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DIFFUSION IN SOLID CATALYSTS
with Typical Effectiveness Factor
ROLE OF PORE DIFFUSION
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activation energy adiabatic adsorption AIChE Amundson analysis assumed assumption axial boundary conditions bubble calculated Carberry carbon Catal catalyst Chapter Chem chemical cm2/sec concentration considered conversion correlation curve deactivation defined by Eq diameter diffusional dimensionless distribution Doraiswamy effective diffusivity effectiveness factor emulsion emulsion phase enzyme equation exothermic exothermic reaction experimental expression Figure first-order reaction fixed-bed reactor flow fluid fluid-bed reactor fluidized bed fluidized-bed reactor fouling fraction Froment function Fundam given gradients heat transfer coefficient Hlavacek hydrogen inlet intraparticle isothermal kinetics Kunii Levenspiel Luss maximum method micropore mixing nonisothermal o-xylene obtained operation optimum oxidation packed packed bed parameter particles Peclet number pellet plots plug-flow poisoning pore pressure Process Design Dev radial rate constant reactant reaction rate regeneration regime region represents Reynolds number Section solid solution Symp Table temperature thermal thermal conductivity Thiele modulus transport values velocity volume