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TECHNICAL NOTES

Numerical Solution for Transient Conjugate Two-Phase Heat Transfer With Heat Generation in the Pipe Wall

[+] Author and Article Information
Yuri V. Fairuzov, Hector Arvizu

Institute of Engineering, P.O. Box 70-472, National Autonomous University of Mexico, Mexico City 04510, Mexico

J. Heat Transfer 124(6), 1213-1218 (Dec 03, 2002) (6 pages) doi:10.1115/1.1470170 History: Received June 05, 2001; Revised December 18, 2001; Online December 03, 2002
Copyright © 2002 by ASME
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References

Figures

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Variation of the mass velocity at the pipeline outlet with time
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Two-phase conjugate heat transfer with heat generation in the wall
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Variation of temperature with time at the inlet (x/L=0),middle (x/L=0.5), and the outlet (x/L=1) of the pipeline
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Variation of the overall temperature difference with time at the inlet (x/L=0),middle (x/L=0.5), and the outlet (x/L=1) of the pipeline predicted by the rigorous model (N=100,Nw=10)
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Variation of the heat flux at the wall-fluid interface with time at the inlet (x/L=0) and the outlet (x/L=1) of the pipeline (tc,f≫tc,w)
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Variation of the heat flux at the wall-fluid interface with time at the inlet (x/L=0) and the outlet (x/L=1) of the pipeline (tc,f∼tc,w)
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Variation of the pressure drop with time

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