Pressure and temperature variations of natural gas flows in a pipeline may cause partial gas condensation. Fluid phase behavior and prevailing conditions often make liquid appearance inevitable, which subjects the pipe flow to a higher pressure loss. This study focuses on the hydrodynamic behavior of the common scenarios that may occur in natural gas pipelines. For this purpose, a two-fluid model is used. The expected flow patterns as well as their transitions are modeled with emphasis on the low-liquid loading character of such systems. In addition, the work re-examines previous implementations of two-flow model for gas-condensate flow.
Low-Liquid Loading Multiphase Flow in Natural Gas Pipelines
Contributed by the Petroleum Division and presented at the ETCE 2002, Houston, TX, February 4–6, 2002 of THE AMERICAN SOCIETY OF MECHANICAL ENGINEERS. Manuscript received by the Petroleum Division, Jul. 2002; revised manuscript received Jun. 2003. Associate Editor: S. A. Shirazi.
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Ayala, L. F., and Adewumi, M. A. (November 18, 2003). "Low-Liquid Loading Multiphase Flow in Natural Gas Pipelines ." ASME. J. Energy Resour. Technol. December 2003; 125(4): 284–293. https://doi.org/10.1115/1.1616584
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