TECHNICAL PAPERS: Phase Change and Multiphase Heat Transfer

Modeling of Conjugate Two-Phase Heat Transfer During Depressurization of Pipelines

[+] Author and Article Information
Y. V. Fairuzov

Institute of Engineering, P.O. Box 70-472, National Autonomous University of Mexico, Mexico City 04510, Mexico e-mail: fairuzov@servidor.unam.mx

J. Heat Transfer 122(1), 99-106 (Oct 07, 1999) (8 pages) doi:10.1115/1.521428 History: Received April 26, 1999; Revised October 07, 1999
Copyright © 2000 by ASME
Your Session has timed out. Please sign back in to continue.


Sucec,  J., 1975, “Unsteady Heat Transfer Between a Fluid With Time Varying Temperature and a Plate: An Exact Solution,” Int. J. Heat Mass Transf., 18, pp. 25–34.
Sucec,  J., 1981, “An Improved Quasi-Steady Approach for Transient Conjugated Forced Convection Problems,” Int. J. Heat Mass Transf., 24, pp. 1711–1722.
Lin,  Y. K., Yin,  C. P., and Yan,  W. M., 1991, “Transient Laminar Mixed Convective Heat Transfer in a Flat Duct,” ASME J. Heat Transfer, 113, pp. 384–390.
Lin,  Y. K., and Kuo,  J. C., 1988, “Transient Conjugated Heat Transfer in Fully Developed Laminar Pipe Flows,” Int. J. Heat Mass Transf., 31, pp. 1093–1102.
Chen,  J. C., 1966, “Correlation for Boiling Heat Transfer to Saturated Liquids in Convective Flow,” Int. Eng. Chem. Process Design Development 5, pp. 322–333.
Klimenko,  V. V., 1988, “A Generalized Correlation for Two-Phase Forced Flow Heat Transfer,” Int. J. Heat Mass Transf., 31, pp. 541–552.
Shah,  M., 1976, “A New Correlation for Heat Transfer During Boiling Flow Through Tubes,” ASHRAE Trans., 82, pp. 66–72.
Fairuzov,  Y. V., 1998, “Blowdown of Pipelines Carrying Flashing Liquids,” AIChE J., 44, pp. 245–254.
Fairuzov,  Y. V., 1998, “Numerical Solution for Blowdown of Pipeline Containing Flashing Liquid,” AIChE J., 44, pp. 2124–2128.
Richardson, S. M., and Saville, G., 1991, “Blowdown of Pipelines,” Proceedings of Offshore Europe 91, Aberdeen, U.K., SPE Paper No. 23070.
Wallis,  G. B., 1980, “Critical Two-Phase Flow,” Int. J. Multiphase Flow, 6, pp. 97–112.
Chen,  J. R., Richardson,  S. M., and Saville,  G., 1995, “Modelling of Two-Phase Blowdown from Pipelines-II. A Simplified Numerical Method for Multi-Component Mixtures,” Chem. Eng. Sci., 50, pp. 2173–2187.
Solorzano,  M., Barragán-Arroche,  F., and Bazua-Rueda,  E., 1996, “Comparative Study of Mixing Rules for Cubic Equations of State in the Prediction of Multicomponent Vapor-Liquid Equilibria,” J. Phase Equilib., 122, pp. 99–106.
McAdams,  W. H., Woods,  W. K., and Heroman,  L. C., 1942, “Vaporization Inside Horizontal Tubes. II-Benzane-Oil Mixtures,” Trans. ASME, 64, pp. 193–200.
Collier, J. G., 1981, “Multicomponent Boiling and Condensation,” Two-Phase Flow and Heat Transfer in the Power and Process Industries, Bergels, A. E., Collier, J. G., Delhaye, J. M., Hewitt, G. F., and Mayinger, F., eds., Hemisphere, Washington, D.C., pp. 520–557.
Stephan,  K., and Korner,  M., 1969, “Calculation of Heat Transfer in Evaporating Binary Liquid Mixtures,” Chem. Ing. Technik. 41, pp. 409–417.
Ransom, V. H., and Trapp, J. A., 1978, “RELAP5 Progress Summary,” PILOT Code Hydrodynamic Model and Numerical Scheme, Idaho National Engineering Laboratory Report No. CD-AP-TR-005.
Patnakar, V. S., 1980, Numerical Heat Transfer and Fluid Flow, Hemisphere, Washington, D.C.
Tam, V. H. Y., and Cowley, L. T., 1988, “Consequences of Pressurised LPG Releases: The Isle of Grain Full-Scale Experiments,” Proceedings of GASTECH 88, 13th International LNG/LPG Conference, Kuala Lumpur, pp. 2–25.
Richardson,  S. M., and Saville,  G., 1996, “Blowdown of LPG Pipelines, Process Environmental Protection,” Trans. Inst. Chem. Eng., 74, pp. 235–245.


Grahic Jump Location
Conjugate two-phase heat-transfer problem
Grahic Jump Location
Staggered difference scheme used for hydrodynamic model
Grahic Jump Location
Temperature histories at closed and open ends of pipeline
Grahic Jump Location
Predicted transient mass velocity profiles
Grahic Jump Location
Predicted transient void fraction profiles
Grahic Jump Location
Transient temperature distributions in the pipe wall at open and closed ends
Grahic Jump Location
Transient temperature profiles along pipeline based on the new energy equation formulation, fL/D=200
Grahic Jump Location
Discrepancy in the predictions of temperature between the simplified and rigorous heat-transfer models, fL/D=200
Grahic Jump Location
Comparison of temperature distributions along pipeline predicted by simplified and rigorous heat-transfer models, fL/D=2




Some tools below are only available to our subscribers or users with an online account.

Related Content

Customize your page view by dragging and repositioning the boxes below.

Related Journal Articles
Related eBook Content
Topic Collections

Sorry! You do not have access to this content. For assistance or to subscribe, please contact us:

  • TELEPHONE: 1-800-843-2763 (Toll-free in the USA)
  • EMAIL: asmedigitalcollection@asme.org
Sign In