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TECHNICAL PAPERS: Natural and Mixed Convection

Effect of Double Dispersion on Mixed Convection Heat and Mass Transfer in Non-Darcy Porous Medium

[+] Author and Article Information
P. V. S. N. Murthy

Department of Mathematics, I.I.T.–Madras, Madras 600 036, India

J. Heat Transfer 122(3), 476-484 (Jan 18, 2000) (9 pages) doi:10.1115/1.1286995 History: Received April 20, 1999; Revised January 18, 2000
Copyright © 2000 by ASME
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References

Figures

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Coupled heat and mass transfer by mixed convection from a vertical plate in a saturated porous medium (reproduced from Lai 4)
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Nondimensional velocity profiles f(η) for −1<N<0,Le=0.1 (aiding flow)
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Nondimensional velocity profiles f(η) for 0<Le<1,N=−0.5 (aiding flow)
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Heat transfer coefficient as a function of Lewis number when N<0. Here N=−0.5,Peγ=0=Peζ (aiding flow).
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Heat transfer coefficient as a function of Lewis number when N>0. Here, N=4.0,Peγ=0=Peζ (aiding flow).
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Mass transfer coefficient as a function of Lewis number when N<0. Here N=−0.5,Peγ=0=Peζ (aiding flow).
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Mass transfer coefficient as a function of Lewis number when N>0. Here, N=4.0,Peγ=0=Peζ (aiding flow).
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Heat transfer coefficient as a function of Ra/Pe when FoPe=1.0,Le=1.0,Peζ=0 (aiding flow)
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Heat transfer coefficient as a function of Ra/Pe when FoPe=1.0,Le=10.0,Peζ=0 (aiding flow)
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Mass transfer coefficient as a function of Ra/Pe when FoPe=1.0,Le=1.0,Peγ=0 (aiding flow)
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Mass transfer coefficient as a function of Ra/Pe when FoPe=1.0,Le=10.0,Peγ=0 (aiding flow)
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Heat transfer coefficient as a function of Le for various values of N when Peγ=0=Peζ,Ra/Pe=1.0,FoPe=1.0 (opposing flow)
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Mass transfer coefficient as a function of Le for various values of N when Peγ=0=Peζ,Ra/Pe=1.0,FoPe=1.0 (opposing flow)
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Heat transfer coefficient as a function of Ra/Pe in the presence of thermal dispersion effects in non-Darcy flow. Here FoPe=1.0,Le=1.0,Peζ=0 (opposing flow).
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Heat transfer coefficient as a function of Ra/Pe in the presence of thermal dispersion effects in non-Darcy flow. Here FoPe=1.0,Le=10.0,Peζ=0 (opposing flow).
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Mass transfer coefficient as a function of Ra/Pe in the presence of solutal dispersion effects in non-Darcy flow. Here FoPe=1.0,Le=1.0,Peγ=0 (opposing flow).
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Mass transfer coefficient as a function of Ra/Pe in the presence of solutal dispersion effects in non-Darcy flow. Here FoPe=1.0,Le=10.0,Peγ=0 (opposing flow).

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