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Catalyst Design: Optimal Distribution of Catalyst in Pellets, Reactors, and Membranes (Cambridge Series in Chemical Engineering) PDF

240 Pages·2005·2.998 MB·English
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Catalyst Design Heterogeneouscatalysisiswidelyusedinchemical,refinery,andpollution- controlprocesses.Forthisreason,achievingoptimalperformanceofcat- alystsisasignificantissueforchemicalengineersandchemists.Thisbook addresses the question of how catalytic material should be distributed insideaporoussupportinordertoobtainoptimalperformance.Ittreats single-andmultiple-reactionsystems,isothermalandnonisothermalcon- ditions, pellets, monoliths, fixed-bed reactors, and membrane reactors. Theeffectsofphysicochemicalandoperatingparametersareanalyzedto gaininsightintotheunderlyingphenomenagoverningtheperformance ofoptimallydesignedcatalysts.Throughout,theauthorsofferabalanced treatmentoftheoryandexperiment.Particularattentionisgiventoprob- lems of commercial importance. With its thorough treatment of the de- sign, preparation, and utilization of supported catalysts, this book will be a useful resource for graduate students, researchers, and practicing engineersandchemists. Massimo Morbidelli is Professor of Chemical Reaction Engineering in theLaboratoriumfu¨rTechnischeChemieatETH,Zu¨rich. Asterios Gavriilidis is Senior Lecturer in the Department of Chemical EngineeringatUniversityCollegeLondon. Arvind Varma is the Arthur J. Schmitt Professor in the Department of ChemicalEngineeringattheUniversityofNotreDame. CAMBRIDGE SERIES IN CHEMICAL ENGINEERING SeriesEditor: ArvindVarma,UniversityofNotreDame EditorialBoard: AlexisT.Bell,UniversityofCalifornia,Berkeley JohnBridgwater,UniversityofCambridge RobertA.Brown,MIT L.GaryLeal,UniversityofCalifornia,SantaBarbara MassimoMorbidelli,ETH,Zurich StanleyI.Sandler,UniversityofDelaware MichaelL.Shuler,CornellUniversity ArthurW.Westerberg,CarnegieMellonUniversity BooksintheSeries: E.L.Cussler,Diffusion:MassTransferinFluidSystems,secondedition Liang-ShihFanandChaoZhu,PrinciplesofGas-SolidFlows HasanOrbeyandStanleyI.Sandler,ModelingVapor-LiquidEquilibria: CubicEquationsofStateandTheirMixingRules T.MichaelDuncanandJeffreyA.Reimer,ChemicalEngineeringDesign andAnalysis:AnIntroduction A.Varma,M.MorbidelliandH.Wu,ParametricSensitivityinChemical Systems JohnC.Slattery,AdvancedTransportPhenomena M. Morbidelli, A. Gavriilidis and A. Varma, Catalyst Design: Optimal DistributionofCatalystinPellets,Reactors,andMembranes Catalyst Design OPTIMAL DISTRIBUTION OF CATALYST IN PELLETS, REACTORS, AND MEMBRANES Massimo Morbidelli ETH,Zurich Asterios Gavriilidis UniversityCollegeLondon Arvind Varma UniversityofNotreDame To our teachers and students CAMBRIDGE UNIVERSITY PRESS Cambridge, New York, Melbourne, Madrid, Cape Town, Singapore, São Paulo Cambridge University Press The Edinburgh Building, Cambridge CB2 2RU, UK Published in the United States of America by Cambridge University Press, New York www.cambridge.org Information on this title: www.cambridge.org/9780521660594 © Cambridge University Press 2001 This publication is in copyright. Subject to statutory exception and to the provisions of relevant collective licensing agreements, no reproduction of any part may take place without the written permission of Cambridge University Press. First published 2001 This digitally printed first paperback version 2005 A catalogue record for this publication is available from the British Library Library of Congress Cataloguing in Publication data Morbidelli, Massimo. Catalyst design : optimal distribution of catalyst in pellets, reactors, and membranes / Massimo Morbidelli, Asterios Gavriilidis, Arvind Varma. p. cm. – (Cambridge series in chemical engineering) Includes bibliographical references. ISBN 0-521-66059-9 1. Catalysts. I. Gavriilidis, Asterios, 1965– II. Varma, Arvind. III. Title. IV. Series. TP159.C3 M62 2001 660´.2995 – dc21 00-041460 ISBN-13 978-0-521-66059-4 hardback ISBN-10 