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The gas phase reaction A → B+C is to be carried out isothermally at 900 K, and at 5 atm in a tubular reactor. It's required to produce 2.5 m/day of C. The reaction is irreversible and 2nd order overall with k= 1.6 dm³/mol.s at 800 K and has an activation energy of 130 kJ/mol. Assuming 60 % conversion of A and that the flow velocity in the reactor is 0.12 m/s. Calculate the length of the reactor.

The gas phase reaction A → B+C is to be carried out isothermally at 900 K, and at 5 atm in a tubular reactor. It's required to produce 2.5 m/day of C. The reaction is irreversible and 2nd order overall with k= 1.6 dm³/mol.s at 800 K and has an activation energy of 130 kJ/mol. Assuming 60 % conversion of A and that the flow velocity in the reactor is 0.12 m/s. Calculate the length of the reactor.

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
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The gas phase reaction A B + C is to be carried out isothermally at 900 K, and at 5 atm in a tubular reactor. It's required to produce 2.5 m³/day of C. The reaction is irreversible and 2nd order overall with k= 1.6 dm³/mol.s at 800 K and has an activation energy of 130 kJ/mol. Assuming 60 % conversion of A and that the flow velocity in the reactor is 0.12 m/s. Calculate the length of the reactor.
Transcribed Image Text:The gas phase reaction A B + C is to be carried out isothermally at 900 K, and at 5 atm in a tubular reactor. It's required to produce 2.5 m³/day of C. The reaction is irreversible and 2nd order overall with k= 1.6 dm³/mol.s at 800 K and has an activation energy of 130 kJ/mol. Assuming 60 % conversion of A and that the flow velocity in the reactor is 0.12 m/s. Calculate the length of the reactor.
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