Proceeding of International Heat Transfer Conference 9 1990
DOI: 10.1615/ihtc9.4130
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Thermal Hydraulic Subchannel Model Based on Void-Drift

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Cited by 5 publications
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“…Form losses in the axial direction Carlucci [38], Rehme [39], Rao [40], Rosehart and Rogers [41] Inter-subchannel turbulent mixing and modified Carlucci inter-subchannel turbulent mixing Ohkawa and Lahey [42] Axial relative velocity, drift flux Wallis [43], Carlucci [38], Ohkawa and Lahey [42] Lateral relative velocity, lateral buoyancy drift velocity Carlucci [38], Rowe [44], Shoukri [45] Void diffusion coefficient Lahey and Moody [46], Rowe [44] Equilibrium void Pre-CHF heat transfer models Dittus-Boelter [47] Pre-CHF single-phase liquid heat transfer Chen [48] Pre-CHF 2-phase heat transfer Ahmad [49], Rouhani [50], Maróti [51], Lahey and Moody [46] Pre-CHF 2-phase heat transfer Hancox and Nicoll [52] Pre-CHF 2-phase heat transfer, interfacial heat transfer, H il Hammouda [53] Onset of nucleate boiling Ishii [54], Thurgood and Kelly [55], Maróti [51], Lahey and Moody [46] Interfacial heat transfer model: based on 4 simplified void fraction regions Thurgood and Kelly [55] Interfacial area: bubbly flow, bubbly-slug flow, churnturbulent flow, and annular flow Thurgood and Kelly [55], Maróti [51],…”
Section: Summary and Recommendationmentioning
confidence: 99%
“…Form losses in the axial direction Carlucci [38], Rehme [39], Rao [40], Rosehart and Rogers [41] Inter-subchannel turbulent mixing and modified Carlucci inter-subchannel turbulent mixing Ohkawa and Lahey [42] Axial relative velocity, drift flux Wallis [43], Carlucci [38], Ohkawa and Lahey [42] Lateral relative velocity, lateral buoyancy drift velocity Carlucci [38], Rowe [44], Shoukri [45] Void diffusion coefficient Lahey and Moody [46], Rowe [44] Equilibrium void Pre-CHF heat transfer models Dittus-Boelter [47] Pre-CHF single-phase liquid heat transfer Chen [48] Pre-CHF 2-phase heat transfer Ahmad [49], Rouhani [50], Maróti [51], Lahey and Moody [46] Pre-CHF 2-phase heat transfer Hancox and Nicoll [52] Pre-CHF 2-phase heat transfer, interfacial heat transfer, H il Hammouda [53] Onset of nucleate boiling Ishii [54], Thurgood and Kelly [55], Maróti [51], Lahey and Moody [46] Interfacial heat transfer model: based on 4 simplified void fraction regions Thurgood and Kelly [55] Interfacial area: bubbly flow, bubbly-slug flow, churnturbulent flow, and annular flow Thurgood and Kelly [55], Maróti [51],…”
Section: Summary and Recommendationmentioning
confidence: 99%
“…In the similar way, a model for F I was selected by comparing dp/dz's obtained from Eqs. 7and (8). As a result, those correlations that were used in the following analysis are listed in Appendix.…”
Section: Total Pressure Gradientmentioning
confidence: 99%