 Sites) 250 7.1 6.6 5.9 5.8 5.0 5.1 5.3 5.5 6.6 6.3 5.7 4.8 Nov Dec Median Average +/- 1 Std. Dev. 200 Hot Water Use (Gal/Day) Maximum / Minimum 150 100 50 0 Jan Feb Mar Apr May Jun Jul Aug Sep Oct Figure 56. Average Daily Hot Water Use for 2-Person Households with Each Site Shown Average Daily Hot Water Use for 2-Person Household (11 Sites) 250 Site Site Site Site Site Site Site Site Site Site Site Hot Water Use (Gal/Day) 200 1 Av erage 3 Av erage 5 Av erage 7 Av erage 9 Av erage 10 Av erage 11 Av erage 13 Av erage 14 Av erage 15 Av erage 16 Av erage Overall Average Site Average with Min / Max Bar 150 100 50 0 Jan Feb Mar Apr May Jun Jul Aug 71 Sep Oct Nov Dec Figure 57 compares the average water use for each four-person household to the overall average. The plot confirms there is significant variation between the four-person households. As discussed above, household-to-household variation in four-person homes is also significant. Occupants in a given house use different amounts of hot water on a day-to-day basis, since they engage in different activities on different days. Figure 58 shows the data for sites with four occupants. For each month the overall average plus-orminus one standard deviation is shown in blue. The median, maximum, and minimum are shown in black. The data for each month on the plot only includes days where the total hot water use was greater than zero and the number of occupants was equal to four. The average number of sites included in each monthly calculation is shown at the top of the plot. For some months, days were excluded because they did not have four occupants or usage was zero. Each monthly value is based on data from 1 to 3 sites. Therefore, the results in the four-occupant households may have a higher uncertainty than for two person households. The variation in average daily hot water use between sites is again shown in Figure 59. In this case the average for each site for each month is shown as a colored symbol and a colored vertical line represents the minimum and maximum daily hot water use in the month for that site. The thick black line super imposes the overall average for all the four person sites. Figure 57. Average Daily Hot Water Use for 4-Person Households Compared to the Average Average Daily Hot Water Use for 4-Person Household (7 Sites) 250 Site Site Site Site Site Site Site Hot Water Use (Gal/Day) 200 1 Av erage 4 Av erage 6 Av erage 7 Av erage 12 Av erage 17 Av erage 18 Av erage Overall Average 150 100 50 0 Jan Feb Mar Apr May Jun Jul Aug 72 Sep Oct Nov Dec Figure 58. Average Daily Hot Water Use for 4-Person Households Average Daily Hot Water Use for 4-Person Household (7 Sites) 250 2.5 2.8 2.8 2.3 1.7 1.4 1.2 1.7 0.9 1.0 1.0 1.6 Oct Nov Dec Median Average +/- 1 Std. Dev. 200 Hot Water Use (Gal/Day) Maximum / Minimum 150 100 50 0 Jan Feb Mar Apr May Jun Jul Aug Sep Figure 59. Average Daily Hot Water Use for 4-Person Household with Each Site Shown Average Daily Hot Water Use for 4-Person Household (7 Sites) 250 Site Site Site Site Site Site Site Hot Water Use (Gal/Day) 200 1 Av erage 4 Av erage 6 Av erage 7 Av erage 12 Av erage 17 Av erage 18 Av erage Overall Average Site Average with Min / Max Bar 150 100 50 0 Jan Feb Mar Apr May Jun Jul Aug 73 Sep Oct Nov Dec 5.3 Entering Cold Water Temperatures As mentioned above, the entering cold water temperatures from a well or public water supply vary across the year. Cold water temperatures were measured at six sites (sites 1, 2, 3, 4, 5, and 8). The entering water temperature for each site could be inferred two different ways: using a flow-weighted average calculation in the data logger at the scan interval, or using the daily minimum entering water temperature from the 15-minute data Figure 60 shows a comparison between the two values. In theory the flow weighted values should be more correct, yet delays in the temperature sensor response could sometimes lead to skewed values. We judged that the minimum value observed in a day – which typically corresponded to a large hot water draw – provides the best indication of the true entering water temperature for that day. Figure 60. Daily Minimum Entering Water Temperature vs. Daily Flow-Weighted Average EWT Entering Water Temperature Daily Flow-Weighted Average EWT (F) 80 70 60 Site 1 (Private) 50 Site 2 (Public) Site 3 (Public) Site 4 (Public) Site 5 (Public) 40 Site 8 (Public) 30 30 40 50 60 70 80 Daily Minimum EWT (F) Figure 61 shows the daily entering water temperatures for the six sites where it was measured. The sites on a public or city water supply show a much larger seasonal variation in entering water temperature than for the home with a private well. The seasonal fluctuation of the city water supply is 25-30°F across the year, since these pipes are often closer to the surface. Site 1, which has a private supply from a well that is more than 200 ft deep, showed much less 74 variation across the year. Figure 62 shows the relationship between daily water entering temperature (minimum EWT) and daily hot water use. Because of the day-to-day variations at each site it is difficult to discern a trend. However, overall most of the sites might imply lower hot water use with warmer inlet temperatures. Figure 61. Seasonal Variation in Entering Water Temperature Entering Water Temperature 80 Site 1 (Private) Site 2 (Public) Site 3 (Public) Site 4 (Public) Site 5 (Public) Site 8 (Public) Daily Minimum EWT (F) 70 60 50 40 30 Q4 Q1 2013 Q2 Q3 Q4 Q1 Q2 2014 75 Q3 Q4 2015 Figure 62. Daily Hot Water Use vs. Entering Water Temperature Daily Hot Water Use 400 Site 1 (Private) Site 2 (Public) Site 3 (Public) Site 4 (Public) Daily Hot Water Use (gallons) Site 5 (Public) Site 8 (Public) 200 0 30 40 50 60 70 80 Daily Minimum EWT (F) 5.4 Hot Water Draw Events At the thirteen (13) sites listed in the table below, data were collected at 5-second intervals so that each water draw event could be separately identified. Table 25 also summarizes the average hot water use as well as the number of draw events per day through June 2014. Some minor differences between the average use given in this table and in the 15-minute data table (Table 23) are noted. Appendix C provides histograms and other statistics of the event data for each site and each household size (2-5 persons) for all the 5-second data sites. 76 Table 25. Beginning and End Dates for Event Data at Each Site with 5-second Monitoring Site Occupancy Data Data Average Average Start Date End Date HW Use (gal/day) Draw Events 83 (No/day) Site 1 Variable (2-5) 12/01/2012 02/13/2014 53a Site 2 3 12/14/2012 05/25/2014 77 52 Site 3 2 12/13/2012 12/31/2014 31 24 Site 4 Variable (4-5) 12/10/2012 07/04/2014 122b 280 Site 5 2 12/14/2012 12/31/2014 57 39 Site 10 2 12/01/2012 02/19/2014 47 48 244 Site 12 4 12/20/2012 04/04/2013 63c Site 13 2 01/10/2013 02/16/2014 54 44 Site 14 2 12/01/2012 02/04/2014 57 34 76 Site 15 Variable (2-3) 12/14/2012 12/05/2014 27d Site 16 2 01/18/2013 02/19/2014 12 35 Site 17 Variable (3-4) 01/24/2013 02/25/2014 80 65 Site 18 Variable (3-4) 12/14/2012 02/21/2014 49 91 Notes: a- Site 1’s 15-minute average HW use differed from the 5-second average because 5-second data was not collected through June 2014. b- Site 4’s 15-minute average HW use differed from the 5-second average because 5-second data was not collected on 1/09/2013, 1/30/2013, and 2/06/2013. c- Site 12’s 15-minute average HW use differed from the 5-second average because 5-second data was not collected from 1/12/13 to 2/13/2013. d- Site 15’s 15-minute average HW use differed from the 5-second average because 5-second data was not collected from 2/14/2013 to 4/01/2013. Figure 63 shows the data for all 5-second interval sites, plotting the daily hot water use versus the number of hot water draw events. Each site is shown as a different color. Sites with 2 people are shown as “+” while sites with 4 people are shown as a “□”. There is significant scatter in the data, though some sites do show similar patterns on the plot. Figure 64 reduces each site to a single data point, using the median hot water use and median number of draws (or events). In this case, sites with 2 people are shown as “Δ” while sites with 4 people are shown as a “□”. Sites with variable occupancy are shown with a “*”. Each site is identified by its own color. The large symbols indicate the medians for the 2-person and 4-person households. The median 2-person household uses 43 gallons per day with 37 draw events. The median 4-person household uses 80 gallons per day with 120 draw events. 