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Pipeline Design & Construction: A Practical Approach, Third EditionAvailable to Purchase
By
M. Mohitpour
M. Mohitpour
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H. Golshan
H. Golshan
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A. Murray
A. Murray
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ISBN-10:
0791802574
No. of Pages:
752
Publisher:
ASME Press
Publication date:
2007

Compression is required in gas pipelines to overcome pressure losses that occur over the length of the pipeline. Gas is generally received from receipt points along the pipeline and delivered to sales stations at specified flows and pressures. Between these points, a pressure drop occurs due to gas expansion, friction loss, a change in elevation, or a change in temperature. Altering the flow will change the pressure in the pipeline. The following methods can be applied to maintain the required pressure at an existing delivery point when there is an increase in flow rate beyond the design point:

• Loop the pipeline

• Add a compressor station

• Utilize both a loop and compression

The evaluation of the method that will be economically more feasible depends on many factors, including:

• Capital expenditures

• Fuel cost

• Emissions

• Maintenance

• Future expansions

Introduction
Types of Compressors
Compressor Drivers
Compressor Station Configuration
Thermodynamics of Isothermal and Adiabatic Gas Compression
Temperature Change in Adiabatic Gas Compression
Thermodynamics of Polytropic Gas Compression
Gas Compressors in Series
Centrifugal Compressor Horsepower
Enthalpy∕Entropy Charts (Mollier Diagram)
Centrifugal Compressor Performance Curve
Influence of Pipeline Resistance on Centrifugal Compressor Performance
Reciprocating Compressors
Gas Compression Solved Problems
Gas Coolers
Introduction
Air-Cooled Heat Exchangers
Cooler Heat Transfer Equations
Fan Air Mass Flow Rate
Required Fan Power
Gas Pressure Drop in Coolers
Iterative Procedure for Calculations Based on Unknown T2
References
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