2022
DOI: 10.1016/j.energy.2022.124240
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Heat transfer deterioration in vertical sCO2 cooling in 3 mm tube

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Cited by 9 publications
(2 citation statements)
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“…A possible cause for the above is an under-prediction of the viscous losses in the flow in the vicinity of the heat transfer equipment of the setup. As qualitatively described in the work of Wahl et al [17], the alignment of the direction of both forcedand natural convection can result in near-wall velocities that are greater than in an adiabatic setting. For flows of supercritical media, this is the case for downward cooled and upward heated pipe flows.…”
Section: Resultsmentioning
confidence: 89%
“…A possible cause for the above is an under-prediction of the viscous losses in the flow in the vicinity of the heat transfer equipment of the setup. As qualitatively described in the work of Wahl et al [17], the alignment of the direction of both forcedand natural convection can result in near-wall velocities that are greater than in an adiabatic setting. For flows of supercritical media, this is the case for downward cooled and upward heated pipe flows.…”
Section: Resultsmentioning
confidence: 89%
“…Wahl et al [1] experimentally investigated the cooling heat transfer coefficient in a 3 mm diameter tube with vertical flow orientation using the mixed convection criterion to evaluate the heat transfer deterioration. The results showed an influence of mixed convection at a stepwise reduction of the mass flux.…”
Section: Heat Exchanger and Transfermentioning
confidence: 99%