77 Figure 63. Hot Water Use vs. Number of Draw Events (all days through December 2014) Daily Hot Water Use (5423 days plotted) 250 2-Person Home 4-Person Home Other HW Use (gal/day) 200 150 100 50 0 0 100 200 300 400 500 Number of Events Site 1 Site 2 Site 3 Site 4 Site 5 Site 10 Site 12 Site 13 Site 14 Site 15 Site 16 Site 17 Site 18 Figure 64. Hot Water Use vs. Number of Draw Events (Median for Sites through December 2014) Median Daily Hot Water Use (13 sites plotted) 150 2-Person Data 4-Person Data Mixed Data HW Use (gal/day) 100 50 All 4-Person Data All 2-Person Data 0 0 100 200 300 Number of Events Site 1 Site 2 Site 3 Site 4 Site 5 Site 10 Site 12 Site 13 78 Site 14 Site 15 Site 16 Site 17 Site 18 . 5.5 Identifying Draws and Estimating Hot Water Waste Energy is wasted every time there is a hot water draw. Hot water runs through distribution piping to the fixture for the occupant’s use. After the draw is complete, the hot water in that pipe cools down to ambient conditions over several hours. The next time hot water is required at that fixture the occupant runs the previously-heated water down the drain while waiting for hot water to appear at the fixture again. Because this process is repeated at several fixtures throughout each day, hot water waste is estimated to be on the order of 10%–30% of total hot water use. We installed temperature sensors near each fixture on the distribution systems at the Field Test Sites 1 through 5 as described in Section 3.2 and Figure 5. The temperature sensor near each fixture was used to determine the portion of hot water draw that was deemed useful, using the methods described in Section 3.2.2. This analysis is fully described summarized in a separate Building America Report (Henderson and Wade, 2014). A sample of the results from that report is summarized here. Figure 63 shows one flow event with temperatures corresponding to the master bath shower. The plot in the upper left shows the flow trace during the event at 5 second intervals (ending with five intervals at zero flow). The red line corresponds to the most common flow rate (in gpm) or “mode” during the event. The plot in the lower left shows the various temperatures during the event. Blue lines correspond to trunk temperatures (TT1, TT2…) while the green lines are the fixture temperatures (TF1, TF2,..). Each line is identified by a number. The plot at the upper right shows the temperature rise for each sensor compared to the beginning of the event (using the same colors). The red line on the upper right and lower left plots is the supply temperature from the water heater unit (TS). The black line on these plots corresponds to the cold water inlet (TC). The trunk line with the highest temperature rise is indicated by blue text and the fixture temperature with the biggest rise is indicated with green text. This first shower of the day lasts for about 6 minutes (84 intervals) and the total draw is 8.8 gallons. The temperature leaving the tank increases as expected and the inlet cold water temperature drops as cold water flows by the sensor. The trunk to the master bedroom increases by 40°F as expected. In this case, there is no temperature sensor for the shower fixture, only for the bathroom sink. So a trunk temperature rise with no large change in fixture temperature indicates a shower. The automated procedure in this case classified this event as a draw at the “Master Shower” fixture. Of the 8.79 gallons of hot water used, only 8.03 gallons was deemed as useful by the criteria (in this case the trunk temperature reaching 100°F). 79 Figure 65. A Sample Hot Water Draw is Identified and Evaluated at Site 1 12/02/12 08:00:05 GAL = 8.79 TH - Hot Temperature Rise (F) Flow Rate (gpm) 2.0 1.5 1.0 0.5 0.0 TC = Cold 30 20 10 2 6 57 4 3 5 4 3 2 1 8 0 -10 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. 0. :0 :1 :2 :3 :4 :5 :6 :7 :0 :1 :2 :3 :4 :5 :6 :7 12/02/12 08:00:05 Intervals=84 140 Temperature (F) 1 120 TT1: Trunk Temp - Master Bathroom: Rise= 40.7 TT2: Trunk Temp - Bathroom 2: Rise= 5.8 1 100 Master Shower 80 26 3 4 3 8 5 1 57 2 4 60 40 0. 0. 0. 0. 0. 0. 0. 0. :0 :1 :2 :3 :4 :5 :6 :7 Useful GAL = 8.03 (TT > 100. ) TF6: Fixture Temp 6 - Master Bath Sink: Rise= 3.8 TF7: Fixture Temp 7 - Bathroom 2 Sink: Rise= 0.3 DHW Site 1 The results from repeating this analysis for all 8,534 events that occurred over 123 days at Site 1 are shown in Table 26. This home has two adults and two college-age students who returned for the college breaks (who mostly used bathroom 2). Fewer than half of the 8,534 events in the 123-day period could be assigned. However, these classified (or assigned) events accounted for 94% of the total water use. Numerous small events could not be assigned. The average unclassified event was less than 0.1 gal. Of the unclassified events, only 18 were over more than 1 gal in the 123-day period. Overall, about 82% of the total classified water use was deemed to be useful, based on the pipe temperature threshold. As expected, the sinks result in the largest amount of hot water waste on a percentage basis. 80 Table 26. Summary of Hot Water Draw Identification at Site 1 December 1, 2012 to April 2, 2013 (123 Days, 8,354 events) Events per Day Total Hot Water Use (gpd) Useful Hot Water (gpd) Wasted Hot Water (gpd) Useful % Dishwasher 1.5 2.7 2.4 0.3 90% Kitchen Sink 17.0 9.1 5.7 3.3 63% Half Bath Sink 2.1 0.7 0.1 0.5 21% Washing Mach 0.7 9.1 8.3 0.8 91% Utility Sink 0.3 0.9 0.5 0.4 53% Master Sink 6.8 2.2 0.6 1.5 28% Master Shower 1.5 17.8 17.0 0.8 95% Bath 2 Sink 1.7 1.2 0.6 0.6 49% Bath 2 Shower 0.7 8.4 7.7 0.8 91% Unaccounted 36.8 3.4 – 3.4 0% All Events 69.4 55.4 42.9 12.5 77% Classified 33 52.0 42.9 9.1 82% % Classified 47% 94% 100% 73% This process was repeated at all five field test sites. Overall, the process was able to classify less than half of the water draws in the five homes but the classified draws accounted for about 95% of the hot water volume in each home. This classification process was achieved without the need to install flow meters for each fixture (which would have been cost-prohibitive and more disruptive to homeowners). The average number of events at each home ranged from 26 per day to 180 per day. A temperature of 90°F at the fixture piping (or 100°F at the trunk line) was selected as the threshold for gauging usefulness. The amount of hot water deemed to be useful ranged from a low of 75% at Site 4 to a high of 91% at Site 5—thus implying 9%–25% waste. Site 4 may have had a lower useful percentage in part be due to the fact that the sensors installed on cross-linked polyethylene (PEX) piping may have had a slower thermal response. As expected, the amount of hot water waste was found to be higher for bathroom and kitchen sinks and lowest for showers and washing machine draws. 