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Consider an ideal CSTR with two inlets and one outlet. Component A is fed into inlet stream 1 and component B is fed into inlet stream 2 The rate of reaction of species A is as follows: rrxn,A = KO CA L/gmol-s The reactor has the following characteristics: • The system is at a constant density of 1.12 g/cm³ • The volumetric flowrate of stream 1 is 8.4 L/s • The mass flowrate of the outlet stream is 61.8 kg/s • The entering concentration of A is 1.9 gmol/L • The entering concentration of B is 3.1 gmol/L 0.5 CB 1.5, where ko = 0.44 • The conversion of species A is 0.5, while the conversion of species B is 0.7 What is the required reactor volum

Consider an ideal CSTR with two inlets and one outlet. Component A is fed into inlet stream 1 and component B is fed into inlet stream 2 The rate of reaction of species A is as follows: rrxn,A = KO CA L/gmol-s The reactor has the following characteristics: • The system is at a constant density of 1.12 g/cm³ • The volumetric flowrate of stream 1 is 8.4 L/s • The mass flowrate of the outlet stream is 61.8 kg/s • The entering concentration of A is 1.9 gmol/L • The entering concentration of B is 3.1 gmol/L 0.5 CB 1.5, where ko = 0.44 • The conversion of species A is 0.5, while the conversion of species B is 0.7 What is the required reactor volum

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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A diagram with relevant streams and labels, List of known and unknown parameters and variables, Clear and explicit units and unit conversions, List of the governing equations, Mention of assumptions (e.g., steady-state, isothermal, constant density), Step-by-step approach from governing equations to solution.

Consider an ideal CSTR with two inlets and one outlet. Component A is fed into inlet stream 1 and component B is fed into inlet stream 2 The rate of reaction of species A is as follows: rrxn,A = KO CA L/gmol-s The reactor has the following characteristics: • The system is at a constant density of 1.12 g/cm³ • The volumetric flowrate of stream 1 is 8.4 L/s • The mass flowrate of the outlet stream is 61.8 kg/s • The entering concentration of A is 1.9 gmol/L • The entering concentration of B is 3.1 gmol/L 0.5 CB 1.5, where ko = 0.44 • The conversion of species A is 0.5, while the conversion of species B is 0.7 What is the required reactor volum
Transcribed Image Text:Consider an ideal CSTR with two inlets and one outlet. Component A is fed into inlet stream 1 and component B is fed into inlet stream 2 The rate of reaction of species A is as follows: rrxn,A = KO CA L/gmol-s The reactor has the following characteristics: • The system is at a constant density of 1.12 g/cm³ • The volumetric flowrate of stream 1 is 8.4 L/s • The mass flowrate of the outlet stream is 61.8 kg/s • The entering concentration of A is 1.9 gmol/L • The entering concentration of B is 3.1 gmol/L 0.5 CB 1.5, where ko = 0.44 • The conversion of species A is 0.5, while the conversion of species B is 0.7 What is the required reactor volum
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