7.51. Liquid benzene at 25°C and 1.2 bar is converted to vapor at 200°C and 5 bar in a two-step steady-flow process: vaporization in a counterflow heat exchanger at 1.2 bar, followed by compression as a gas to 5 bar. Determine the duty of the exchanger and the power requirement of the compressor in kJ mol-¹. Assume a compressor efficiency of 75%, and treat benzene vapor as an ideal gas with constant Cp 105 J-mol-1.K-1 =
7.51. Liquid benzene at 25°C and 1.2 bar is converted to vapor at 200°C and 5 bar in a two-step steady-flow process: vaporization in a counterflow heat exchanger at 1.2 bar, followed by compression as a gas to 5 bar. Determine the duty of the exchanger and the power requirement of the compressor in kJ mol-¹. Assume a compressor efficiency of 75%, and treat benzene vapor as an ideal gas with constant Cp 105 J-mol-1.K-1 =
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
Question
![7.51. Liquid benzene at 25°C and 1.2 bar is converted to vapor at 200°C and 5 bar in
a two-step steady-flow process: vaporization in a counterflow heat exchanger at
1.2 bar, followed by compression as a gas to 5 bar. Determine the duty of the
exchanger and the power requirement of the compressor in kJ mol-¹. Assume a
compressor efficiency of 75%, and treat benzene vapor as an ideal gas with constant
Cp 105 J-mol-1.K-1
=](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F24a6ad28-6ecb-4e08-a399-67171c1fe08f%2F39934505-a5f8-4dd1-9d46-dded11761e5d%2Frhjlswm_processed.png&w=3840&q=75)
Transcribed Image Text:7.51. Liquid benzene at 25°C and 1.2 bar is converted to vapor at 200°C and 5 bar in
a two-step steady-flow process: vaporization in a counterflow heat exchanger at
1.2 bar, followed by compression as a gas to 5 bar. Determine the duty of the
exchanger and the power requirement of the compressor in kJ mol-¹. Assume a
compressor efficiency of 75%, and treat benzene vapor as an ideal gas with constant
Cp 105 J-mol-1.K-1
=
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