81 5.6 Field Test Site 1 – HPWH Performance Field Site 1 had a General Electric 50 gallon Heat Pump Water Heater (model GEH50DEEDSR) installed on April 10, 2013. Figure 66 shows that the daily conversion efficiency (thermal energy out divided by electric energy in) for the unit as function of hot water use. Occasionally a large water draw resulted in operation of the electric elements. These days are shown with a red diamond. The efficiency is significantly reduced on these days. Days with element operation are not strongly correlated to the daily hot water use. The blue *’s indicate days when the compressor was off and the unit operated like a conventional electric water heater. The green diamonds indicate very small amounts of element operation which are discussed in more detail below. Figure 67 shows the same data but with input power as function of water use. The power shows a strong linear trend with hot water use – except on days with element operation. The linear trend of electric use projects back to 2 kWh/day with no hot water use. This compares to the value of 0.69 kWh/day measured in the laboratory. The operation of the recirculation pump may account for most of the additional standby losses. Table 27 summarizes the monthly performance of the HPWH. The average annual conversion efficiency for May 2013 to April 2014 was 1.4 with an average water use of 43.7 gallons per day. The nominal or rated EF for this unit is 2.4. The monthly data shows that the HPWH compressor stopped working in August 2014 and reverted to resistance element operation. Resistance-only operation provided the opportunity to directly compare hybrid heat pump operation and resistanceonly operation. Comparing the month efficiencies for December 2013 and 2014, which had similar water use, shows the conversion efficiencies were 1.37 and 0.67 respectively. This comparison implies that the HPWH reduces electric use compared to standard electric operation by one half. 82 Figure 66. Conversion Efficiency (or COP) as a Function of Hot Water Use DHW1 - 04/10/13 to 03/31/15 3.0 Conversion Efficiency (-) 2.5 2.0 Elements ON 1.5 1.0 0.5 0.0 0 50 100 150 200 Hot Water Use (gal/day) Figure 67. HPWH Input Power as a Function of Hot Water Use DHW1 - 04/10/13 to 03/31/15 30 Input Power (kWh/day) 25 Elements ON 20 15 10 5 0 0 50 100 150 Hot Water Use (gal/day) 83 200 Table 27. Summary of Monthly HPWH Performance HW Use (gal/day) Electric Use (kWh) COP (-) Element Runtime (hrs) Vacation Days May-13 69.3 182.9 1.71 9.6 0 Jun-13 60.5 139.4 1.80 5.6 2 Jul-13 39.2 108.2 1.51 3.6 7 Aug-13 44.7 128.9 1.47 5.7 9 Sep-13 37.3 101.7 1.49 2.7 2 Oct-13 25.6 97.9 1.10 3.2 9 Nov-13 45.4 133.5 1.42 6.9 0 Dec-13 61.1 200.4 1.37 19.1 1 Jan-14 29.9 120.5 1.12 6.1 10 Feb-14 34.9 117.5 1.22 4.7 8 Mar-14 45.0 155.6 1.35 7.4 1 Apr-14 31.3 125.5 1.10 7.2 9 May-14 61.6 167.0 1.65 7.5 0 Jun-14 32.3 112.7 1.22 4.7 6 Jul-14 68.1 177.2 1.65 11.4 4 Aug-14 62.2 155.4 1.71 5.8 0 Sep-14 43.7 277.2 0.66 56.0 4 Oct-14 39.1 294.5 0.57 65.7 3 Nov-14 38.2 290.0 0.57 65.1 6 Dec-14 59.5 418.3 0.67 94.2 0 Jan-15 22.7 267.9 0.40 60.1 7 Feb-15 41.8 319.4 0.57 71.9 2 Mar-15 29.6 306.2 0.47 68.4 10 Annual 43.7 1,612.0 1.41 81.7 58 Several days with electric element operation are shown in the following figures. Each shows the hot water draw pattern, the operating status of the upper (SE1) and lower (SE2) elements, and power use profile for each day. It typically takes a large draw to induce element operation. The numbers displayed on the water use plot indicate the number of gallons associated with each draw event. Figure 68 shows that on April 10, 2013 a 20 gallon draw following a 9.8 gallon draw was sufficiently large to activate the element. Once the elements start, they operate for 80-90 minutes (at 4.5 kW). Figure 69 shows another large draw (or series of draws) on April 23 that also induced element operation. Figure 70 shows operation for May 21 where large draws within a few hours of each other induced two distinct cycles of element operation. 84 Figure 71 shows a day with only a few minutes of element operation that occurred for no apparent reason. This unexpected behavior started to occur more frequently in the fall of 2013. Figure 68. Plot of HPWH Performance for a Day with Element Operation - April 10, 2013 04/10/13 FW= 41.4 gal/day 12 9.8 HW Use (gal) 10 DRAW= 20.0 gal 0.9 4.0 20.0 1.2 2.9 1.3 0.9 0.4 0.0 8 6 4 2 0 22: 0: 9 10 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 11 SE1= 25.8 min, SE2= 56.9 min ON SE2 OFF ON SE1 OFF 22: 0: 9 10 WE= 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 11 04/10/13 8.0 kwh/day 5 Power (kW) 4 3 2 1 0 22: 0: 9 10 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 11 April 2013 85 Figure 69. Plot of HPWH Performance for a Day with Element Operation - April 23, 2013 04/23/13 FW= 101.2 gal/day HW Use (gal) 25 1.2 0.1 7.6 20 22.3 DRAW= 54.2 gal 0.0 1.1 11.9 0.7 54.2 0.2 1.6 0.3 15 10 5 0 22: 0: 22 23 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 24 SE1= 18.4 min, SE2= 63.3 min ON SE2 OFF ON SE1 OFF 22: 0: 22 23 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 24 04/23/13 WE= 10.7 kwh/day 5 Power (kW) 4 3 2 1 0 22: 0: 22 23 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 24 April 2013 86 Figure 70. Plot of HPWH Performance for a Day with Significant Element Operation - May 21, 2013 05/21/13 FW= 114.6 gal/day HW Use (gal) 15 0.1 10.1 0.1 1.1 DRAW= 64.7 gal 1.0 1.1 64.7 0.2 33.7 0.0 0.0 0.2 2.3 10 5 0 22: 0: 20 21 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 22 SE1= 14.2 min, SE2= 130.5 min ON SE2 OFF ON SE1 OFF 22: 0: 20 21 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 22 05/21/13 WE= 14.1 kwh/day 5 Power (kW) 4 3 2 1 0 22: 0: 20 21 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 22 May 2013 87 Figure 71. Plot of HPWH Performance for a Day with Small Amounts of Element Operation November 12, 2013 11/12/13 FW= 34.1 gal/day HW Use (gal) 10 0.2 0.2 6.0 8 DRAW= 17.7 gal 17.7 0.3 4.7 2.9 0.2 0.30.1 6 4 2 0 22: 0: 11 12 SE1= 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 13 0.0 min, SE2= 2.8 min ON SE2 OFF ON SE1 OFF 22: 0: 11 12 WE= 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 13 11/12/13 3.1 kwh/day Power (kW) 0.8 0.6 0.4 0.2 0.0 22: 0: 11 12 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 13 November 2013 88 All days through May 28, 2014 with any element operation are shown on Figure 72. The electric elements are usually activated by a 30 gallon draw. In some cases draws as small as 20 gallons activated the elements – typically when a smaller draw had just recently occurred (and the total of the two draws was near to or exceeding 30 gallons). Figure 72. Plot of Element Runtime as Function of Hot Water Draw Size 200 2 cycles of element operation Element Runtime (min) 150 100 1 cycle of element operation 50 few minutes of unexplained operation 0 0 20 40 60 80 Largest Draw Volume (gal) 89 100 120 5.6.1 Unexpected Aspects of HPWH Performance Figure 73 is a shade plot showing when the lower element (SE2) on the HPWH tank operated from October 2013 through February 2014. The periods with normal periods of element operation appear as the black 1-2 hour events. The many small 2-6 minute periods of operation appear as light gray intervals. The small events started in late October 2013 and continued through until late January 2014. Table 28 lists all the unexplained events that occurred over the entire monitoring period. In addition