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Dispersion Langmuir-Hinshelwood model

Problem. Think about the overall strategy that must be implemented to account for the effect of interpellet axial dispersion on ihe outlet concentration of reactant A when Langmuir-Hinshelwood kinetics and Hougen-Watson models are operative in a packed catalytic tubular reactor. Residence-time distribution effects are important at small mass transfer Peclet numbers. [Pg.592]


See other pages where Dispersion Langmuir-Hinshelwood model is mentioned: [Pg.499]    [Pg.263]    [Pg.499]    [Pg.619]    [Pg.284]    [Pg.901]    [Pg.365]    [Pg.144]    [Pg.36]   
See also in sourсe #XX -- [ Pg.65 , Pg.70 , Pg.235 , Pg.415 , Pg.641 , Pg.642 , Pg.652 , Pg.653 , Pg.654 , Pg.655 , Pg.661 ]




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