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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

Vanvik, T., and Moe, R., 1998, “Direct Heating of Multiphase Flowlines for Hydrate Control on Åsgard,” Multiphase Technology, Technology from the Arctic to the Tropics, J. P. Brill and G. A. Gregory, eds., BHR Group, pp. 207–216.
Aarseth, F., 1997, “Use of Electrical Power in Control of Wax and Hydrates,” Offshore Technology Conference, Annual Proceedings, 4 , Richardson, TX, USA, p. 13.
Bergles, A. E., 1981, “Instabilities in Two-Phase Systems,” Two-Phase Flow and Heat Transfer in the Power and Process Industries, J. G. Collier, J. M. Delhaye, G. F. Hewitt, and F. Mayinger, eds., Hemisphere Publishing Corporation, pp. 383–423, Chap. 13.
Fairuzov,  Y. V., 2000, “Modeling of Conjugate Two-Phase Heat Transfer During Depressurization of Pipelines,” ASME J. Heat Transfer, 122, pp. 99–106.
Fairuzov,  Y. V., 1998, “Numerical Solution for Blowdown of Pipeline Containing Flashing Liquid,” AIChE J., 44, pp. 2124–2128.
Bejan, A., 1993, Heat Transfer, John Wiley & Sons, New York.
Gungor,  A. E., and Winterton,  R. S. H., 1987, “Simplified General Correlation for Saturated Flow Boiling and Comparisons of Correlations With Data,” Chem. Eng. Res. Des., 65, pp. 148–156.
Hewitt, G. F., 1998, Boiling, Handbook of Heat Transfer, Third Ed., W. M. Rohsenow, J. P. Hartnett, and Y. I. Cho, eds. McGraw-Hill Handbooks, New York, pp. 15.97–15.103.

Figures

Grahic Jump Location
Variation of the mass velocity at the pipeline outlet with time
Grahic Jump Location
Two-phase conjugate heat transfer with heat generation in the wall
Grahic Jump Location
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
Grahic Jump Location
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)
Grahic Jump Location
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)
Grahic Jump Location
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)
Grahic Jump Location
Variation of the pressure drop with time

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