to the periods on the shade plot, other grouping of events also occurred in April 2014. The table also shows the water use for each of these days. The events do not appear to have been linked to changes in daily water use. A portion of these events (shown in red) showed a different operating pattern with 12-16 minutes of operation for the top element (SE1). These short periods of operation are also unexpected relative to the expected control scheme of the unit. Figure 73. Shade Plot Showing Unexplained Periods When Lower Electric Element Runs a Small Amount SE2 24 22 20 18 Hour of Day 16 14 12 10 8 6 Period with Short Element Operation 4 2 0 October November December 2013 January 2014 Day (MAX/MIN = 90 15.00/ 0.00 ) Feb Table 28. Summary of Days with Unexpected Element Operation Date 7/19/2013 10/29/2013 11/3/2013 11/5/2013 11/10/2013 11/12/2013 11/13/2013 11/14/2013 11/19/2013 11/23/2013 11/24/2013 11/25/2013 11/26/2013 11/29/2013 11/30/2013 12/2/2013 12/3/2013 12/4/2013 12/7/2013 12/8/2013 12/9/2013 12/10/2013 12/11/2013 12/13/2013 12/14/2013 12/15/2013 12/16/2013 12/17/2013 12/18/2013 12/20/2013 12/21/2013 12/28/2013 12/30/2013 HW Use (gal) 60.6 32.4 30.0 87.0 33.6 34.1 60.6 56.7 25.4 35.9 26.5 16.9 32.7 34.9 59.2 44.7 39.6 33.9 53.9 15.7 38.0 34.7 49.9 33.1 35.9 40.1 50.3 34.3 59.1 49.2 89.0 17.5 64.5 SE1 (min) SE2 (min) 16.3 - 3.0 1.4 3.6 1.5 2.8 4.7 4.1 3.3 4.7 4.9 3.2 5.2 1.7 5.2 1.5 5.4 3.8 1.7 5.0 3.3 3.1 3.7 1.7 4.8 6.6 3.3 7.6 3.5 5.4 3.2 1.4 4.7 Date 1/2/2014 1/3/2014 1/4/2014 1/6/2014 1/7/2014 1/8/2014 1/9/2014 1/10/2014 1/12/2014 1/14/2014 1/15/2014 1/16/2014 1/18/2014 1/20/2014 2/9/2014 4/10/2014 4/11/2014 4/12/2014 4/13/2014 4/16/2014 4/18/2014 4/20/2014 4/21/2014 4/23/2014 4/24/2014 4/25/2014 4/26/2014 4/27/2014 4/28/2014 4/29/2014 4/30/2014 5/2/2014 5/3/2014 5/4/2014 5/5/2014 5/6/2014 5/7/2014 5/8/2014 5/11/2014 5/12/2014 5/20/2014 7/21/2014 HW Use (gal) 24.5 0.0 1.6 0.0 0.0 1.8 0.1 0.0 1.4 0.0 0.2 4.9 84.0 77.7 52.1 53.9 8.0 58.3 113.3 29.2 26.2 41.4 32.9 32.0 40.6 44.0 59.8 26.6 10.9 33.9 71.1 21.3 23.1 45.0 44.2 69.1 45.5 49.0 101.2 SE1 (min) SE2 (min) 12.3 12.8 12.7 13.8 3.6 1.4 1.5 1.7 3.3 1.6 1.8 1.8 5.8 1.7 3.5 5.0 3.4 3.4 1.7 1.6 6.3 5.1 3.5 5.0 5.4 6.6 6.8 6.3 5.2 6.8 6.5 4.8 1.4 1.6 6.8 3.9 3.2 2.9 1.8 1.7 2.1 3.1 - Notes: Black data are short periods of lower element operation (SE2). Red data are days with upper element operation (SE1) 91 Around August 3, 2014 the power draw of the HPWH compressor suddenly started to change. Figure 74 shows how the compressor power started to fluctuate for a few days right before stopping operation on September 6. The fluctuation in power might imply a slow leak of refrigerant charge or some other slowly-failing components such as the evaporator fan. From that point on the resistance elements satisfied the water heating load. Figure 74. Last Few Days of HPWH Compressor Operation 5 Element Power (4.5 kW) Power (kW) 4 3 2 Normal Compressor Power 1 0 1 2 3 Fluctuating Compressor Power 4 5 6 7 8 9 10 11 12 September 2014 5.6.2 HPWH Interactions with the Space The psychrometric plot in Figure 75 below shows two distinct groupings of the daily data: One trend corresponding to the summer period when humidity is high. One trend in the winter when the basement dries out (and becomes colder) because outdoor conditions are dry and cold. Figure 76 shows the daily wet bulb and dry bulb in basement. While the design conditions for EF test specify 68°F and 50% RH (which corresponds to a wet bulb near 57°F), the conditions in this basement were often much colder. 92 Figure 75. Psychrometric Conditions in Basement – with and without HPWH Operation DHW1 - 11/16/12 to 05/28/14 0.020 HPWH ON 0.015 Humidity Ratio (lb/lb) HPWH OFF Dehumidifier set at 60% RH 0.010 80% DOE Test Conditions (68°F, 50%) 60% 0.005 40% Winter Period (2012/2013, before HPWH) 20% 50 55 60 65 70 75 0.000 80 Dry Bulb Temperature (F) Figure 76. Wet Bulb and Dry Bulb in Basement – with and without HPWH Operation DHW1 - 11/16/12 to 05/28/14 65 HPWH ON 60 Wet Bulb Temperature (F) HPWH OFF 55 DOE Test Conditions (68°F, 50%) 50 45 Winter Period (2012/2013, before HPWH) 40 55 60 65 Basement Temperature (F) 93 70 Figure 77 shows effect of HPWH and dehumidifier operation on temperature and humidity conditions in the basement. There were minimal temperature and humidity variations before the HPWH was installed on April 10, 2013. Once the HPWH started to operate the temperature near the units started to vary by as much 10°F. As the temperature decreased the dew point decreased as well, but the relative humidity increases as the temperature is depressed. Dehumidifier (DH) operation started in late May 2013. However the dehumidifier runtime sensor was not installed until Jun 12, 2013. DH runtime is shown on the bottom of the figure. Figure 77. Basement Temperature and Humidity Shown with DH Operation – Entire Test Period Basement Temperature Trends 60 40 Crawl Space Near Unit Dew Point (Near Unit) Temperature Run Time (min) 20 Q4 Q1 2012 2013 Q2 Q3 Q4 Q1 Q2 2014 Dehumidifier Status Basement Temperatures and RH 15 80 100 10 80 60 Dehumidifier Set Point: 60% RH 5 60 40 0 20 Q4 2012 Q4 Q1 Q2 2013 Q1 Q2 2012 2013 Basement Temp (Near Unit) Basement RH (Near Unit) Q3 Q4 Q3 Q4 40 Q1 Q2 2014 Q1 Q2 2014 Dehumidifier Status Run Time (min) 15 10 5 0 Q4 Q1 2012 2013 Q2 Q3 Q4 Q1 2014 94 Q2 20 Relative Humidity (%) Temperature (F) 80 Figure 78 shows the same data for one day on June 20. Each time the HPWH runs the temperature near the unit drops by 5-10°F. The dew point also drops. However, the relative humidity increases as the space is cooled. This increase in relative humidity causes the dehumidifier to stay on continuously for the 3 hour period when the HPWH is on (8-11 am). In the short term, HPWH operation induces additional DH operation. Longer terms impacts are discussed below. Figure 78. Basement Temperature and Humidity Shown with DH Operation – June 20, 2013 Basement Temperature Trends - 06/20/13 60 Crawl Space Near Unit Dew Point (Near Unit) 40 20 22: 0: 19 20 2: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 21 Dehumidifier Status - 06/20/13 Basement Temperatures and RH -06/20/13 15 Temperature Run Time (min) 4: 80 100 10 80 60 5 Dehumidifier Set Point: 60% RH 60 0 2022: 0: 2: 4: 6: 8: 10: Basement Temp (Crawl Space) Basement Temp (Near Unit) Basement RH (Near Unit) 12: 14: 16: 18: 20: 19 22: 20 0: 2: 4: 6: 8: 10: 12: 19 20 40 14: 16: 18: 20: 40 22: 0: 22: 21 0: 21 Dehumidifier Status - 06/20/13 Run Time (min) 15 10 5 0 22: 0: 19 20 2: 4: 6: 8: 10: 12: 14: 16: 18: 20: 22: 0: 21 95 20 Relative Humidity (%) Temperature (F) 80 Figure 79 compares the daily average humidity ratio near the HPWH unit and to the humidity ratio outdoors (using weather data from the Syracuse Airport). As expected there is a strong correlation between basement humidity and outdoor humidity due to air leakage. In the winter the humidity in the basement is slightly higher than outdoors due to moisture generation in the house (HPWH moisture removal in the winter is minimal since the dew point is so low). In the summer, both HPWH and DH operation tend to remove moisture, which pushes the basement humidity ratio below ambient. Figure 79. Comparison of Daily Average Basement and Outdoor Humidity Ratios Humidity Ratio Comparison 0.015 Basement Humidity (lb/lb) Winter 0.010 Summer 0.005 0.000 0.000 0.005 0.010 0.015 0.020 Outdoor Humidity (lb/lb) Although HPWH operation triggers the dehumidifier operation in the short term, on average across a day it reduces the total load on the dehumidifier by removing some of the moisture from the space. Figure 80 shows the trend of dehumidifier operation with ambient humidity ratio. The red diamond highlights days when the hot water use was high and the HPWH operated for more than 600 minutes per day. The green triangles highlight days when the water use was lower and the HPWH operates less than 300 minutes. The DH operates more when the HPWH is on more often. The figure also shows that dehumidifier runtime was affected by the outdoor humidity ratio. 