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contributor authorChu, Xu
contributor authorLaurien, Eckart
date accessioned2017-05-09T01:32:16Z
date available2017-05-09T01:32:16Z
date issued2016
identifier issn2332-8983
identifier otherNERS_2_3_031019.pdf
identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/162225
description abstractFor fluids at supercritical pressure, the phase change from liquid to gas does not exist. Meanwhile, the fluid properties change drastically in a narrow temperature range. With supercritical fluid as working fluid in a heated pipe, heattransfer deterioration and recovery have been observed, which corresponds to the turbulent flow relaminarization and recovery. Direct numerical simulation (DNS) of supercritical carbon dioxide flow in a heated vertical circular pipe is developed with the opensource code OpenFOAM in this study. Forcedconvection and mixedconvection cases including upward and downward flow have been considered in the simulation. In the forced convection, flow turbulence is attenuated due to acceleration from thermal expansion, which leads to a peak of the wall temperature. However, buoyancy shows a stronger impact on the flow. In the upward flow, the average streamwise velocity distribution turns into an Mshaped profile because of the external effect of buoyancy. Besides that, negative buoyancy production caused by the density variation reduces the Reynolds shear stress to almost zero, which means that the flow is relaminarized. Further downstream, turbulence is recovered. This behavior of flow turbulence is confirmed by visualization of turbulent streaks and vortex structures.
publisherThe American Society of Mechanical Engineers (ASME)
titleDirect Numerical Simulation of Heated Turbulent Pipe Flow at Supercritical Pressure
typeJournal Paper
journal volume2
journal issue3
journal titleJournal of Nuclear Engineering and Radiation Science
identifier doi10.1115/1.4032479
journal fristpage31019
journal lastpage31019
treeJournal of Nuclear Engineering and Radiation Science:;2016:;volume( 002 ):;issue: 003
contenttypeFulltext


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