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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 1/21 Florent Jomard Commissariat à l’Énergie Atomique DEN/DTEC/STCF/LGCI Site de Marcoule BP 17171 30207 Bagnols sur Cèze, France Jean-Pierre Feraud Commissariat à l’Énergie Atomique DEN/DTEC/STCF/LGCI Site de Marcoule BP 17171 30207 Bagnols sur Cèze, France Jacques Morandini Astek Rhone-Alpes 1 place du Verseau 38130 Echirolles, France Yves Du Terrail Couvat Laboratoire EPM, Madylam 1340 Rue de la Piscine Domaine Universitaire 38400 Saint Martin d’Hères, France Jean-Pierre Caire LEPMI, ENSEEG 1130 Rue de la Piscine 38402 Saint Martin d’Hères, France MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 2/21 I.Introduction II.The Westinghouse sulfur cycle III.Modeling aim IV.Coupling of physical phenomena with Fluent ® / Flux Expert ® codes V.Electrolyzer modeling, boundary conditions VI.Software coupling results VII.Conclusion, future prospect
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 3/21 Global warming context requires decreasing world's greenhouse gas emission I. Introduction hydrogen alternative solution to replace primary energy Exemple : Hydrogen + fuel cells can replace internal combustion engines CEA / PSA Fuel cells : GENEPAC ( GENérateur Electrique de Pile A Combustible) PSA hydrogen concept car ( 207 ePure)
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 4/21 wide uses of energy = hydrogen mass production High temperature cycles for hydrogen production - 100% thermochemical : Bunsen Cycle… - hybride cycle (Westinghouse sulfur cycle, Deacon cycle…) - 100% electrochemical cycle (high temperature electrolysis of water) I. Introduction High temperature hydrogen production technologies could be provided by using : - Gen. IV Nuclear power plants - Thermal solar facilities…
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 5/21 H 2, product ½ O 2 by product II. The Westinghouse sulfur cycle Hybrid Sulfur Process block H 2 O feed Thermal energy Filter press Electrolyzer (50 – 100°C) Concentration Évaporation Décomposition Absorption 300°C Concentration 300°C Thermal Decomposition 850°C Evaporation 600°C Thermal energy H 2 O + SO 2 + ½ O 2 H 2 SO 4 Electrical energy Compression H 2 SO 4 part SO 2 part H 2 SO 4 SO 2 Cooling SO 2 H 2 O SO 2 H 2 O SO 2 H 2 O Absorption 25°C Westinghouse sulfur cycle
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 6/21 Process working conditions - -T°C : 50 - 100°C - - [H 2 SO 4 ] : 20 - 60 % weight - - PSO 2 1 bar - Current density 200 mA/cm² H+H+ H+H+ H+H+ H+H+ H+H+ H+H+ H+H+ H+H+ H+H+ e-e- II. The Westinghouse sulfur cycle membrane Two compartment membrane electolysis cell : Anode + + Cathode - - SO 2 2 H H 2 2 4 4 H H + + H H 2 2 Anolyte : H 2 O-SO 2 - H 2 SO 4 Catholyte: H 2 O – H 2 SO 4 SO 2 + 2H 2 O H 2 SO 4 + 2H + + 2e - 2H + + 2e - H 2
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 7/21 Within the framework of the Westinghouse cycle studies The aim of our works consists of modeling a filter press electrolyzer for hydrogen production. III. Modeling aim Our studies have to take into account numerous physical interactions : - electrokinetic (overpotential), - thermal behaviour (Joule effect), - fluid dynamics (forced convection), - multiphasic flow (electrolyte + bubble plume). We expect that the virtual filter press design will work as a real one
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 8/21 IV. Coupling of physical phenomena with Fluent® / Flux Expert® codes Physical phenomena : - Thermohydraulics (Fluent, finite volume method) Navier-Stokes continuity equations Heat transfert equation - CFD, Fluent model selected - k-ε turbulence model so-called « realizable » - diphasic flow description : Euler-Euler - separate phase : disperse phases momentum Diphasic fluid dynamic (1) (2)
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 9/21 IV. Coupling of physical phenomena with Fluent® / Flux Expert® codes Physical phenomena (continuation) : - Electrokinetics (Flux-Expert, finite element method) Charge Balance, Laplace equation : Ohm's Law, primary current distribution (a): Secondary current distribution, Butler-Volmer's Law (b) : Electrode Electrolyte (j) Potential (V) Cell width (a) Interface gap (1) (2) (b) (a)
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 10/21 IV. Coupling of physical phenomena with Fluent® / Flux Expert® codes Software coupling : Fluent ® –Flux Expert ® coupling flowchart = message-passing function physical phenomena can be solved by using different meshes (structured or unstructured) Communication between the two codes : simple and robust message- passing library algorithms developed are mainly location and interpolation algorithms
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 11/21 FLUENT ® Solve the two phase Thermohydraulic problem Calculation of Temp. (K) in all the domain u (flow velocity) α g ( hydrogen concentration) FLUX EXPERT ® Solve the Electrokinetic problem Calculation of U : Potential (V) J : current densities (A.m -2 ) Qs/Qv : Thermal Joule effect ( W.m -3 ) Thermal and current densities inputs hydrogen concentration Temperature IV. Coupling of physical phenomena with Fluent ® / Flux Expert ® codes
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 12/21 V. Electrolyzer modeling, boundary conditions : The FM01-LC laboratory scale electrolyzer : 0.16m 0.04m 0.013m H + +H 2 SO 4 H 2 SO 4 + SO 2 H 2 SO 4 + SO 2 H 2 SO 4 H2H2 + - z x y Electrolyzer operating principle With : cathode, hydrogen release area, catholyte, membrane, anolyte,. anode.
