1). The irreversible, elementary gas phase reaction shown below is carried out in an isothermal, isobaric CSTR reactor. Calculate the volume of the reactor that reaches conversion equal to 80%. A B C -ra = k CA Data: yaº = 1/2., k = 0.1 s¹, FA° = 2 mol/s, CA° = 1 mol/liter 2). The elementary gas phase reaction A-2B+2C , -TA = K CA It is carried out isothermally in a flow reactor with no change in pressure. Pure A enters the reactor at 10 atm and 127 °C and a molar flow of 2 mol/min. If you want to achieve 90% conversion calculate: a) The stochiometric table, b) The values of 8 and ε, c) The output volume flow.
1). The irreversible, elementary gas phase reaction shown below is carried out in an isothermal, isobaric CSTR reactor. Calculate the volume of the reactor that reaches conversion equal to 80%. A B C -ra = k CA Data: yaº = 1/2., k = 0.1 s¹, FA° = 2 mol/s, CA° = 1 mol/liter 2). The elementary gas phase reaction A-2B+2C , -TA = K CA It is carried out isothermally in a flow reactor with no change in pressure. Pure A enters the reactor at 10 atm and 127 °C and a molar flow of 2 mol/min. If you want to achieve 90% conversion calculate: a) The stochiometric table, b) The values of 8 and ε, c) The output volume flow.
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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Answer question 1 & 2
Transcribed Image Text:1). The irreversible, elementary gas phase reaction shown below is carried out in an
isothermal, isobaric CSTR reactor. Calculate the volume of the reactor that reaches
conversion equal to 80%.
A B C
-ra = k CA
Data: yaº = 1/2., k = 0.1 s¹, FA° = 2 mol/s, CA° = 1 mol/liter
2). The elementary gas phase reaction
A-2B+2C
, -TA = K CA
It is carried out isothermally in a flow reactor with no change in pressure. Pure A
enters the reactor at 10 atm and 127 °C and a molar flow of 2 mol/min. If you want to
achieve 90% conversion calculate:
a) The stochiometric table,
b) The values of 8 and ε,
c) The output volume flow.
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