2020
DOI: 10.1016/j.nucengdes.2019.110388
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Mechanistic modeling of the thermal-hydraulics in polydispersed flow film boiling in LOCA conditions

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Cited by 8 publications
(10 citation statements)
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“…In fact, the mean droplets diameter is 65 pm, 85 pm, 68 pm, and 70 pm for steam flow rates of 2.2 kg/h, 4.0 kg/h, 6.1 kg/, and 7.4 kg/h, respectively. Comparing these values with the condition upstream of the heated tube (Table 2), we find a reduction in the droplets diameter by 23% to 30%, which occurs due to heat transfer from both wall and steam to droplets that results in their evaporation, as discussed by Oliveira et al [25]. Droplets breakup does not occur in any case because their Weber number never reaches the critical value of 12 [33], as shown in Fig.…”
Section: Pda Results: Droplets Characteristicssupporting
confidence: 68%
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“…In fact, the mean droplets diameter is 65 pm, 85 pm, 68 pm, and 70 pm for steam flow rates of 2.2 kg/h, 4.0 kg/h, 6.1 kg/, and 7.4 kg/h, respectively. Comparing these values with the condition upstream of the heated tube (Table 2), we find a reduction in the droplets diameter by 23% to 30%, which occurs due to heat transfer from both wall and steam to droplets that results in their evaporation, as discussed by Oliveira et al [25]. Droplets breakup does not occur in any case because their Weber number never reaches the critical value of 12 [33], as shown in Fig.…”
Section: Pda Results: Droplets Characteristicssupporting
confidence: 68%
“…for 2.2 kg/h steam flow rate, is approximately 4450. During the Leidenfrost regime, droplets impact contributes significantly to the heat dissipation, as already discussed by several authors [25][26][27],…”
Section: Irt Results: Internai Heat Dissipation and Wall Rewettingmentioning
confidence: 65%
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“…The predominant mechanism in the cooling of the fuel rods by the steam/droplets flow is the steamto-wall convection. Nevertheless, cooling given by the impact of droplets on the wall is not negligible [1]. Moreover, the fluid area in the sub-channels could be severely reduced by the ballooning of fuel rods during the LOCA transient.…”
Section: Introductionmentioning
confidence: 99%
“…As the water level rises, steam and droplets are generated at the quenching front, providing a dispersed flow that plays a very important role to cool the regions that are not yet immersed into water. With that said and knowing that wall-to-steam convection is the predominant heat dissipation process in dispersed flow film boiling [9,10], the cooling in blocked sub-channels is highly degraded because of the preferential steam flow through intact or less blocked regions, which is known as flow redistribution or bypass effect [11].…”
Section: Introductionmentioning
confidence: 99%