Review Article

CFD Applications to Pressurized Thermal Shock-Related Phenomena

Table 8

CFD simulations of a two-phase (steam–water) flow on the TOPFLOW-PTS experiments.

CFD simulationTestCodeMesh resolutionTwo-phaseStandard Standard SST RSMLESInterfacial momentum transferHeat and mass transferFluid propertiesSimulation

Apanasevich et al. [91]NURISP project, steady-state steam–water case (pre-test)ANSYS CFX 12.00.85 M elementsInhomogeneous (two-fluid) modelN/ADCC model based on the surface renewal theory proposed by Hughes and Duffey [102] and two resistance modelConstantTransient
Martin et al. [93]NURISP project, steady-state steam–water case (pre-test)NEPTUNE_CFD0.43 M cells (fluid domain) and 0.06 M cells (solid domain)Two-fluid modelLIMN/ACATHARETransient
Apanasevich et al. [92]NURISP project, steady-state steam–water case (pre-test)ANSYS CFX 12.00.87 M and 1.7 M elementsTwo-fluid modelAIAD and no modeling (standard two-fluid model)DCC model based on the surface renewal theory proposed by Hughes and Duffey [102] and two resistance modelIAPWSTransient
Coste and Lecomte [104]SSSW 3-2NEPTUNE_CFD 1.30.54 M cellsTwo-fluid modelLIM
(ver. 1.0.8 and ver. 2.0-beta)
DCC model based on the surface renewal theory proposed by Coste[110], Lakehal et al. [111], Magnaudet and Calmet [112], and wall law type model [103]N/ATransient
Apanasevich et al. [15]NURISP project, steady-state steam–water case (pre-test)ANSYS CFX 12.0, ANSYS FLUENT 12.0 and NEPTUNE_CFD 1.0.8CFX: 0.87 M and 1.7 M cells, FLUENT: 0.87 M elements, and NEPTUNE_CFD: 0.53 M cells and 1.5 M elementsCFX and NEPTUNE_CFD: Two-fluid model and FLUENT: VOF method
(NEPTUNE_CFD)

(CFX)

Smagorinsky SGS model
(FLUENT)
CFX: AIAD and constant drag coefficient of 0.44,
FLUENT: N/A, and NEPTUNE_CFD: LIM
CFX: DCC model based on the surface renewal theory [116] by Hughes and Duffey [102], FLUENT: DCC model based on the surface renewal theory by Hughes and Duffey [102], NEPTUNE_CFD: DCC model based on the surface divergence model by Lakehal et al. [121] and the surface renewal theory by Coste [110] and wall law type model [103]CFX: IAPWS, FLUENT:
no equation of state and user function for the case of steam, and NEPTUNE_CFD: CATHARE
FLUENT: Transient and CFX and NEPTUNE_CFD: not listed
Apanasevich et al. [35]NURESAFE project, undisclosed in detail (There is a possibility of SSSW 3-17.)ANSYS CFX 14.51.2 M and 2.0 M cellsTwo-fluid modelAIAD and constant drag coefficient of 0.44DCC model based on the surface renewal theory proposed by Hughes and Duffey [102] and Magnaudet and Calmet [112]IAPWSSteady-state
Coste and Mérigoux [105] and Mérigoux et al. [106]NURESAFE project, SSSW 3-16, 3-17, 3-18, 3-19NEPTUNE_CFD 2.0.0 and 2.2.00.44 M, 0.78 M, 1.1 M, and 1.8 M cellsTwo-fluid model
(ver. 2.0.0)

SSG
(ver. 2.2.0)
LIMDCC model based on the surface divergence model proposed by Magnaudet and Calmet [112](ver. 2.0.0), Lakehal et al. [111] (ver. 2.2.0) and wall law type model [103]CATHARETransient
Mérigoux et al. [107]SSSW 3-17 (mesh sensitivity study) and TSW 3-5NEPTUNE_CFD 3.0.00.44 M, 0.78 M, 1.1 M, 1.8 M cells
(SSSW 3-17) and 0.78 M cells (TSW 3-5)
Two-fluid model
SSG
LIMDCC model based on the surface divergence model proposed by Lakehal et al. [111] and wall law type model [103]CATHARETransient
Mérigoux et al. [17]NURESAFE project, SSSW 3-17ANSYS CFX 16.0, TransAT 5.1.2_RC2, and NEPTUNE_CFD 3.0.0CFX: 1.2 M cells, NEPTUNE_CFD: 0.78 M cells, and TransAT: 1.2 M elementsCFX, NEPTUNE_CFD: Two-fluid model and TransAT: LS method
(TransAT)

(CFX)

SSG
(NEPTUNE_CFD)
CFX: AIAD and NEPTUNE_CFD: LIMCFX: DCC model based on the surface divergence model proposed by Lakehal et al. [111], NEPTUNE_CFD: DCC model based on the surface divergence model proposed by Lakehal et al. [111] and wall law type model [103], and TransAT: DCC model based on the surface divergence model proposed by Coste [110]CFX: IAPWS, NEPTUNE_CFD: CATHARE, and TransAT: constantCFX: steady-state and NEPTUNE_CFD and TransAT: transient

SSSW: steady-state steam–water with mass transfer due to condensation; TSW: transient steam–water with mass transfer due to condensation. Data in italics under mesh resolution: conditions used for validation among multiple conditions or conditions that were indicated to be suitable.