0-521-66059-9 hardback ISBN-13 978-0-521-01985-9 paperback ISBN-10 0-521-01985-0 paperback Contents Preface page xiii 1 Introduction 1 1.1 ImportanceofCatalysis 1 1.2 NonuniformCatalystDistributions 1 1.3 OverviewofBookContents 4 2 Optimization of the Catalyst Distribution in a Single Pellet 6 2.1 TheCaseofaSingleReaction 6 2.1.1 IsothermalConditions 6 2.1.2 NonisothermalConditions 15 2.1.3 ArbitraryKineticswithExternalTransportResistances 18 2.1.4 DynamicBehavior 23 2.2 MultipleReactions 25 2.2.1 IsothermalConditions 25 2.2.2 NonisothermalConditions 28 2.3 TheGeneralCaseofaComplexReactionSystem 30 2.3.1 AnIllustrativeExample 31 2.3.2 GeneralReactionSystem 35 2.4 CatalystDispersionConsiderations 40 2.4.1 FactorsAffectingCatalystDispersion 40 2.4.2 DependenceofCatalyticSurfaceAreaonCatalystLoading 43 2.5 OptimalDistributionofCatalystLoading 46 2.5.1 TheProblemFormulation 47 2.5.2 ASingleFirst-OrderIsothermalReaction 51 2.5.3 LinearDependencebetweentheActiveElementSurface AreaandItsLoading 54 2.5.4 First-OrderNonisothermalReactions:NumericalOptimization 55 2.5.5 MultistepOptimalLoadingDistribution 59 2.6 ExperimentalStudies 63 2.6.1 OxidationReactions 63 2.6.2 HydrogenationReactions 66 2.6.3 Fischer–TropschSynthesis 68 vii viii Contents 3 Optimization of the Catalyst Distribution in a Reactor 69 3.1 ASingleReaction 69 3.1.1 IsothermalConditions 69 3.1.2 NonisothermalConditions 75 3.2 MultipleReactions 77 3.2.1 IsothermalConditions 77 3.2.2 NonisothermalConditions 79 3.3 ExperimentalStudies 83 3.3.1 PropaneandCOOxidation 83 3.3.2 CatalyticIncinerationofVolatileOrganicCompounds 85 4 Studies Involving Catalyst Deactivation 86 4.1 NonselectivePoisoning 86 4.2 SelectivePoisoning 89 4.3 ExperimentalStudies 91 4.3.1 Methanation 91 4.3.2 Hydrogenation 92 4.3.3 NOReduction 94 5 Membrane Reactors 95 5.1 MembraneReactorswithNonuniformCatalystDistribution 95 5.2 OptimalCatalystDistributioninPelletsforan InertMembraneReactor 100 5.3 OptimalCatalystDistributioninaCatalyticMembraneReactor 100 5.4 ExperimentalStudies 102 5.4.1 DehydrogenationReactions 102 5.4.2 PreparationofCatalyticMembranes 105 6 Special Topics of Commercial Importance 110 6.1 AutomotiveExhaustCatalysts 110 6.1.1 DesignofLayeredCatalysts 111 6.1.2 NonuniformAxialCatalystDistribution 113 6.2 HydrotreatingCatalysts 115 6.3 CompositeZeoliteCatalysts 119 6.4 ImmobilizedBiocatalysts 121 6.5 FunctionalizedPolymerResins 124 6.5.1 PreparationofNonuniformlyFunctionalizedResinParticles 124 6.5.2 ApplicationstoReactingSystems 126 7 Preparation of Pellets with Nonuniform Distribution of Catalyst 131 7.1 AdsorptiononPowders 132 7.1.1 AdsorptionIsothermModels 132 7.1.2 EffectofImpregnationVariablesonAdsorption 135 7.1.2.a SolutionpHandNatureofSupport 135 7.1.2.b SurfaceHeterogeneity 138 7.1.2.c IonicStrength 140 7.1.2.d PrecursorSpeciation 140 7.1.2.e Coimpregnants 142 7.1.2.f NatureoftheSolvent 144 7.1.3 SurfaceIonizationModels 144 7.1.3.a Constant-CapacitanceModel 145 Contents ix 7.1.3.b Diffuse-LayerModel 146 7.1.3.c BasicSternModel 147 7.1.3.d Triple-LayerModel 147 7.1.3.e Four-Layermodel 149 7.2 SimultaneousDiffusionandAdsorptioninPellets 149 7.2.1 TheoreticalStudies 150 7.2.1.a DryImpregnation 150 7.2.1.b WetImpregnation 153 7.2.1.c EffectsofElectrokineticandIonicDissociationPhenomena 156 7.2.1.d EffectofDryingConditions 156 7.2.2 ExperimentalStudies 158 7.2.2.a Single-ComponentImpregnation 159 7.2.2.b MulticomponentImpregnation 161 7.2.2.c EffectsofDrying 165 7.2.2.d DeterminationofCatalystDistribution 169 7.2.3 ComparisonofModelCalculationswithExperimentalStudies 169 7.2.3.a DryImpregnation 169 7.2.3.b WetImpregnation 171 AppendixA:ApplicationoftheMaximumPrincipleforOptimization ofaCatalystDistribution 181 AppendixB:OptimalCatalystDistributioninPelletsforanInert MembraneReactor:ProblemFormulation 188 B.1 TheMassandEnergyBalanceEquations 188 B.2 ThePerformanceIndexes 191 B.3 DevelopmentoftheHamiltonian 192 Notation 195 References 201 AuthorIndex 221 SubjectIndex 225

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