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Frank ANSYS Flashing Condensation b

Simulation of Flashing and Steam Condensation in Subcooled Liquid using ANSYS CFX. Thomas Frank ANSYS Germany, 83624 Otterfing 2006 ANSYS , Inc. All rights reserved. ANSYS , Inc. Proprietary Contents Introduction CFX real fluid properties Redlich-Kwong EOS. IAPWS-IF97 standard for water & steam The CFX thermal phase change model Validation: The Edwards test Steam Condensation in sub-cooled liquid Summary & Outlook 2006 ANSYS Inc. Th. Frank : Simulation of Flashing and Steam Condensation Slide 2. All rights reserved. 5th FZD & ANSYS MPF Workshop, April 2007, Dresden, Germany ANSYS , Inc. Proprietary Introduction Typical applications : NRS accident scenarios ( SBLOCA, LBLOCA, PTS). Depressurization of superheated fluids ( Flashing ). BWR fuel assemblies (boiling). Steam recondensation in containments Chemical reactor safety . 2006 ANSYS Inc.

© 2006 ANSYS, Inc. All rights reserved. ANSYS, Inc. Proprietary Simulation of Flashing and Steam Condensation in Subcooled Liquid using ANSYS CFX

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Transcription of Frank ANSYS Flashing Condensation b

1 Simulation of Flashing and Steam Condensation in Subcooled Liquid using ANSYS CFX. Thomas Frank ANSYS Germany, 83624 Otterfing 2006 ANSYS , Inc. All rights reserved. ANSYS , Inc. Proprietary Contents Introduction CFX real fluid properties Redlich-Kwong EOS. IAPWS-IF97 standard for water & steam The CFX thermal phase change model Validation: The Edwards test Steam Condensation in sub-cooled liquid Summary & Outlook 2006 ANSYS Inc. Th. Frank : Simulation of Flashing and Steam Condensation Slide 2. All rights reserved. 5th FZD & ANSYS MPF Workshop, April 2007, Dresden, Germany ANSYS , Inc. Proprietary Introduction Typical applications : NRS accident scenarios ( SBLOCA, LBLOCA, PTS). Depressurization of superheated fluids ( Flashing ). BWR fuel assemblies (boiling). Steam recondensation in containments Chemical reactor safety . 2006 ANSYS Inc.

2 Th. Frank : Simulation of Flashing and Steam Condensation Slide 3. All rights reserved. 5th FZD & ANSYS MPF Workshop, April 2007, Dresden, Germany ANSYS , Inc. Proprietary Material Properties: EOS. Changes over wide range of (T,p). fluid properties depend on thermodynamic state Equation of state (EOS) types in CFX: Ideal gas law Tabulated data; Real gas property (RGP) tables Redlich-Kwong EOS. User defined equation of state (CCL, CEL). User defined materials and material properties large degree of customizability 2006 ANSYS Inc. Th. Frank : Simulation of Flashing and Steam Condensation Slide 4. All rights reserved. 5th FZD & ANSYS MPF Workshop, April 2007, Dresden, Germany ANSYS , Inc. Proprietary Material Properties: IAPWS Properties of Water and Steam : IAPWS-IF97 equation-of-state implemented Reference: W. Wagner, A. Kruse: The Industrial Standard IAPWS-IF97: Properties of Water and Steam , Springer, Berlin, 1998.

3 1. subcooled water 2. supercritical water/steam 3. superheated steam 4. saturation data 5. high temperature steam (currently not yet implemented in CFX). 2006 ANSYS Inc. Th. Frank : Simulation of Flashing and Steam Condensation Slide 5. All rights reserved. 5th FZD & ANSYS MPF Workshop, April 2007, Dresden, Germany ANSYS , Inc. Proprietary Material Properties: IAPWS Properties of Water and Steam Water & steam selectable from IAPWS database specify (T,p) range CFX internal use of tabulated values for speed of computation Definition of Homogeneous Binary Mixture Water & Steam . phase pair related properties container' for Tsat=Tsat(p) and = (T). 2006 ANSYS Inc. Th. Frank : Simulation of Flashing and Steam Condensation Slide 6. All rights reserved. 5th FZD & ANSYS MPF Workshop, April 2007, Dresden, Germany ANSYS , Inc. Proprietary Thermal Phase Change Model.

