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Q1] An irreversible reaction must be carried separately in PFR and CSTR reactors. Calculate the volumes of each reactor. The kinetics data are provided, and the feed flow is 2.0 m3/min. Its pressure is 1 atm at 300°C. The reactant is introduced with 30% inert into the reactor. XA 0 0.2 0.4 0.6 (-A) mol/(L s) 0.01 0.005 0.002 0.001 (15 marks)

Q1] An irreversible reaction must be carried separately in PFR and CSTR reactors. Calculate the volumes of each reactor. The kinetics data are provided, and the feed flow is 2.0 m3/min. Its pressure is 1 atm at 300°C. The reactant is introduced with 30% inert into the reactor. XA 0 0.2 0.4 0.6 (-A) mol/(L s) 0.01 0.005 0.002 0.001 (15 marks)

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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Q1] An irreversible reaction must be carried separately in PFR and CSTR reactors. Calculate the volumes of each reactor. The kinetics data are provided, and the feed flow is 2.0 m3/min. Its pressure is 1 atm at 300°C. The reactant is introduced with 30% inert into the reactor. XA 0 0.2 0.4 0.6 (-A) mol/(L s) 0.01 0.005 0.002 0.001 (15 marks)
Transcribed Image Text:Q1] An irreversible reaction must be carried separately in PFR and CSTR reactors. Calculate the volumes of each reactor. The kinetics data are provided, and the feed flow is 2.0 m3/min. Its pressure is 1 atm at 300°C. The reactant is introduced with 30% inert into the reactor. XA 0 0.2 0.4 0.6 (-A) mol/(L s) 0.01 0.005 0.002 0.001 (15 marks)
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