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Calculate the reactor volume required to achieve 90% conversion in an isothermal PFR for the 2nd order irreversible reactions, 2A — В + С The feed consists of pure A at a molar flow rate of 1.2 mol/s. The reaction rate constant is 6.7 mol/s-m-³ bar2. The pressure of the reactor is 1.4 bar at the inlet, falling linearly with reactor length, to 1.0 bar at the outlet. The reactor is of uniform cross-sectional area.

Calculate the reactor volume required to achieve 90% conversion in an isothermal PFR for the 2nd order irreversible reactions, 2A — В + С The feed consists of pure A at a molar flow rate of 1.2 mol/s. The reaction rate constant is 6.7 mol/s-m-³ bar2. The pressure of the reactor is 1.4 bar at the inlet, falling linearly with reactor length, to 1.0 bar at the outlet. The reactor is of uniform cross-sectional area.

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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Calculate the reactor volume required to achieve 90% conversion in an isothermal PFR for the 2nd order irreversible reactions, 2A → B + C The feed consists of pure A at a molar flow rate of 1.2 mol/s. The reaction rate constant is 6.7 mol/s-m-3 bar-2. The pressure of the reactor is 1.4 bar at the inlet, falling linearly with reactor length, to 1.0 bar at the outlet. The reactor is of uniform cross-sectional area.
Transcribed Image Text:Calculate the reactor volume required to achieve 90% conversion in an isothermal PFR for the 2nd order irreversible reactions, 2A → B + C The feed consists of pure A at a molar flow rate of 1.2 mol/s. The reaction rate constant is 6.7 mol/s-m-3 bar-2. The pressure of the reactor is 1.4 bar at the inlet, falling linearly with reactor length, to 1.0 bar at the outlet. The reactor is of uniform cross-sectional area.
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