2019
DOI: 10.1051/e3sconf/201912801017
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Comparison of the 1D and 2D calculation models used for determination of the heat transfer coefficient during flow boiling heat transfer in a minichannel

Abstract: The paper discusses the results of the flow boiling heat transfer in a vertical minichannel with rectangular cross-section. The heating element for FC-72 flowing in the minichannel is a thin plate. Infrared thermography is used to determine changes in the temperature on its outer side. The aim of the calculation is to determine the heat transfer coefficient using 1D and 2D calculation models. Local values of heat transfer coefficient on the surface between the heated plate and boiling fluid are calculated from… Show more

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Cited by 4 publications
(1 citation statement)
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“…However, due to thermal conduction in the microchannel substrate, this inevitably results in some degree of circumferential non-uniform heat flux on the internal wetted surface. Studies have been conducted on the influence of parameters such as the number of channels [6,7], the cross-sectional profile [8][9][10], hydraulic diameters [11][12][13][14][15], systems with uniform heating [16][17][18][19][20][21][22], the orientation of the channel [1,23,24], hydrodynamic effects like confinement [25][26][27] and the effect of varying working fluids [28,29].…”
Section: Introductionmentioning
confidence: 99%
“…However, due to thermal conduction in the microchannel substrate, this inevitably results in some degree of circumferential non-uniform heat flux on the internal wetted surface. Studies have been conducted on the influence of parameters such as the number of channels [6,7], the cross-sectional profile [8][9][10], hydraulic diameters [11][12][13][14][15], systems with uniform heating [16][17][18][19][20][21][22], the orientation of the channel [1,23,24], hydrodynamic effects like confinement [25][26][27] and the effect of varying working fluids [28,29].…”
Section: Introductionmentioning
confidence: 99%