2016
DOI: 10.1007/s00231-016-1874-6
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Experimental study on heat transfer of supercritical carbon dioxide in a long silica-based porous-media tube

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Cited by 5 publications
(4 citation statements)
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“…7(b)). In other words, U eva decreased with increasing heat source temperature because of the decrease in the specific heat of the working fluid far from the pseudocritical temperature [25]. For the ORC system, the working fluid pump supplied pressure in the evaporator.…”
Section: Resultsmentioning
confidence: 99%
“…7(b)). In other words, U eva decreased with increasing heat source temperature because of the decrease in the specific heat of the working fluid far from the pseudocritical temperature [25]. For the ORC system, the working fluid pump supplied pressure in the evaporator.…”
Section: Resultsmentioning
confidence: 99%
“…The heat transfer coefficient of supercritical CO 2 can be determined using the logarithmic mean temperature difference approach, as presented in the following equations: Tm=ΔTinΔToutlnΔTinΔTout ΔTin=Tw,1Tin ΔTout=Tw,10Tout h=QATm where h represents the test section's mean heat transfer coefficient. To comprehend phenomena related to heat transfer and fluid flow, the wall temperature and pressure and temperature of supercritical fluid were measured.…”
Section: Experimental Apparatus and Thermodynamic Analysis Methodologymentioning
confidence: 99%
“…Studies have indicated that fast variations in fluid physical properties close to the pseudocritical and critical points result in a maximal heat transfer coefficient. In particular, heat transfer‐related phenomena are affected by buoyancy in vertical and horizontal tubes .…”
Section: Introductionmentioning
confidence: 99%
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