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We will using the 7 solving strategies to analyze the size of a CSTR with the following liquid phase, irreversible elementary reaction at steady-state: 2A - B(liquid, steady-state) Given that v = 400 L/h, Can= 1 mol/L, k = 0.1 L mor hr, determine the conversion in the CSTR reactor needed to produce 100 mol/hr of B (no B enters the reactor). Hint The design equation is not needed yet (how else can calculate conversion?). Given that v, =400 L/h, CA0 =1 mol/L, k =0.1 L mol hr', (i.e., same conditions) determine the volume of the CSTR reactor needed to produce 100 mol/hr of B (no B enters).

We will using the 7 solving strategies to analyze the size of a CSTR with the following liquid phase, irreversible elementary reaction at steady-state: 2A - B(liquid, steady-state) Given that v = 400 L/h, Can= 1 mol/L, k = 0.1 L mor hr, determine the conversion in the CSTR reactor needed to produce 100 mol/hr of B (no B enters the reactor). Hint The design equation is not needed yet (how else can calculate conversion?). Given that v, =400 L/h, CA0 =1 mol/L, k =0.1 L mol hr', (i.e., same conditions) determine the volume of the CSTR reactor needed to produce 100 mol/hr of B (no B enters).

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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We will using the 7 solving strategies to analyze the size of a CSTR with the following liquid phase, irreversible elementary reaction at steady-state: 2A - B(liquid, steady-state) Given that vo = 400 L/h, CA0 = 1 mol/L, k = 0.1 L mol hr, determine the conversion in the CSTR reactor needed to produce 100 mol/hr of B (no B enters the reactor). Hint: The design equation is not needed yet (how else can calculate conversion?). Given that vo =400 L/h, CA0 =1 mol/L, k =0.1 L mol hr', (i.e., same conditions) determine the volume of the CSTR reactor needed to produce 100 mol/hr of B (no B enters).
Transcribed Image Text:We will using the 7 solving strategies to analyze the size of a CSTR with the following liquid phase, irreversible elementary reaction at steady-state: 2A - B(liquid, steady-state) Given that vo = 400 L/h, CA0 = 1 mol/L, k = 0.1 L mol hr, determine the conversion in the CSTR reactor needed to produce 100 mol/hr of B (no B enters the reactor). Hint: The design equation is not needed yet (how else can calculate conversion?). Given that vo =400 L/h, CA0 =1 mol/L, k =0.1 L mol hr', (i.e., same conditions) determine the volume of the CSTR reactor needed to produce 100 mol/hr of B (no B enters).
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