2000
DOI: 10.13182/fst00-a120
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An Experimental Examination of the Loss-of-Flow Accident Phenomenon for Prototypical ITER Divertor Channels ofY= 0 andY= 2

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Cited by 6 publications
(11 citation statements)
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“…The heat transfer coefficient in forced flow saturated boiling is estimated by the correlation proposed by Chen [7]: F is the convective boiling enhancement factor and calculated as F = 1.0 for 1/X tt ≤ 0.1 2.35(1/X tt + 0.213) 0.736 for 1/X tt > 0.1 (13) where X tt is the Lockhart-Martinelli parameter and given by where T sat is the wall superheat, P sat is the difference between the saturation pressures calculated from the wall temperature and the fluid temperature and S is the nucleate boiling suppression factor and calculated as Re TP is the two-phase Reynolds number and given by…”
Section: Saturated Nucleate Boilingmentioning
confidence: 99%
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“…The heat transfer coefficient in forced flow saturated boiling is estimated by the correlation proposed by Chen [7]: F is the convective boiling enhancement factor and calculated as F = 1.0 for 1/X tt ≤ 0.1 2.35(1/X tt + 0.213) 0.736 for 1/X tt > 0.1 (13) where X tt is the Lockhart-Martinelli parameter and given by where T sat is the wall superheat, P sat is the difference between the saturation pressures calculated from the wall temperature and the fluid temperature and S is the nucleate boiling suppression factor and calculated as Re TP is the two-phase Reynolds number and given by…”
Section: Saturated Nucleate Boilingmentioning
confidence: 99%
“…The swirl tape inserts influence on the fully developed nucleate boiling regime is negligible; however, they considerably increase the critical heat flux [12]. When the cooling channel features a swirl tape insert, swirl tape factors must be applied to the previously described heat transfer correlations that were defined for bare channel tubes [13].…”
Section: Heat Transfer Enhancementmentioning
confidence: 99%
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