96 Figure 80. Effect of Outdoor Humidity Ratio on Dehumidifier Runtime Outdoor Humidity vs. Dehumidifier Operation Dehumidifier Runtime (min/day) 1500 1000 HPWH Runtime > 600 min/day HPWH Runtime < 300 min/day 500 0 0.000 0.005 0.010 0.015 0.020 Outdoor Humidity (lb/lb) Multi-linear regression used to relate the dehumidifier runtime with HPWH runtime and outdoor humidity ratio. The relation is given as: DH Where DH = a0 + a1×WO + a2×HP - Dehumidifier Runtime (minutes/day) HP - HPWH Runtime (minutes/day) WO - Outdoor Humidity Ratio (lb/lb) The detailed statistical results of the multi-linear regression are given in Table 29. The coefficient for HPWH runtime (a2) has a value -0.215, indicating that each additional hour of HPWH runtime reduces dehumidifier runtime by 0.215 hours. The t-statistic for this coefficient is greater than 2, indicating it is statistically different than zero at the 90% confidence level (i.e., significant). This coefficient is used to predict the overall annual impact of HPWH on dehumidifier runtime and energy use in the table below. 97 Table 29. Multi-linear Regression Results Parameter Coefficient St.Dev. T-ratio ======================================================== a0 -70.796859 38.188783 -1.8538653 a1 107834.44 3390.6148 31.803802 a2 -0.21532982 0.083295891 -2.5851194 R-Squared = 0.72706893 Coefficient of Variation, CV = 0.67269096 Mean Bias Error, MBE = 4.5500627e-015 Analysis of Variance Source Sum of Squares D.F. Mean Square F-Ratio =========================================================== Model 1.6060515e+008 3 53535049. Residual 32952693. 380 86717.612 617.34920 =========================================================== Total 1.9355784e+008 383 Table 30 shows that DH energy is about 864 kWh for the year in this basement. Running the HPWH is estimated to have reduced DH energy use by 84 kWh over the year, or about 10%. This compares to the $20 savings estimated by ACEEE (2011) in Section 2.1.7. Table 30. Monthly Summary of Dehumidifier and HPWH Operation Apr-13 May-13 Jun-13 Jul-13 Aug-13 Sep-13 Oct-13 Nov-13 Dec-13 Jan-14 Feb-14 Mar-14 Apr-14 May-14 Jun-14 Jul-14 Aug-14 Sep-14 Oct-14 Nov-14 Dec-14 Total DH DH Runtime Energy (Hrs) (kWh) 0.0 0.0 0.0 0.0 413.5 124.1 693.3 208.0 625.9 187.8 466.6 140.0 351.5 123.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 232.2 81.3 500.8 150.2 592.3 177.7 739.0 221.7 538.8 161.7 298.0 104.3 0.0 0.0 0.0 0.0 2,783.2 864.1 HPWH Runtime (Hrs) 167.3 282.1 228.4 181.8 205.8 176.0 165.2 210.0 250.0 191.5 191.7 245.2 194.0 268.2 182.7 257.3 257.1 147.7 111.3 109.0 146.3 2,507.8 HPWH Predicted DH Energy Reduction (kWh) (kWh) 97.0 182.9 139.4 14.7 108.2 11.7 128.9 13.3 101.7 11.4 97.9 12.4 133.5 200.4 120.5 117.5 155.6 125.5 167.0 20.2 112.7 11.8 177.2 16.6 155.4 16.6 277.2 9.5 294.5 8.4 290.0 418.3 1,596.1 83.7 Note: The highlighted months are months before the dehumidifier status sensor was installed 98 5.6.3 Impact of Recirculation Pump on System Performance On April 10, 2013 the distribution system at Site 1 was modified to include a Bell & Gossett ecorcirc pump (the same time the HPWH was installed). This recirculation pump includes a built-in time clock to initiate operation as well as a built-in temperature sensor to stop operation once return water at the pump has warmed to the desired set point (the setting was 85°F). The pump was installed near the tank and pulls water from supply lines at two remote locations: kitchen sink and half bath sink. Half inch PEX was used for the recirculation line (see Appendix A). The pump was scheduled operate at times when hot water use in this home was considered probable (i.e., 5:30 to 7:30 AM, 10:30 to 11:30 AM, and 3:30 to 5:30 PM each day, EST). All total, the recirculation pump is allowed to operate for up to 5 hours each day. However, the actual runtime was typically in the range of 2–6 minutes/day because of the pump’s controller sensed that the return water was already at the set point of 85F. Figure 81 is a shade plot that qualitatively shows when the pump operated. Each day is shown as a vertical stripe on the plot with shades of gray. Subsequent days are shown along the x-axis. Periods when the pump operates are shown with darker shades of gray. The shade plot shows that the pump always operates at the beginning of each of the three periods. Operation later in the period is intermittent. Figure 81. Shade Plot Showing Runtime of Recirculation Pump Recirc Pump 24 22 20 18 Hour of Day 16 14 12 10 8 6 4 2 0 April May 2013 Day (MAX/MIN = 2.33/ 0.00 ) 99 The evaluation from the Building America report (Henderson and Wade 2014) showed that the useful portion of the delivered hot water increased from 82% to 91% after the pump was installed. Assuming an average water use of 48 gallons per day this equates to reduction in water use of 4 gallons per day. The energy required by the HPWH to heat this saved water is about 0.4 kWh/day (assuming a conversion efficiency of 1.5 for the HPWH), and the standby losses for the installed HPWH with the pump operating was about 2 kWh/day. In contrast the same HPWH in the lab required 0.6 kWh/day to maintain the tank temperature with no water use. So recirculation pump operation reduces hot water use but increases standby losses. The net impact of these two factors is summarized below. Savings from reduced hot water use (4 gal/day less) 0.4 kWh/day Additional Standby losses (2 kWh/day minus 0.6 kWh/day) 1.4 kWh/day Net savings -1.0 kWh/day Operating of the recirculation pump did NOT result in net energy savings. Energy use increased by about one kWh per day. Before the HPWH was installed the indirect tank on the oil-fired boiler met the water heating load. Standby losses for the indirect tank resulted in an average boiler runtime of 9.4 minutes for each day with no water use. The fuel oil boiler nozzle and pressure resulted in a 0.89 gallon per hour rating. Assuming 0.89 gal/h x 140 MBtu/gal x 9.4/60 * 0.85 the thermal losses are 16.5 Btu/h on average. 