Development of twophaseeulerfoam

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ISPRAS OPEN 2016 NUMERICAL STUDY OF SADDLE-SHAPED VOID FRACTION PROFILES EFFECT ON THERMAL HYDRAULIC PARAMETERS OF THE CHANNEL WITH TWO-PHASE FLOW USING OPENFOAM AND COMPARISON WITH EXPERIMENTS Varseev E.V. (Rosatom CICE&T) Kornienko Yu.N. (IPPE) Moscow, December 2016

Introduction Two- and multiphase flows with bubble structure is widely presented in traditional and nuclear power industry, in chemical and technological production, pipeline transport of hydrocarbons, metallurgical and other equipment. Regimes of normal operation for such systems are justified by experimental and numerical methods based on regulatory and reference data The models presented in the majority of the onedimensional codes not always adequately enough describe gas distribution via radius of the channel and don t take into account abnormal growth of friction at the wall of the channel, and for this reason they are in the process of active verification. Implementation of CFD codes for multiphase flow simulation with Euler-Euler approach allows to overcome shortcoming of the one-dimensional semiempirical codes. Kornienko Yu.N. Generalization of analytical integral forms of friction, heat and mass transfer coefficients for non-equilibrium two-phase flows. Annular channels and fuel assemblies. // Issues of atomic energy. Physics of nuclear reactors series, 2013. Issue.4. P. 61-76. (in Russian) 2

Purpose of the work The present work is dedicated to verification of numerical model in standard solver of open-source CFD code OpenFOAM for two-phase flow simulation twophaseeulerfoam, and to determination of the baseline model parameters. The investigation of heterogeneous distributions of non-equilibrium coolant flow, which leads to abnormal friction increase of the channel in two-phase adiabatic water-gas flows with low void fractions, presented There are a significant number of works in open literature, dedicated to two-phase flow modeling with CFD codes have the following distinctive features: - authors use modified solvers with two-phase models; - for verification they use international experimental data for void fraction distribution; - authors basically don t consider effects of abnormal friction increase On contrary, during this work authors used default OpenFOAM solver for velocities and void-fraction profiles calculation; the results of simulation were compared against Russian experimental data including comparison of friction at the wall. As a result the friction coefficient of channels walls were obtained in the wide range of gas flow ratio β. 3

Development of twophaseeulerfoam OpenFOAM 1.7.x (2010) twophaseeulerfoam Euler-Euler solver for turbulent two-phase flows Constant material properties Constant dispersed phase diameter No bubble specific drag models, turbulent dispersion or wall lubrication force No heat or mass transfer Hard coded k-eps turbulence model 2.1.0 (2011) Temperature base heat transfer solution, compressibility, non-unifrom diameter 2.1.1 (2012) Improved void fraction solution algorithm (MULES) 2.2.0 (2013) Support for multiphase thermodynamics, enthalpy based energy solution 2.3.0 & 2.3.1 (2014) Consolidation, new runtime selectable interfacial and turbulence models. Large selection of closure models 3.0 & 3.0.1 (2015) Boundary condition with heat flux 4.0 (2016) Simplification of sub-models use 4

Information on experiment Siberian Branch of Russian Academy of Sciences Nakoryakov V.E. et al. Local Characteristics of Upward Gas-Liquid Flows // Int. J. Multiphase Flow 1981. V. 7. P. 63-81. 5

Experimental data 6

Case set-up inlet symmetry wall inlet: - Uniform velocity profile for liquid and gas phases (U g, U l ) - Uniform void fraction profile (α) wall: - No-slip BC for liquid phase - Slip BC for gas phase - Standard wall-function for turbulence parameters outlet: - zerogradient for velocity and turbulence parameters, - fixed pressure value inlet 7

Interfacial interaction models Interfacial interaction models in OpenFOAM 2.3.0 (2012): 8

twophaseeulerfoam Properties Reader Utility to simplify phaseproperties file input 9

Determining optimal mesh size α = 0 α = 0,05 Experiment Simulation, mesh 1 Simulation, mesh 2 Simulation, mesh 3 Experiment, regime 9 Simulation Data [Nakoryankov], mesh 1 1000 cells, mesh 2 4000 cells, mesh 3 10 000 cells Comparison of simulation results and experimental data for single-phase simulation Nakoryakov V.E. et al. Local Characteristics of Upward Gas-Liquid Flows // Int. J. Multiphase Flow 1981. V. 7. P. 63-81. 10

Simulation results (1) Void fraction distribution via radius and height of the channel α h = 0,1 м α h = 0,3 м α h = 0,6 м r/r 0 r/r 0 r/r 0 α h = 0,05 м α h = 0,2 м α h = 0,4 м r/r 0 r/r 0 r/r 0 11

Simulation results (2) Experiment, regime 9 Simulation Experiment, regime 6 Simulation OpenFOAM 2.3 «Baseline» model d b = const (1 mm) T9: α=0,05; β=0,07 Re = 44 000 Experiment, regime 19 Simulation Experiment, regime 12 Simulation T6: α=0,07; β=0,15 Re = 22 000 T19: α=0,03; β=0,04 Re = 110 000 T12: α=0,15; β=0,2 Re = 44000 Void fraction distribution via radius 12

Simulation results (3) OpenFOAM 3.0 «baseline model» + d b IATE (0,5 1,5 мм) + turbulentbreakup + komegasst-sato + randomcoalescence α α Experiment, regime 11 Simulation, OF30 Experiment, regime 15 Simulation, OF30 r/r 0 r/r 0 13

Simulation results (4) β > 0,2 (β =0,254) α Сеточная зависимость r/r 0 Зависимость от размера пузырька, d [мм] 14

Simulation results (5) k, omega Single phase Two-phase Single phase Two-phase r, м Turbulence suppression in two-phase flow 15

Simulation results (6) Dependence of shear stress at the wall τ on gas flow ratio β Experiment [1], Re = 40 000 Simulation OF Armand [9] 1. Nakoryakov V.E. et al. Local Characteristics of Upward Gas-Liquid Flows // Int. J. Multiphase Flow 1981. V. 7. P. 63-81. 9. Armand A.A., Nevstryaeva E.I. Investigation of mechanism of two-phase flow in vertical tube. // Izv. VTI Vol. 2, P. 1-8. 1950 16

Conclusion In the work the result of numerical simulation of void fraction distribution via radius of the channel with two-phase flow with low (β = 0.05 0,2) gas flow ratios are presented In the area of the low void-fractions simulation results demonstrate abnormal increase (six times increase in the maximum) of shear stress in the round channel, which was observed experimentally Based on simulation results the decision was made that OpenFOAM code is adequately simulates saddle-shaped void-fraction profile, which is believed to be the reason of abnormal increase of shear stress in channel at 0 < β < 0,2 17

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