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Gas phase reactions are carried out primarily in tubular reactors where the flow is generally turbulent. For a first order reaction, the amount (W) of the catalyst can be calculated by the equation below: FA0P W kCa0 2[(1 + e)In| Where p =180 lb/ft’, C40=2 lb mol/ft’, and e = 1. X is the conversion, which must not be smaller than 0 and greater than 1. a) Create a Function M. file with the an input value of (X) b) If the input X value is less than 0 or greater than 1, warn the user and ask a new value of X between O and 1. c) After getting proper value of X, calculate the Amount of the catalyst (W) from the equation above, for different FA0 values that depends on the selected conversion of (X) with varying reaction rate constant (k) starting from 1 s'' by increasing with the step size 0.1 to 3 s'' for the feasible (X) value Conversion (X) FA0 X< 0.3 X< 0.6 0.5 0.45 X<0.8 0.4 X20.9 0.35 d) Display your results as a Table that shows the reaction rate constant (k) in the first column and Amount of catalyst (W) in the second column using “fprintf" function. e) Find the maximum amount of catalyst and make decision If maximum amount of Catalyst (W) calculated is lower than 35 lb display the scale as “LAB SCALE ", If maximum Amount of Catalyst (W) is equal or higher than 35 lb display the scale as "INDUSTRIAL SCALE" f) Plot of the Amount of catalyst (W) as a function of reaction rate constant (k) with suitable title and labels. Winc

Gas phase reactions are carried out primarily in tubular reactors where the flow is generally turbulent. For a first order reaction, the amount (W) of the catalyst can be calculated by the equation below: FA0P W kCa0 2[(1 + e)In| Where p =180 lb/ft’, C40=2 lb mol/ft’, and e = 1. X is the conversion, which must not be smaller than 0 and greater than 1. a) Create a Function M. file with the an input value of (X) b) If the input X value is less than 0 or greater than 1, warn the user and ask a new value of X between O and 1. c) After getting proper value of X, calculate the Amount of the catalyst (W) from the equation above, for different FA0 values that depends on the selected conversion of (X) with varying reaction rate constant (k) starting from 1 s'' by increasing with the step size 0.1 to 3 s'' for the feasible (X) value Conversion (X) FA0 X< 0.3 X< 0.6 0.5 0.45 X<0.8 0.4 X20.9 0.35 d) Display your results as a Table that shows the reaction rate constant (k) in the first column and Amount of catalyst (W) in the second column using “fprintf" function. e) Find the maximum amount of catalyst and make decision If maximum amount of Catalyst (W) calculated is lower than 35 lb display the scale as “LAB SCALE ", If maximum Amount of Catalyst (W) is equal or higher than 35 lb display the scale as "INDUSTRIAL SCALE" f) Plot of the Amount of catalyst (W) as a function of reaction rate constant (k) with suitable title and labels. Winc

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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Windo- Gas phase reactions are carried out primarily in tubular reactors where the flow is generally turbulent. For a first order reaction, the amount (W) of the catalyst can be calculated by the equation below: FAOP(1 + E)ln W = kCA0 Where p =180 lb/ft³, C40=2 lb mol/ft², and ɛ = 1. X is the conversion, which must not be smaller than 0 and greater than 1. a) Create a Function M. file with the an input value of (X) b) If the input X value is less than 0 or greater than 1, warn the user and ask a new value of X between O and 1. c) After getting proper value of X, calculate the Amount of the catalyst (W) from the equation above, for different FA0 Values that depends on the selected conversion of (X) with varying reaction rate constant (k) starting from 1 s'' by increasing with the step size 0.1 to 3 s'' for the feasible (X) value Conversion (X) FA0 X< 0.3 0.5 X<0.6 0.45 X<0.8 0.4 X2 0.9 0.35 d) Display your results as a Table that shows the reaction rate constant (k) in the first column and Amount of catalyst (W) in the second column using “fprintf’ function. e) Find the maximum amount of catalyst and make decision If maximum amount of Catalyst (W) calculated is lower than 35 lb display the scale as "LAB SCALE ", If maximum Amount of Catalyst (W) is equal or higher than 35 Ilb display the scale as “INDUSTRIAL SCALE" f) Plot of the Amount of catalyst (W) as a function of reaction rate constant (k) with suitable title labels. Wind
Transcribed Image Text:Windo- Gas phase reactions are carried out primarily in tubular reactors where the flow is generally turbulent. For a first order reaction, the amount (W) of the catalyst can be calculated by the equation below: FAOP(1 + E)ln W = kCA0 Where p =180 lb/ft³, C40=2 lb mol/ft², and ɛ = 1. X is the conversion, which must not be smaller than 0 and greater than 1. a) Create a Function M. file with the an input value of (X) b) If the input X value is less than 0 or greater than 1, warn the user and ask a new value of X between O and 1. c) After getting proper value of X, calculate the Amount of the catalyst (W) from the equation above, for different FA0 Values that depends on the selected conversion of (X) with varying reaction rate constant (k) starting from 1 s'' by increasing with the step size 0.1 to 3 s'' for the feasible (X) value Conversion (X) FA0 X< 0.3 0.5 X<0.6 0.45 X<0.8 0.4 X2 0.9 0.35 d) Display your results as a Table that shows the reaction rate constant (k) in the first column and Amount of catalyst (W) in the second column using “fprintf’ function. e) Find the maximum amount of catalyst and make decision If maximum amount of Catalyst (W) calculated is lower than 35 lb display the scale as "LAB SCALE ", If maximum Amount of Catalyst (W) is equal or higher than 35 Ilb display the scale as “INDUSTRIAL SCALE" f) Plot of the Amount of catalyst (W) as a function of reaction rate constant (k) with suitable title labels. Wind
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