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The homogeneous gas phase reaction A -> 2R is irreversible and of first scheme. At 750 K, the velocity constant has the value k = 0.10 min-1. Calculate the volume of a tube reactor that produces 1 ton R per day at 95% turnover of A, temperature 750 K and atmospheric pressure on incoming flow contains 50% A and the rest inert gas. The molecular weight of R is 200 g / mol. This question has already been answered once but i find the presentation lacking. Could the steps please be shown better and on paper, would truly be appreciated.

The homogeneous gas phase reaction A -> 2R is irreversible and of first scheme. At 750 K, the velocity constant has the value k = 0.10 min-1. Calculate the volume of a tube reactor that produces 1 ton R per day at 95% turnover of A, temperature 750 K and atmospheric pressure on incoming flow contains 50% A and the rest inert gas. The molecular weight of R is 200 g / mol. This question has already been answered once but i find the presentation lacking. Could the steps please be shown better and on paper, would truly be appreciated.

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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The homogeneous gas phase reaction A -> 2R is irreversible and of first
scheme. At 750 K, the velocity constant has the value k = 0.10 min-1.
Calculate the volume of a tube reactor that produces 1 ton R per day at 95% turnover of A, temperature 750 K and atmospheric pressure on incoming flow contains 50% A and the rest inert gas. The molecular weight of R is 200 g / mol.

This question has already been answered once but i find the presentation lacking. Could the steps please be shown better and on paper, would truly be appreciated.

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