Elements of
Chemical Reaction Engineering
6th Edition



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Essentials of
Chemical Reaction Engineering
Second Edition

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Chapter 14 Video Screencasts

Steady-State Binary Fickian Diffusion
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This example of steady state Fickian diffusion shows a calculation of the concentration profile and the mass flow rate of octane vapor through a tube.[Section 14.2]
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Mass Transfer in a Catalyst Sphere
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This problem uses a shell balance to determine the rate of product formed with respect to time for a spherical catalyst. [Section 14.4]
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Catalytic Packed Bed Reactor
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This example uses catalyst weight in an isothermal packed bed reactor to solve mole balance. [Section 14.4]
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Diffusion and Bulk Flow for Catalytic Reaction
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This example calculates the concentration profile and the flux to a catalyst surface that is covered by a porous layer. The reaction has a mole change therefore bulk flow is taken into account. [Section 14.4]
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Diffusion and Reaction in a Cylindrical Porous Catalyst
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This example examines a concentration gradient in a porous cylindrical catalyst pellet, and determines the amount reacting within the cylinder. [Section 14.4]
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