Propane is dehydrogenated in an Isothermal batch reactor: C3Hg(g) → C3H6(g) + H2(g). Propane is fed into a 0.1 m reactor at 171 °C and absolute pressure of 42.0 atm. The reaction proceeds to 98% conversion. For calculations in this problem, assume the inlet non-ideal and the outlet ideal (even if it is not). Hydrogen: Tc = 41.3 K, Pc = 20.8 atm Propylene: Tc = 365.1 K, Pc = 45.4 atm Propane: T. = 369.9 K, Pc = 42.0 atm a. According to the conversion specified above, how many total moles are in the reactor at the end of the operation? b. What is the final reactor pressure? Was the ideal assumption appropriate?
Propane is dehydrogenated in an Isothermal batch reactor: C3Hg(g) → C3H6(g) + H2(g). Propane is fed into a 0.1 m reactor at 171 °C and absolute pressure of 42.0 atm. The reaction proceeds to 98% conversion. For calculations in this problem, assume the inlet non-ideal and the outlet ideal (even if it is not). Hydrogen: Tc = 41.3 K, Pc = 20.8 atm Propylene: Tc = 365.1 K, Pc = 45.4 atm Propane: T. = 369.9 K, Pc = 42.0 atm a. According to the conversion specified above, how many total moles are in the reactor at the end of the operation? b. What is the final reactor pressure? Was the ideal assumption appropriate?
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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Transcribed Image Text:Propane is dehydrogenated in an isothermal batch reactor: C3H8(g)→ C3H6(g) + H2(g). Propane is fed into a 0.1 m reactor at 171 °C and absolute pressure of 42.0 atm. The reaction proceeds to 98%
conversion. For calculations in this problem, assume the inlet non-ideal and the outlet ideal (even if it is not).
Hydrogen: Tc = 41.3 K, Pc = 20.8 atm
%3D
Propylene: Tc = 365.1 K, Pc = 45.4 atm
Propane: T. = 369.9 K, Pc = 42.0 atm
%3D
a. According to the conversion specified above, how many total moles are in the reactor at the end of the operation?
b. What is the final reactor pressure? Was the ideal assumption appropriate?
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