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(4) 0.2 mol/s of CO2 at 370 K and 2 bars is adiabatically and reversibly compressed in a steady flow system to 20 bars. Find the outlet temperature (K) of the CO2 and the power required (kW) assuming it follows the equation of state: Z = 1+ P(a/T - b/T².6) where a = 0.342 K/bar and b = 16340 K²-/bar Use the ideal gas heat capacity given in Problem 1.

(4) 0.2 mol/s of CO2 at 370 K and 2 bars is adiabatically and reversibly compressed in a steady flow system to 20 bars. Find the outlet temperature (K) of the CO2 and the power required (kW) assuming it follows the equation of state: Z = 1+ P(a/T - b/T².6) where a = 0.342 K/bar and b = 16340 K²-/bar Use the ideal gas heat capacity given in Problem 1.

Introduction to Chemical Engineering Thermodynamics
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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(4) 0.2 mol/s of CO2 at 370 K and 2 bars is adiabatically and reversibly compressed in a steady flow system to 20 bars. Find the outlet temperature (K) of the CO2 and the power required (kW) assuming it follows the equation of state: Z = 1+ P(a/T - b/T2.6) where a = 0.342 K/bar and b = 16340 K?.6/bar Use the ideal gas heat capacity given in Problem 1.
Transcribed Image Text:(4) 0.2 mol/s of CO2 at 370 K and 2 bars is adiabatically and reversibly compressed in a steady flow system to 20 bars. Find the outlet temperature (K) of the CO2 and the power required (kW) assuming it follows the equation of state: Z = 1+ P(a/T - b/T2.6) where a = 0.342 K/bar and b = 16340 K?.6/bar Use the ideal gas heat capacity given in Problem 1.
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