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 13/21 V. Electrolyzer modeling, boundary conditions CATHOLYTE CATHODE membran ANOLYTE ANODE Overpotential Area 0 V Y (mm) Overpotential Area Z (mm) 2000 A.m -2 CATHOLYTE CATHODE membrane ANOLYTE ANODE Flux-Expert Hydrogen bubbles velocity : 0.01m.s -1 bubble emission angle : 45° Electrolyte uniform velocity profile , ,k,c p : temperature dependent No thermal exchange with outside Hydrogen area 160 mm V= 0.07m.s -1 T=323K CATHOLYTE CATHODE membrane ANOLYTE ANODE 0 1.5 6.5 6.6 11.2 13 mm Fluent Boundary conditions to produce 5 Nl.h -1 of hydrogen
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 14/21 123 VI. Numerical results Residuals continuity u residual sulphuric acid u residual hydrogen v residual sulphuric acid v residual hydrogen w residual sulphuric acid w residual hydrogen T 1 residual sulphuric acid T 2 residual hydrogen K residual sulphuric acid residual sulphuric acid (1–K) residual hydrogen FLUENT iterations Code Coupling Behavior Interaction between the two codes is demonstrated by the convergence of the computational residuals with successive iterations FLUX-EXPERT iterations
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 15/21 T =323 K υ = 0.069 m.s -1 T =323 K υ = 0.069 m.s - 1 0.16 m 0 m VI. Numerical results Thermal problem : Graded colors scale Temp. (K)
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 16/21 3 mm VI. Numerical results Catholyte Cathode % H 2 (vol.) Cathode Anode membrane Hydrogen plume area approx. 1 mm Diphasic problem resolution : Hydrogen volume fraction < 72% Maximum concentation at 0.2 mm from cathode
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 17/21 VI. Numerical results % H 2 (vol.) Cathode Anode Graded colors scale height = 0.15m height = 0.08m height = 0.01m Diphasic problem resolution :
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 18/21 Anolyte VI. Numerical results Fluid dynamic calculation : Anolyte flow appearance: Flat (uniform velocity) + wall effect on membrane and anode sides Caracteristic of turbulent flow Catholyte flow appearance : Wall effect on membrane side, High velocity increasing on cathode side (X4) Characteristic of air lift effect Catholyte Flow m.s -1 membrane
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 19/21 Anodic overpotential = 70 % tension of cell Tension of cell : 0.73V Goal : Design a cell to obtain 0.6 V of total tension VI. Numerical results Electrokinetics calculation : V) Potential (V)
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 20/21 Modeling with Flux-Expert / Fluent Codes Performed with message-passing library Only 24h of calculation on Pentium IV(F. Expert) + Core 2 Duo (Fluent) PC CFD results Electrolyte rising temperature : 4°C Catholyte motion (x4), hydrogen bubbly effect Electrokinetics calculation Electrochemical irreversible process taken into account with Flux Expert® Total cell tension obtained : 0.73V (in accordance with literature results) VI. Conclusion, future prospect
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DEN/VRH/DTEC/STCF/LGCI JP FERAUD ICONE15, Nagoya 2007 April 22-26 MODELING A FILTER PRESS ELECTROLYZER FOR THE WESTINGHOUSE HYBRID CYCLE USING TWO COUPLED CODES ICONE15 -10639 21/21 VI. Conclusion, future prospect Calculation / Experiments Experiments required to complete the lack of anodic overpotential law Check Validity of diphasic flow behavior development of specific physical operators modelling a stack of cells before scaling-up Optimization of the future electrochemical process with a design of numerical experiments
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