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(a) Write out each step of the algorithm.

(a) Write out each step of the algorithm.

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 reversible gas-phase elementary reaction CH₂ CH₂ (a) Write out each step of the algorithm. + H₂ (ethylbenzene styrene + H₂) is carried out in an isothermal CSTR with no pressure drop. The feed enters a volumetric flow rate of vo = 5000 dm³/hour. The feed consists of half ethyl benzene (species A) and half interts on a molar basis and is well mixed before it enters the reactor (I). The pressure in the reactor is 6 atm (so PA0 = 3 atm and P10 = 3 atm, making the initial concentration of A = 0.04 mol/dm^3). The molar flow rate of A is FAO = 200 mol/hr. At the reaction temperature of 640 C, the rate constant isk₁= 5.92 mol/ (dm³ hr * Atm). The equilibrium constant is Kf = 9 atm and the equilibrium conversion is X₂ = * 0.84.
Transcribed Image Text:The reversible gas-phase elementary reaction CH₂ CH₂ (a) Write out each step of the algorithm. + H₂ (ethylbenzene styrene + H₂) is carried out in an isothermal CSTR with no pressure drop. The feed enters a volumetric flow rate of vo = 5000 dm³/hour. The feed consists of half ethyl benzene (species A) and half interts on a molar basis and is well mixed before it enters the reactor (I). The pressure in the reactor is 6 atm (so PA0 = 3 atm and P10 = 3 atm, making the initial concentration of A = 0.04 mol/dm^3). The molar flow rate of A is FAO = 200 mol/hr. At the reaction temperature of 640 C, the rate constant isk₁= 5.92 mol/ (dm³ hr * Atm). The equilibrium constant is Kf = 9 atm and the equilibrium conversion is X₂ = * 0.84.
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