A gas condensate transmission line transports 263 MMSCF/day of gas from a processing plant to a compressor station site 15 Miles away. The maximum pipe operating pressure is limited to 1232 Psia. The delivery pressure desired at the end of the pipeline is a minimum of 800 Psia, the gas temperature is 600 Rº and the pipeline efficiency of 0.9, a) Calculate the pipeline diameter required using the IGT, and Panhandle B equations. b) Explain the effect of increasing pipeline diameter on outlet pressure, assuming the flow rate and inlet pressure remain constant?

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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A gas condensate transmission line transports 263 MMSCF/day of gas from a processing
plant to a compressor station site 15 Miles away. The maximum pipe operating pressure is
limited to 1232 Psia. The delivery pressure desired at the end of the pipeline is a minimum
of 800 Psia, the gas temperature is 600 Rº and the pipeline efficiency of 0.9,
a) Calculate the pipeline diameter required using the IGT, and Panhandle B equations.
b) Explain the effect of increasing pipeline diameter on outlet pressure, assuming the flow
rate and inlet pressure remain constant?
Hints:
1- Base pressure
= 14.7 psia and base temperature = 60 Fº.
2- The specific gravity throughout all questions is equal of 0.7.
3- Use Lee method to calculate the viscosity throughout all questions.
Transcribed Image Text:A gas condensate transmission line transports 263 MMSCF/day of gas from a processing plant to a compressor station site 15 Miles away. The maximum pipe operating pressure is limited to 1232 Psia. The delivery pressure desired at the end of the pipeline is a minimum of 800 Psia, the gas temperature is 600 Rº and the pipeline efficiency of 0.9, a) Calculate the pipeline diameter required using the IGT, and Panhandle B equations. b) Explain the effect of increasing pipeline diameter on outlet pressure, assuming the flow rate and inlet pressure remain constant? Hints: 1- Base pressure = 14.7 psia and base temperature = 60 Fº. 2- The specific gravity throughout all questions is equal of 0.7. 3- Use Lee method to calculate the viscosity throughout all questions.
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