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3D couette flow of dusty fluid with transpiration cooling
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Govindarajan A. , Ramamurthy V. , Sundarammal K.. 3D couette flow of dusty fluid with transpiration cooling[J]. Journal of Zhejiang University Science A, 2007, 8(2): 313-322.
@article{title="3D couette flow of dusty fluid with transpiration cooling",
author="Govindarajan A. , Ramamurthy V. , Sundarammal K.",
journal="Journal of Zhejiang University Science A",
volume="8",
number="2",
pages="313-322",
year="2007",
publisher="Zhejiang University Press & Springer",
doi="10.1631/jzus.2007.A0313"
}
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%T 3D couette flow of dusty fluid with transpiration cooling
%A Govindarajan A.
%A Ramamurthy V.
%A Sundarammal K.
%J Journal of Zhejiang University SCIENCE A
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%I Zhejiang University Press & Springer
%DOI 10.1631/jzus.2007.A0313
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T1 - 3D couette flow of dusty fluid with transpiration cooling
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A1 - Sundarammal K.
J0 - Journal of Zhejiang University Science A
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%@ 1673-565X
Y1 - 2007
PB - Zhejiang University Press & Springer
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DOI - 10.1631/jzus.2007.A0313
Abstract: The couette dusty flow between two horizontal parallel porous flat plates with transverse sinusoidal injection of the dusty fluid at the stationary plate and its corresponding removal by constant suction through the plate in uniform motion was analyzed. Due to this type of injection velocity the dusty flow becomes 3D. Perturbation method is used to obtain the expressions for the velocity and temperature fields of both the fluid and dust. It was found that the velocity profiles of both the fluid and dust in the main flow direction decrease with the increase of the mass concentration of the dust particles, and those in cross flow direction increase with an increase in the mass concentration of the dust particles up to the middle of the channel and thereafter decrease with increase in mass concentration of the dust particles. The skin friction components Tx and Tz in the main flow and transverse directions respectively increase with an increase in the mass concentration of the dust particles (or) injection parameter. The heat transfer coefficient decreases with the increase of the injection parameter and increases with the increase in the mass concentration of the dust particles.
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