Given a spherical catalyst, having a diameter of d₁ = 15mm is said to be used in a packed bed reactor. The fluid contains Cab 1.25mol of reactant A, flowing at a free stream velocity of u-0.80 m/s. Given the fluid properties: 2.5x10-11 m² Diffusivity DAB Momentum diffusivity v =! 0.78x10-6 m² a) Calculate the mass flux of A at the boundary if the reaction is external mass transfer limiting and proceeds instantaneously. b) What will be the mass flux of A at the boundary given a rate law -TAS = K, CAS; K₁ = 5.0 x10-6 m³ m²s
Given a spherical catalyst, having a diameter of d₁ = 15mm is said to be used in a packed bed reactor. The fluid contains Cab 1.25mol of reactant A, flowing at a free stream velocity of u-0.80 m/s. Given the fluid properties: 2.5x10-11 m² Diffusivity DAB Momentum diffusivity v =! 0.78x10-6 m² a) Calculate the mass flux of A at the boundary if the reaction is external mass transfer limiting and proceeds instantaneously. b) What will be the mass flux of A at the boundary given a rate law -TAS = K, CAS; K₁ = 5.0 x10-6 m³ m²s
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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