4 Bulk Condensation & Evaporation Interfacial mass transfer =. Mass transfer rate per unit area lv = m lv A lv Interfacial area/unit volume Swarm of rising vapor Volume V. bubbles. Vapor inside is at dP. saturation temperature Interfacial area N p Ap ,lv Surrounding liquid at temperature Tl N pV p r . V. N p Ap ,lv V p Ap ,lv 6r . Area density: Alv = = r =. V Vp Vp dP. Condensation /Evaporation rate = hlv (Tl Ts ) / L Alv hlv = l Nulv / d P. Heat transfer coefficient from Ranz-Marshall correlation (further available: heat transfer coeff., Nusselt number, Hughmark correlation). 2006 ANSYS Inc. Th. Frank : Simulation of Flashing and Steam Condensation Slide 7. All rights reserved. 5th FZD & ANSYS MPF Workshop, April 2007, Dresden, Germany ANSYS , Inc. Proprietary Validation: The Edwards Test Edwards Test well known test case in nuclear reactor thermohydraulics Used for validation of many 1-d/system & CFD.

5 Codes, RELAP-5, ATHLET, SERAPHIM, etc. Experimental data available: Edwards , O'Brien : Studies of phenomena connected with the depressurization of water reactors , J. Br. Nucl. Energy Soc., Vol. 9, pp. 125-135 (1970). Takata T., Yamaguchi A.: Numerical approach to the safety evaluation of Sodium-water reaction , J. Nucl. Science &. Technology, Vol. 40, No. 10, pp. 708-718 (2003). 2006 ANSYS Inc. Th. Frank : Simulation of Flashing and Steam Condensation Slide 8. All rights reserved. 5th FZD & ANSYS MPF Workshop, April 2007, Dresden, Germany ANSYS , Inc. Proprietary Validation: The Edwards Test pressurized pipe section, 7 Mpa, 502 K. measurement location burst disc free outlet Pressurized pipe section ( long) initially filled with water; 2m long pipe under atmospheric pressure p = 7 MPa TWater = 502 K. LPipe = m DPipe = m Pressurized pipe closed with a burst disc, broken at t= Comparison of pressure & volume fraction over time at the measurement location at x= m from the left pipe wall 2006 ANSYS Inc.

6 Th. Frank : Simulation of Flashing and Steam Condensation Slide 9. All rights reserved. 5th FZD & ANSYS MPF Workshop, April 2007, Dresden, Germany ANSYS , Inc. Proprietary Edwards Test Flow Setup Physical setup: 1d setup, 400 & 1000 grid cells (hexahedra). Pressurized pipe section: filled with water and water steam p=7 MPa, TWater=TSteam=502 K (saturation temperature). Pipe section under atmospheric pressure: filled entirely with water steam p=1 atm, TSteam=373 K. Eulerian two-phase flow simulation assumed bubble diameter : dbubble=1mm Laminar (no turbulence model). Two-resistance interfacial heat transfer model Water Ranz-Marshall Water Steam zero resistance Thermal Phase Change Model 2006 ANSYS Inc. Th. Frank : Simulation of Flashing and Steam Condensation Slide 10. All rights reserved. 5th FZD & ANSYS MPF Workshop, April 2007, Dresden, Germany ANSYS , Inc.