5.7 Field Test Site 2 – Condensing Storage Tank At Site 2 a new AO Smith Vertex (GDHE-50) condensing storage tank water heater was installed near the location of the original water heater on May 21, 2013. At the same time a Taco SmartPlus® recirculation pump was installed on the supply line with the sensor downstream of the pump. A ½-in PEX return line was added from the supply line under the kitchen sink back to the cold water inlet to the water heater. The pump, combined with the return line, allowed the first 13 ft of supply piping towards the kitchen to stay at temperature in order to reduce hot water waste. The pump was set in the “Smart/Learn Mode,” where it ran based on the pattern established over the last 7 days of operation. In this Smart Mode, the pump runs in the Pulse Mode (running for 2.5 minutes out of every 10 minutes) for a 2-hour window centered around each draw recorded from one week (168 hours) ago. Figure 82 is a shade plot showing when the recirculation pump operated. Each day is shown as a vertical stripe on the plot. 15-minute intervals with no pump operation are shown as light gray. Periods with 2.5 minutes of operation are shown as medium gray. Darker periods have more runtime in the 15-minute interval. Since the hot water usage 100 pattern in the house was irregular, the pump controls did not settle into a consistent weekly pattern. The most consistent pattern may have been for few weeks in November. Figure 82. Shade Plot Showing When Recirculation Pump Operated Recirculation Pump Runtime 24 22 20 18 Hour of Day 16 14 12 10 8 6 4 2 0 Jun Jul Aug Sep Oct Nov Dec Nov Dec 2013 Day (MAX/MIN = 5.08/ 0.00 ) Figure 83. Plots of Daily Runtime for Recirculation Pump Runtime (min/day) 400 200 0 Jun Jul Aug Sep Oct 2013 2014 101 Figure 83 shows how the daily total runtime varied over the same period. The measured runtime for the pump was about 200 minutes/day on average (about 14% of the time). The “Smart/Learn Mode” reduced the runtime by only a modest amount compared to the “Pulse Mode” (which would have run the pump 25% of the time 24 hours/day). In contrast, the timer-controlled pump at Site 1 runs the pump only about 3 minutes/day in the 5-hour window when operation is enabled. Recirculation pump operation was disabled on December 2, 2013. Figure 84 compares the gas use verses hot water use for similar periods with and without the pump operating. The days shown in the plot all had incoming cold water temperatures between 51°F and 56°F. Operation of the recirculation pump (black data) showed increased thermal losses (gas use) compared to periods without the pumping operating (red data). The data in Table 31 show the y-offsets for the best fit lines to these two data sets. The operation of the recirculation pump increased losses by 5 MBtu/day, from 27 MBtu/day to 32 MBtu/day. In both cases standby losses were much higher than the 7 MBtu/day that had been measured in the laboratory. Figure 84. Impact of Recirculation Pump Operation on Water Heater Gas Use (when cold water is between 51 and 56°F) DHW2 - 05/21/13 to 05/25/14 200 Gas Use (MBtu/day) 150 100 Recirculation Pump Off 50 Laboratory Losses = 7 MBtu/day 0 0 50 100 150 Water Use (gal/day) 102 200 Table 31. Impact of Recirculation Pump Operation on Standby Losses Standby Losses (gas use no water use) Laboratory Measurements 7 MBtu/day Recirculation Pump Operating May 21 to December 2, 2103 32 MBtu/day No Recirculation Pump December 3, 2013 to May 25, 2014 27 Mbtu/day Figure 85 shows the measured conversion efficiency verses hot water use. The efficiency was 0.4 to 0.6 – which is much lower than the 0.86 that was measured in the laboratory for the standard water use profile. At least some of the scatter in the data is due to the changes in water temperatures across the year. Although other unknown thermal loss mechanisms may have also played a role given the much the much lower than expected conversion efficiency. Figure 85. Variation of Efficiency with Hot Water Use for Period With Recirculation Pump Off DHW2 - 05/21/13 to 05/25/14 1.0 Daily Conversion Efficiency (-) Laboratory EF is 0.86 @ 64 gal/day 0.8 0.6 Recirculation Pump Off 0.4 0.2 0 50 100 150 200 Water Use (gal/day) 103 250 300 5.8 Field Test Site 3 – Gas-Fired Condensing Tankless At Site 3 a tankless water heater (Rinnai RL75i) was installed to replace the conventional gas-fired tank on March 22, 2013. Details about the water heater and installation are given in Appendix A. The impact of this change on this household with two people is shown in the plots below. Figure 86 shows data for the pre-retrofit period with the conventional gas-fired tank as black, while data with the tankless unit (after March 22) are shown as red. Total water use changed only slightly; however, the number of hot water draws was reduced by more than 50% with the tankless unit. The minimum activation flow threshold of 0.4 gpm for the tankless unit (as well as the startup delay) caused the occupants to change their hot water use. The evaluation from the Building America Report (Henderson and Wade 2014) showed that the useful portion of the delivered hot water decreased from 90%–91% with the conventional tank to 84%–86% with the tankless unit. This 4-6% reduction in useful delivered hot water (about 1.7 gallons per day) was mostly due to the startup delay of the tankless unit (i.e., the time delay for burner activation). Figure 86. Comparing HW Use and Events for Conventional Tankless Systems Site 3 (excluding vacations) AVG = 34.5 AVG = 32.0 Water Use (gal/day) 120 100 80 60 40 20 0 31 7 14 21 28 4 11 18 25 4 11 18 25 1 8 15 22 29 6 13 20 27 3 10 17 24 1 8 15 22 January February March April May June Draw Events (no/day) AVG = 52.3 July AVG = 20.1 150 100 50 0 31 7 14 21 28 4 11 18 25 4 11 18 25 1 8 15 22 29 6 13 20 27 3 10 17 24 1 8 15 22 January February March April May 104 June July The conversion efficiency of the tankless was typically 0.75, just below the rated EF of 0.82. As expected the tankless unit has little or no standby losses, so the conversion efficiency is not strongly dependent on daily water use. Figure 87. Conversion Efficiency Versus Hot Water Use 03/22/13 to 04/02/15 1.0 Rated EF is 0.82 @ 64 gal/day Conversion Efficiency (-) 0.8 0.6 0.4 0.2 0.0 0 20 40 60 Hot Water Use (gal/day) 105 80 100 6 Conclusions and Lessons 6.1 Summary of Findings and Conclusions This study evaluated a wide array of issues related to the performance of water heaters in New York homes. The study looked at the performance of water heater products ranging from standard gas water heater tanks through high efficiency gas-fired options. It also looked at solar and heat pump options as an alternative to standard electric water heaters. We used laboratory testing to make comparisons between different systems and to discern the impact of the new water use profiles in the forthcoming DOE Test Procedure to determine the new Uniform Energy Factor (UEF). Because the water use pattern can have a significant impact on performance, we also measured hot water flow in several homes to understand the magnitude and timing of hot water use. Data were also collected to quantify hot water waste due to the distribution system in several homes. Field testing also provided the means to measure the performance of water heating systems under actual, in-situ conditions. 6.1.1 Impact of Draw Profile on Efficiency Residential water heaters are currently rated by the Energy Factor (EF) which is determined by a simulated use test (SUT) procedure that imposes a hot water draw pattern on the appliance and then measures the thermal energy output and energy input over a 24 hour cycle. One issue with the current procedure is the unrealistic water draw profile that included six large draws taken one hour apart for a total 64.2 gallons per day. After several years of rulemaking with the industry, DOE recently modified this procedure (July 11, 2014) to include more realistic water use patterns. The low, medium or high use patterns are used in the test procedure depending on the first hour rating (FHR) of unit. The updated test rating procedure determines a new descriptor known as the Uniform Energy Factor (UEF). We imposed the original (or current) six-draw use profile on the water heaters in the laboratory and then also imposed the proposed multi-event patterns from ASHRAE 118.2, which included low use (40 gallons per day), normal use (64.2 gallons per day) and high use (82.8 gallons per day). Generally we found that the standard gas-fired water heater (Gas STD) and the high efficiency power vented water heater (HE-PVNT) have conversion efficiencies that were very close to the rated EF. The conversion efficiency was only slightly affected by