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Under ultraviolet radiation, reactant A of CAo = 10 kmolm³ in a process stream (v =1 m³/min) decomposes as follows. R, 'R = 16C5 kmol/m³-min R– desired product %3D Is = 12CA 7= C S, kmol/m-min T, kmol/m³-min We wish to design a reactor setup for a specific duty. Sketch the scheme selected, and calculate the fraction of feed transformed into desired produet as well as the volume of reactor needed.

Under ultraviolet radiation, reactant A of CAo = 10 kmolm³ in a process stream (v =1 m³/min) decomposes as follows. R, 'R = 16C5 kmol/m³-min R– desired product %3D Is = 12CA 7= C S, kmol/m-min T, kmol/m³-min We wish to design a reactor setup for a specific duty. Sketch the scheme selected, and calculate the fraction of feed transformed into desired produet as well as the volume of reactor needed.

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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Under ultraviolet radiation, reactant A of CAo = 10 kmolm³ in a process stream (v =1 m³/min) decomposes as follows. R, TR = 16C5 kmol/m³-min R– desired product %3D S, Is = 12C, kmol/m-min T, 7= C kmol/m³-min We wish to design a reactor setup for a specific duty. Sketch the scheme selected, and caleulate the fraction of feed transformed into desired product as well as the volume of reactor needed.
Transcribed Image Text:Under ultraviolet radiation, reactant A of CAo = 10 kmolm³ in a process stream (v =1 m³/min) decomposes as follows. R, TR = 16C5 kmol/m³-min R– desired product %3D S, Is = 12C, kmol/m-min T, 7= C kmol/m³-min We wish to design a reactor setup for a specific duty. Sketch the scheme selected, and caleulate the fraction of feed transformed into desired product as well as the volume of reactor needed.
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