7 Proprietary Edwards Test Flow Setup (cont.). Physical setup (cont.): Water & Water Steam properties Case Water Water Steam 1) Redlich-Kwong EOS incompressible, Redlich-Kwong EOS, const. fluid high pressure cond. properties (1-30 MPa, 450-900 K). 2) IAPWS-IF97 compressible compressible, MPa, MPa, 373-600 K 373-600 K. Upwind advection scheme Transient simulation, 2nd order backward Euler time integration [ , ], 15, ,35 coeff. loops Adaptive time step control t . Convergence criteria: Max. Residuals < 2006 ANSYS Inc. Th. Frank : Simulation of Flashing and Steam Condensation Slide 11. All rights reserved. 5th FZD & ANSYS MPF Workshop, April 2007, Dresden, Germany ANSYS , Inc. Proprietary Edwards Test CFX Convergence History Difficult convergence, due to sudden evaporation ( Flashing ). Improved with 500 table entries in IAPWS-IF97 property tables 2006 ANSYS Inc.

8 Th. Frank : Simulation of Flashing and Steam Condensation Slide 12. All rights reserved. 5th FZD & ANSYS MPF Workshop, April 2007, Dresden, Germany ANSYS , Inc. Proprietary Edwards Test Pressure Wave Propagation Pressure wave propagation in 1d geometry of Edwards pipe Further rise of pressure level due to evaporation 2006 ANSYS Inc. Th. Frank : Simulation of Flashing and Steam Condensation Slide 13. All rights reserved. 5th FZD & ANSYS MPF Workshop, April 2007, Dresden, Germany ANSYS , Inc. Proprietary Edwards Test Steam Volume Fraction Distribution Evaporation starts first at burst disc location Further evaporation after reflection of the pressure wave from left end of the Edwards pipe 2006 ANSYS Inc. Th. Frank : Simulation of Flashing and Steam Condensation Slide 14. All rights reserved. 5th FZD & ANSYS MPF Workshop, April 2007, Dresden, Germany ANSYS , Inc.

9 Proprietary Edwards Test Pressure at Measurement Location qualitatively good agreement for the difficult physics pressure wave propagation velocity in good agreement with Takata experiment; pressure drop slightly overpredicted Experiment Experiment (Takata). RELAP5, Mod 2. RELAP5, Mod 3. Pressure [MPa]. SERAPHIM (Takata, 3d/1d). (Redlich-Kwong). (IAPWS-IF97). 0 10 20 30 40 50. Time [ms]. 2006 ANSYS Inc. Th. Frank : Simulation of Flashing and Steam Condensation Slide 15. All rights reserved. 5th FZD & ANSYS MPF Workshop, April 2007, Dresden, Germany ANSYS , Inc. Proprietary Edwards Test Full Pressure Transient T=550ms pressure transient at measurement location x= good agreement to Takata experiment Experiment Experiment (Takata). RELAP5, Mod 2. RELAP5, Mod 3. Pressure [MPa]. SERAPHIM (Takata, 3d/1d). (Redlich-Kwong). (IAPWS-IF97).

10 0 50 100 150 200 250 300 350 400 450 500 550 600. Time [ms]. 2006 ANSYS Inc. Th. Frank : Simulation of Flashing and Steam Condensation Slide 16. All rights reserved. 5th FZD & ANSYS MPF Workshop, April 2007, Dresden, Germany ANSYS , Inc. Proprietary Edwards Test Steam VF at Measurement Location steam volume fraction transient at measurement location x= good agreement to Takata experiment Air Volume Fraction [-]. Experiment (Takata). SERAPHIM (Takata, 3d/1d). (Redlich-Kwong). (IAPWS-IF97). 0 50 100 150 200 250 300 350 400 450 500 550 600. Time [ms]. 2006 ANSYS Inc. Th. Frank : Simulation of Flashing and Steam Condensation Slide 17. All rights reserved. 5th FZD & ANSYS MPF Workshop, April 2007, Dresden, Germany ANSYS , Inc. Proprietary Edwards Test Parameter Variation for Initialisation Parameter variation wrt. initial value of vapor void fraction in pressurized pipe section and assumed bubble diameter Simulations performed for the first 50ms only Experiment Experiment (Takata).


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