the more realistic normal draw profile. For the tankless condensing water heater (TANKLESS) we found a conversion efficiency slightly lower than its EF, or 0.90 compared to 0.94 EF. Going from six large water draws to the 12 smaller draws at the same daily usage level slightly lowered the conversion efficiency from 0.9 to 0.86. The lower use profile resulted in an even lower conversion efficiency (dropping from 0.86 to 0.81) and the high use profile resulted in a higher efficiency 106 (increasing fron 0.86 to 0.88). Therefore, the new UEF is likely to be more representative of actual performance for tankless water heaters. The large draws of the current EF procedure overstated actual efficiency. The high-efficiency, condensing gas-fired tank unit (HE-Cond) and the Hybrid unit (which is a tankless unit with a small internal storage tank) are both currently rated by thermal efficiency (TE) under a test intended for commercial water heaters. For both these units, the measured conversion efficiency was lower than the TE, as would be expected. Going forward these units will be rated under the new UEF descriptor. For HE-Cond unit the conversion efficiency was 0.86 compared to 0.96 TE. Field testing by the manufacturer had shown efficiencies of 0.81 for this unit (Adams 2008). For the HYBRID unit the conversion efficiency was 0.73 compared to 0.90 TE. The efficiency did vary considerably for the HYBRID unit depending on the water use profile. The conversion efficiency varied from 0.65 at low usage to 0.78 for high usage. The strong dependence on usage is even greater than for the tankless unit. The measured conversion efficiency of 2.53 for the HPWH in the laboratory was slightly higher than the 2.4 EF with conventional six draw profile. The warmer conditions in the lab (75°F) compared to the test procedure (68°F) contributed to the better-than-expected performance. The low use profile did result in a slightly lower conversion efficiency as would be expected. The high use profile caused the resistance elements to operate to recover from the large draws in the pattern. This lowered the overall conversion efficiency to 1.77, or by 25% compared to the normal use efficiency. 6.1.2 Side-by-Side Solar Testing Two solar systems were tested side-by-side in the laboratory. The first system was a conventional 120 gallon single tank unit (SOLAR) with an internal heat exchanger coil connected to pressurized glycol loop that ran to the solar collector on the roof. This system is one of the most common solar products sold in New York State. The second system was a new glycol drain-back system (SOLAR-Drain) designed to provide the widely-recognized performance benefits of drain-back systems to a cold climate application. This two tank system included a 92 gallon solar pre-heat tank with internal heat exchanger that could hold the entire charge of glycol when the collector pump was off. The single tank conventional system had an OG-300 Solar Energy Factor (SEF) of 3.2. The expected annual Solar Fraction (SF) from SRCC for Syracuse was expected to be 0.56. We measured a solar fraction of 0.47 for the year, which generally in-line with expectations. The drain-back system initially had performance problems where it would vapor-lock and stop operating on sunny days. Once this problem was corrected the system behaved as expected, and we saw slightly better performance for the drain-back system on partially sunny days. However, the improved performance at part load conditions did not translate into an overall improvement compared to the baseline solar system. The annual solar fraction for the drainback system was just slightly less than the baseline one-tank system at 0.46, in spite of the expected performance benefit of having two tanks. 107 6.1.3 Hot Water Use Patterns in Test Homes We measured hot water use in 18 single family homes around Syracuse. The median water use for all the homes was 45 gal/day with an average occupancy of 2.7 people per household. The median for the sample of 2-person households was 39 gal/day, which is in-line with larger national studies such as Parker (2013) which estimates 38 gal/day and a study in the Pacific Northwest (Larson 2015) that found 34 gal/day. The median for the 4-person households was 66 gal/day compared to 63 gal/day nationally (Parker 2013) and 56 gal/day for the Northwest (Larson 2015). Hot water use in a given household varies significantly from day to day. For instance, for the 2-person households the standard deviation of water use within each home ranged from 8 to 23 gal/day, compared to a median of 39 gal/day. So peak water use is often 2 to 3 times median water use. We also noted seasonal variations in water use, presumably as the inlet water temperature changed. The houses on public water supply systems – where water pipes are often close to ground level – showed much more variation for the inlet water temperature across the year. Inlet water temperatures typically ranged from 38°F to 70°F across the year. For rural houses on wells the inlet temperature varied much less (48°F to 60°F). The degree of seasonal water use variation for the 2-person households was much smaller than for the 4-person households. This is mostly likely due to the greater importance of showers in mix of water use activities for households with more people. During a shower, occupants clearly mix in more hot water in the winter months to achieve the desired outlet temperature at the showerhead. For other water uses, the volume of hot water may be less sensitive to cold water temperatures. We developed average profiles for water use based on the 15-minute data. The average profiles showed a use pattern that is biased towards morning use for the 2-person household. For the 4-person households the profile was more evenly divided between morning and evening use – perhaps because the occupants modify their behavior and schedule to accommodate the needs of the entire household. At 13 of the test homes we also collected detailed data about each water use event. Water use patterns are more realistically represented as a series of distinct draw events across a day instead of the continuous daily profiles determined from the 15-minute data. The size and timing of draw events are what affect system performance (i.e. large draws can cause resistance element operation for the HPWH). While there is significant variation between sites we found that the average draw event was about one gallon – so a house that uses 50 gallons per day will typically have 50 draw events across the day. 108 6.1.4 Disaggregating Hot Water Use and Estimating Hot Water Waste At five of the field test sites we installed temperature sensors on the distribution piping near each fixture and on some trunk lines to allocate water draws to each end use and to estimate the amount of hot water waste. This analysis technique was only able to classify about half of the draw events across the five sites. However, it was able to account for 95% of hot water use at the sites. The large number of unclassified events was typically very small draws. Using the temperature sensors on the pipe surface near each fixture, we were able to estimate the amount of unusable previously-heated water that was run down the drain before useful hot water reached each fixture. We selected a threshold temperature of 90°F at the pipe surface to correspond to an acceptable hot water temperature at the fixture. Using these criteria we found that from 9% to 25% of the hot use at each site was associated with hot water waste – i.e., previously-heated water that is run down the drain waiting for an acceptable temperature at the fixture. This matches well to the estimated waste of 2 gallons per day per occupant from Parker (2013), which equates to about 11% hot water waste. Hot water waste was found to be highest at kitchen and bathroom sinks and lowest for showers and washing machine draws. 