At 3.45MPA T/°C H, kJ/kg S, kJ/kgK 38 949.6 5.264 150 1236.7 6.041 155 1250.3 6.075 160 1263.9 6.108 165 1277.5 6.139 170 1291.1 6.169 175 1304.8 6.199 180 1318.4 6.227 185 1332 6.253
At 3.45MPA T/°C H, kJ/kg S, kJ/kgK 38 949.6 5.264 150 1236.7 6.041 155 1250.3 6.075 160 1263.9 6.108 165 1277.5 6.139 170 1291.1 6.169 175 1304.8 6.199 180 1318.4 6.227 185 1332 6.253
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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Methane gas is compressed at the rate of 3x104 m3/hr (as measured at 0.1013MPa and 15°C) from 0.69MPa and 26.7°C to 3.45MPa. The compressor operates adiabatically and has an efficiency of 80% compared with isentropic compression. After compression the methane is cooled at a constant pressure of 3.45MPa to a temperature of 38°C. What is the power requirement of the compressor and what is the rate of heat removal in the cooler?
Data from Methane
At 0.69MPa and 26.7°C: H=946.7kJ/kg, S = 6.071kJ/kgK
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