Dr.Ing. Program “Multiphase Transport” Institutt for energi- og prosessteknikk Ole.J.Nydal@ntnu.no • • • NFR project 144036/211 (KMB) Participants (2003) – NFR, Shell, Statoil, Total – NTNU, Dept. Energy and Process Engineering – Laboratories at IFE and SINTEF Initially 4 doctorals, currently 6 OG seminar 10-11 March 2004, Trondheim Research challenges in multiphase transport • • • Computational tools – Flow capacity of pipelines; pressure drop and holdup – Dynamics: Unstable flow, transient operations Fluid related effects – Solid deposits (gas hydrates, wax, scale, sand) and corrosion Equipment Stigerør – Separation, boosting, metering, control Transport ledninger Brønner OG seminar 10-11 March 2004, Trondheim Computational tools: Background • Successful Norwegian R&D on computational tools: – SINTEF: Two Phase Flow Laboratory established in 1983 – IFE: Transient flow model 1980: OLGA prototype – A series of collaboration projects has resulted in OLGA becoming international industry standard for transient simulations. Commercialized by Scandpower • Further tendencies: – Towards 3D simulation – Integrated flow assurance models: wells / pipe networks / fluid / process / control OG seminar 10-11 March 2004, Trondheim PhD program: Objectives • Provide candidates with expert knowledge on multiphase pipe flow • Provide results which are relevant and useful for the industry – Experimental data for model verification – Flow models which can be implemented in industrial simulators • Make use of multiphase flow laboratories at SINTEF and IFE for fundamental studies – Communication between multiphase laboratories OG seminar 10-11 March 2004, Trondheim Organization • • • • • Coordinator: Ole Jørgen Nydal Open ended structure: Companies participate with PhD candidates NFR: candidates or support for extended experimental work 2 meetings/year (often at company offices) All multiphase activities are reported into the program (20 persons 2003) – Doctorals, Post.Doc. students, visitors 2001 Person Olav Kristiansen Transition Trygve Wangensteen Model Monika Johansen Slug flow George W. Johnson Waves Fabien Renault Initiation Jørn Kjølaas Plug NFR project OG seminar 10-11 March 2004, Trondheim 2002 2003 2004 2005 Activities • • • • Important with a combination of experiments and modeling Experiments – SINTEF , IFE laboratories can provide data for model tuning – NTNU lab can provide data on transients Flow modelling – Mathematical formulation – Numerical methods – Methods of implementation Current focus on transient aspects – Gas-oil-water flows OG seminar 10-11 March 2004, Trondheim Flerfase laboratorier i Trondheim Mellomstor loop SINTEF Stor loop SINTEF Mikro loop (CO2) OG seminar 10-11 March 2004, Trondheim Mini loop til forelesninger Liten loop EPT Multiphase flow laboratory • • • Flow of oil-water-air mixtures in pipes • Flow regimes • Pressure drop and phase fractions • Transients: Unstable flows, pigging, riser slugging Mini-loop for demonstration / education NetLab: Internet access to laboratory • Remote demonstrations, flow studies, courses Oil-water-air, atmospheric pressure 3, 6 cm. I.D., 14 m length, +- 15 deg. 6 m high, L- and S shaped • More information http://www.ept.ntnu.no/Multiphase Ole Jørgen Nydal, NTNU Tlf: 73550564 Fax: 73593859 Ole.J.Nydal@ntnu.no OG seminar 10-11 March 2004, Trondheim Liquid flows 0.02 - 2 m/s Air 0.5 – 30 m/s Pigging, gas lift, reservoir inlet Instrumentation: Flow rates, pressure drop, holdup Manual and automated control Student laboratory NTNU OG seminar 10-11 March 2004, Trondheim NetLab Multiphase flow laboratory on internet • • • • Operate multiphase flow laboratory from internet • Control video camera • Control pumps and valves • Monitor flow in pipe • Record flow rates, pressure and holdup Remote access applications • Demonstrations • Courses • Flow studies Flow examples • Flow of gas-liquid, oil-water, gas-oilwater • Flow regimes • Transients Collaboration • Cyberlab A/S • HiST OG seminar 10-11 March 2004, Trondheim Examples on experiments • • • • • • • • • • Two and three phase flow in S-shaped riser. Stability maps and slug characteristics Pigging in S-riser and straight pipe: start-up and flowing conditions V-shaped geometry: Stop-restart experiments Stratified-slug transition: hysteresis and effect of pressure Low liquid loading experiments: three phase flow Flow with vanishing liquid on the wall: horizontal and vertical Rising bubbles in large diameter vertical pipes (20, 40 cm) Bubble velocity in oil-water flow Oil-water flow in undulating pipes Oil-water flow in gas lifted wells: flow instabilities OG seminar 10-11 March 2004, Trondheim Multiphase Transport: Research tasks • Olav: Effect of pressure on the transition to slug flow (SINTEF lab) – Field problem: occurrence of initial large slug • Fabien: Transition models – Flow regime transition criteria, slug initiation modeling • Monika: Experiments on three phase slug flow – Bubble propagation in oil-water systems • Trygve: Three phase flow models – Slug tracking with water • George: Transitional regime between stratified and slug flow – Experiments and flow modeling • Jørn: Pipeline plugged with gas hydrates – Computational methods for hydrate plug dynamics OG seminar 10-11 March 2004, Trondheim Transient pipe flow modelling • All regimes can be present in a pipeline – Both compressible and incompressible flows • Classical modelling – Pipeline divided into numerical grid – Conservation equations solved with specific closure laws for each regime (two fluid or drift flux formulation) • Slug tracking modelling – Pipeline divided into parts with liquid (slugs) and gas (bubbles) – Incompressible models for liquid parts – Compressible models for gas parts – Object oriented implementation OG seminar 10-11 March 2004, Trondheim Control volumes • General model: Slug capture if grid is much smaller than slugs • OLGA: Sub grid tracking P, H P, H • Petra: Adaptiv and moving grid on front P, H • Um P, H Ug,Ul Sluggit: Grid = slugs and bubbles P, H OG seminar 10-11 March 2004, Trondheim Ul P, H Terrain slugging in S-riser Inlet pressure 0.8 P (b a r) 0.6 G eo metry used in the com putations 0.4 G eo metry of the experimental loop 0.2 0 0 50 100 150 200 250 300 350 400 450 300 350 400 450 300 350 400 450 Holdup probe trace at the end of the first riser 0 0 50 100 150 200 250 Holdup probe trace at the outlet 0 0 50 100 150 200 250 Pressure drop in the first pipe 0.3 Experiments 1.8 x 10 5 Inlet pressure P (Pa) 1.6 1.4 1.2 1 0 50 100 150 200 250 300 350 400 450 300 350 400 450 300 350 400 450 Holdup at the end of the first riser 1 H (-) 0.8 0.6 0.4 0.2 0 0 50 100 150 200 250 Holdup at the outlet 1 H (-) 0.8 0.6 0.4 0.2 0 0 50 100 150 Slug tracking OG seminar 10-11 March 2004, Trondheim 200 250 simulations Conclusion • • • A PhD project on Multiphase Transport has been established, with important support from NFR The project has grown 50% during the project period The project extends beyond the NFR project period, as long as it maintains industry interest The project supplies the industry with – Experts within multiphase transport – Support for model improvements: Experimental data and prototype flow models • Further development of the program – Incorporate other aspects of flow assurance OG seminar 10-11 March 2004, Trondheim