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TECHNICAL NOTES

Enhanced Natural Convection in a Vertical Rectangular Cavity on Account of the Mixing of Two Pure Gases

[+] Author and Article Information
Antonio Campo

College of Engineering, Idaho State University, Pocatello, ID 83209

Blas Zamora

Dpto. de Ingeniería Mecánica y Energética, Universidad Politécnica de Cartagena, 30203 Cartagena, Murcia, Spain

J. Heat Transfer 122(2), 384-387 (Sep 29, 1999) (4 pages) doi:10.1115/1.521477 History: Received January 06, 1999; Revised September 29, 1999
Copyright © 2000 by ASME
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References

Gebhart, B., Jaluria, Y., Mahajan, R. L., and Sammakia, B., 1988, Buoyancy-Induced Flows and Transport, Hemisphere, New York.
Wilke,  C. R., 1950, “A Viscosity Equation for Gas Mixtures,” J. Chem. Phys. 18, pp. 517–523.
Wassiljeva,  A., 1904, “Heat Conduction in Gaseous Mixtures,” Phys. Z. 5, pp. 737–750.
Mason,  E. A. and Saxena,  S. C., 1958, Phys. Fluids 1, pp. 361–370.
Mason,  E. A. and Saxena,  S. C., 1959, J. Chem. Phys. 31, pp. 511–518.
Jakob,  M., 1946, “Free Convection Through Enclosed Plane Gas Layers,” Trans. ASME 68, pp. 189–195.
Graff,  J. G., and Van der Held,  E. F., 1952, “The Relation Between the Heat Transfer and Convection Phenomena in Enclosed Plain Air Layers,” Appl. Sci. Res. Ser. A, 3, pp. 393–405.
Mills, A. F., 1995, Heat Transfer, Richard Irwin, Boston, MA.

Figures

Grahic Jump Location
Vertical rectangular cavity
Grahic Jump Location
Variation of the relative mean heat transfer coefficient, h̄m/B, with the composition, x, of a He/N2 gas mixture for n=1/4: (a) 200 K, (b) 1000 K
Grahic Jump Location
Variation of the relative mean heat transfer coefficient, h̄m/B, with the composition, x, of a He/N2 gas mixture for n=1/3: (a) 200 K, (b) 1000 K

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