Review Article

Review of Available Data for Validation of Nuresim Two-Phase CFD Software Applied to CHF Investigations

Table 2

Correspondence between the data sources relative to DNB investigations and the basic phenomena at the mesoscale. α: local void fraction, Ai: local interfacial area density, δb: local average bubble diameter, Fδ: bubble size distribution, Vlz: axial mean liquid velovity, vlz: rms axial liquid velovity, Vbz: axial mean bubble velovity, Tl: liquid temperature, Tw: wall temperature, Tw: rms value of wall temperature, Vlx: radial component of mean liquid velovity, vlx: rms radial component of liquid velovity, ϕcrit: critical heat flux.

DEDALEDEBORADEBORA PromoterAGATE (&AGATE-promoter)ASUPURDUE boilingKAERI boilingTOPFLOWBFBTLWL

GeometryTube L = 6 m D = 0.0381 mTube D = 0.0192 mTube + promoterRod bundle (tube +promoter)Annulus Di = 15.78 mm De = 38.02 mAnnulus Di = 19.1 m De = 38.1 mAnnulus Di = 19 mm De = 37.5 mmTube D = 195.3 mmRod bundleRod bundle
Fluid/flow conditionsAir-water adiabaticR12R12waterR113Steam-waterSteam-waterAir-water and steam-waterSteam/ waterSteam/ water
Local measur-ementsα, Ai, δb, Fδ, Vlz, vlz, Vbz at Z/D=8, 55 & 155α, Ai, Tl, Tw, δb, Vbz,α, Ai, Tl, Tw, δb, Vbz,Vlz, vlzVlx, vlxα, Vlz, vlz, vlx, Vbz, Tw, Tw, turbulent heat fluxesα, Ai, δb, Vbz at z/D=52.6 +visual observationsα, Ai, δb, Vlz, Vbzα, δb, Vbz, Fδαϕcritϕcrit
Wall to fluid heatXXXX
Bubbles transport and dispersionXXXXXX
Vaporization-condensationXXXXX
Coalescence and breakup of bubblesXXXXXX
Turbulent Transfers of heat and momentumXXXXXXXX
Effects of polydispersionXX
Effects of gridsXX
Combined effects in real geometryBWRPWR WWER