Evaluating the Effective Friction Factor and Overall Heat Transfer Coefficient During Unsteady Pipeline Operation

[+] Author and Article Information
G. R. Price, R. K. McBrien

Fluid Dynamics Group, NOVA Research & Technology Corporation, 2928-16th Street N.E., Calgary, Alberta T2E 7K7, Canada

S. N. Rizopoulos, H. Golshan

System Design, TransCanada Pipelines Ltd., Calgary, Alberta T2P 2N6, Canada

J. Offshore Mech. Arct. Eng 121(2), 131-136 (May 01, 1999) (6 pages) doi:10.1115/1.2830078 History: Received April 01, 1998; Revised December 24, 1998; Online December 17, 2007


This paper presents a method to determine the effective friction factor and overall heat transfer coefficient for a high-pressure, natural gas pipeline during fully transient flow conditions. Time-varying SCADA (supervisory control and data acquisition) measurements at the pipeline boundaries (i.e., inlet and outlet) provide boundary conditions for a transient flow model, as well as additional information which is utilized to determine these parameters. The resulting friction factor and overall heat transfer coefficient minimize the least-squared difference between the additional SCADA measurements at the pipeline outlet and the corresponding values predicted from the transient flow model. This concept is referred to as parameter estimation. The transient flow model is based on a numerical solution of the one-dimensional conservation equations (i.e., continuity, momentum, and energy) which are discretized using a highly accurate compact finite-difference scheme. The transient flow model and parameter estimation is incorporated into a computer program that is initially tested on a simple pipeline with steady flow conditions. The predicted outlet pressure and temperature using the estimated friction factor and overall heat transfer coefficient exactly matches the corresponding prescribed values. Subsequently, a portion of the Foothills Pipe Line Ltd. transmission system in Alberta is considered using time-varying SCADA flow measurements. The resulting outlet pressure and temperature from the transient flow model are in good agreement with SCADA measurements for this pipeline section.

Copyright © 1999 by The American Society of Mechanical Engineers
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