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In a packed bed reactor, where the flow is turbulent, a = 0.04 kg−1, PO = 10 atm, W = 20 kg, and the equation y = (1–a • W)1/2 is applicable. Calculate the exit pressure (in atm) if the

In a packed bed reactor, where the flow is turbulent, a = 0.04 kg−1, PO = 10 atm, W = 20 kg, and the equation y = (1–a • W)1/2 is applicable. Calculate the exit pressure (in atm) if the

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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In a packed bed reactor, where the flow is turbulent, a = 0.04 kg-1, PO = 10 atm, W = %3D 20 kg, and the equation y = (1-a · W)1/2 is applicable. Calculate the exit pressure (in atm) if the catalyst particle diameter is increased by a factor of 3. Give your answer to one decimal place (without unit).
Transcribed Image Text:In a packed bed reactor, where the flow is turbulent, a = 0.04 kg-1, PO = 10 atm, W = %3D 20 kg, and the equation y = (1-a · W)1/2 is applicable. Calculate the exit pressure (in atm) if the catalyst particle diameter is increased by a factor of 3. Give your answer to one decimal place (without unit).
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