6.1.5 HPWH Field Performance A HPWH was installed at Site 1 in a wet, unconditioned basement near a hot water boiler. The HPWH, which was the same as the laboratory test unit, was found to have an overall annual conversion efficiency of 1.4 while operating in the hybrid mode. Resistance element operation on days with large water use events (e.g., draws over 20 gallons) resulted in the lower efficiency. The controls on the HPWH unit required full recovery of tank temperature with the resistance element. Cold air temperatures in the basement (50-65°F) also reduced efficiency. The HPWH unit operated in the resistance-only mode for significant portion of the test period (due to a problem with compressor). This provided the opportunity to directly compare hybrid heat pump operation and resistanceonly operation for the same tank in the same distribution system. The efficiencies in these two modes were different by a factor of two, mainly because the configuration in this site resulted in a conversion of efficiency of the unit in the resistance mode of 0.67. While thermal standby losses from the HPWH were probably higher than for a conventional electric tank, this comparison still implies that the HPWH reduces electric use compared to a standard electric by nearly half. The HPWH operation had only a moderate impact on space conditions, lowering basement air temperatures by 24°F on average. Therefore, there was no discernible impact of HPWH operation on the heating load in the conditioned space above. The basement also had a dehumidifier that kept the basement below 60% RH in the summer. From the measured data we determined that each 5 hours of HPWH operation reduced dehumidifier 109 runtime by one hour, reducing dehumidifier energy use by about 84 kWh annually. The savings of $10 per year are slightly less than the $20 dehumidification benefit estimated by ACEEE (2011). 6.1.6 Impact of Switching to Tankless Unit At Site 3 a standard gas water heater was monitored for a few months and then replaced with a non-condensing tankless unit with an EF of 0.82. Installing the tankless unit did not significantly change the daily average water use of the household, which was about 34 gallons per day. However, it did change the number of hot water draw events. With the tankless unit the number of draws was reduced by more than half, from 54 to 20 draw events per day. The occupants adjusted their behavior presumably because small draws no longer provided hot water at the desired temperature because of the time delays associated with burner startup in the tankless unit. On average the conversion efficiency was about 0.75 at 64 gallons per day, slightly below the rated EF. 6.1.7 Field Performance of High Efficiency Condensing Tank At Site 2 we installed the same condensing storage tank that was installed in the laboratory. The condensing storage tank had much lower efficiency then was measured in the laboratory. The measured conversion efficiency of 0.5 at 64 gallons per day compared to 0.86 in the laboratory. Part of the poor performance was due the use of a recirculation pump at this site. The recirculation pump reduced hot water waste but greatly increased thermal standby losses from this system. 6.1.8 Recirculation Pumps to Reduce Hot Water Waste At two field test sites, we installed different types of recirculation pumps along with a return line back to the tank inlet. The pumps used slightly different control methods to keep the main supply trunk primed with hot water to reduce wait times and hot water waste. At both sites the pumps reduced hot water waste but had an even greater impact on standby losses. Hot water waste was reduced by about 4 gallons per day at Site 1 due to pump operation, but standby losses were increased by more than the savings from eliminating this waste. At Site 1 we calculated a net increase in energy use of 1 kWh per day. Recirculating water clearly increases thermal losses from the supply and return piping near the tank; so while water use is lower, energy use increases. Therefore in regions like the Northeast where energy savings are of more concern with than water conservation, recirculation pumps do not seem to be justified. 6.2 Lessons Learned 6.2.1 One Water Use Profile May Not Fully Characterize Performance The new simulated use test procedure to determine the UEF rightly selects an appropriate usage profile (low, medium or high) based on the first hour rating (FHR) or “size” of the water heater. However, measured field data 110 show that water use in a given house can vary significantly from day to day as the occupants engage in different activities. Therefore, appliances such as the HPWH will have efficiencies approaching the UEF on days when usage in near normal, but much lower efficiency on high use days when the resistance element is engaged. In this respect, the new test procedure still may fall short of representing actual efficiency. 6.2.2 Controls and Tank Size Matter for HPWH The performance of the HPWH we tested in laboratory and field demonstrated the importance of control in providing efficient operation. In the hybrid mode, the unit controls put priority on using the resistance elements to provide a rapid recovery after a large draw. Obviously, this control strategy is important in achieving the first hour rating (FHR) for the unit. Control approaches that consider time of day and others factors when deciding when and how much to use the resistance elements versus the heat pump would greatly impact actual efficiency. Evaluations at NREL (Sparn et al. 2014) have highlighted the benefit of improved control strategies on HPWH efficiency. Many manufacturers are now on their second and third generation of HPWH products. A NYSERDA-sponsored field test of different first and second generation HPWH units in Delaware County is expected to show the improvements in performance for different generations of these products (Ealey 2015). In addition to controls, many manufacturers now have units with larger storage tanks to minimize the chance of element operation during a large draw. For instance General Electric now offers both a 50 gallon and an 80 gallon version of their HPWH. 6.2.3 HPWH is an Energy Efficient Option in Rural Homes There are 1.2 million New York homes that use electric resistance water heaters. Another 1.3 million homes use oil for water heating. Several hundred thousand of these households are rural and suburban single family homes with basements which are good candidates for a HPWH installation. The HPWH offers significant savings compared to electric and even offer savings compared to oil-fired water heating options. These units are now competitively priced at big box stores, implying a strong do-it-yourself market is developing for these relatively easy-to-install units. 111 7 References ACEEE. 2011. Emerging Hot Water Technologies and Practices for Energy Efficiency as of 2011. Report A112. American Council for an Energy Efficient Economy. Washington, DC. Prepared October 2011. Revised February 2012. Adams, C. 2008. “A. O. Smith Vertex Condensing Tank-type Water Heater.” ACEEE Hot Water Forum Sacramento. June 3. AHRI. 2011. Directory of Certified Product Performance. 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