Low-Liquid Loading Multiphase Flow in Natural Gas Pipelines-Reference-Cited by-同舟云学术

Low-Liquid Loading Multiphase Flow in Natural Gas Pipelines

Published:2003-11-18 Issue:4 Volume:125 Page:284-293
ISSN:0195-0738
Container-title:Journal of Energy Resources Technology
language:en
Short-container-title:

Author:

Ayala Luis F.¹,Adewumi Michael A.²

Affiliation:

1. The Pennsylvania State University, 230A Hosler Building, University Park, PA 16802-5001

2. The Pennsylvania State University, 202 Hosler Building, University Park, PA 16802-5000

Abstract

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.

Publisher

ASME International

Subject

Geochemistry and Petrology,Mechanical Engineering,Energy Engineering and Power Technology,Fuel Technology,Renewable Energy, Sustainability and the Environment

Link

http://asmedigitalcollection.asme.org/energyresources/article-pdf/125/4/284/5851836/284_1.pdf

Reference25 articles.

1. Coulter, D. M. , 1979, “New Equation Accurately Predicts Flowing Gas Temperature,” Pipeline Industry, 50(5), pp. 71–73.

2. Vincent, P. A., and Adewumi, M. A., 1990, “Engineering Design of Gas-Condensate Pipelines With a Compositional Hydrodynamic Model,” SPEPE, 5(4), pp. 381–386.

3. Ayala, L. F., 2001, “A Unified Two-Fluid Model for Multiphase Flow in Natural Gas Pipelines,” MS Thesis, Pennsylvania State U., University Park.

4. Adewumi, M. A., and Mucharam, L., 1990, “Compositional Modeling of Gas/Gas-Condensate Dispersed Flow in Gas Pipelines,” SPEPE, 5(1), pp. 85–90.

5. Chen, N. H. , 1979, “An Explicit Equation for Friction Factor in Pipe,” Ind. Eng. Chem. Fundam., 18(3), pp. 296–297.

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