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12. Reactor design

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Product-Driven Process Design
This chapter is in the book Product-Driven Process Design
12 Reactordesign12.1 EssenceofreactorsThe conversion of feed to products is the essence of a chemical process and, thus,the reactor is the heart of a chemical plant. When designing a reactor, an engineermustfirstcollectdataaboutthechemicalreactionandthenselectappropriatereac-tionconditions,whichwillhelpdeterminesuitablematerialsofconstruction.Next,thedesignershoulddeterminetheratelimitingstepand,fromthis,thecriticalsizingparameter.Next,preliminarysizing,layoutandcostingcanbeconductedforthere-actor.Atthispoint,simulationsandexperimentscanbeconductedtoverifythattheproposedreactorwillmeetthedesiredspecifications.Thedesignisoptimizeduntilthesetargetsaremet.Throughoutthedesignprocess,itisimportantfortheengineertoconsiderthemostappropriatetypeofreactortouse,anymixingorheattransferequipmentthatmustbeaddedandsafetyconsiderations.ThischapterfollowsTowlerandSinnott(2013)andtheopenprocessdesigntex-booktoalargeextent.12.2 Idealreactors12.2.1 BatchreactorsIn a batch reactor, the reagents are added together and allowed to react for a givenamountoftime.Thecompositionschangewithtime,butthereisnoflowthroughtheprocess.Additionalreagentsmaybeaddedasthereactionproceeds,andchangesintemperaturemayalsobemade.Productsareremovedfromthereactorafterthereac-tionhasproceededtocompletion.Batchprocessesaresuitableforsmall-scaleproduction(lessthan1,000,000lb/yr)and for processes where several different products or grades are to be produced inthesameequipment(Douglas,1988).Whenproductionvolumesarerelativelysmalland/orthechemistryisrelativelycomplex,batchprocessingprovidesanimportantmeansofqualitycontrol.12.2.2 Plugflowreactor(PFR)Aplugflowreactor(PFR)withtubulargeometryhasperfectradialmixingbutnoaxialmixing.Allmaterialshavethesameresidencetime,τ,andexperiencethesametem-peratureandconcentrationprofilesalongthereactor.TheequationforPFRsisgivenbydM=rdV,(12.1)https://doi.org/10.1515/9783110570137-012
© 2020 Walter de Gruyter GmbH, Berlin/Munich/Boston

12 Reactordesign12.1 EssenceofreactorsThe conversion of feed to products is the essence of a chemical process and, thus,the reactor is the heart of a chemical plant. When designing a reactor, an engineermustfirstcollectdataaboutthechemicalreactionandthenselectappropriatereac-tionconditions,whichwillhelpdeterminesuitablematerialsofconstruction.Next,thedesignershoulddeterminetheratelimitingstepand,fromthis,thecriticalsizingparameter.Next,preliminarysizing,layoutandcostingcanbeconductedforthere-actor.Atthispoint,simulationsandexperimentscanbeconductedtoverifythattheproposedreactorwillmeetthedesiredspecifications.Thedesignisoptimizeduntilthesetargetsaremet.Throughoutthedesignprocess,itisimportantfortheengineertoconsiderthemostappropriatetypeofreactortouse,anymixingorheattransferequipmentthatmustbeaddedandsafetyconsiderations.ThischapterfollowsTowlerandSinnott(2013)andtheopenprocessdesigntex-booktoalargeextent.12.2 Idealreactors12.2.1 BatchreactorsIn a batch reactor, the reagents are added together and allowed to react for a givenamountoftime.Thecompositionschangewithtime,butthereisnoflowthroughtheprocess.Additionalreagentsmaybeaddedasthereactionproceeds,andchangesintemperaturemayalsobemade.Productsareremovedfromthereactorafterthereac-tionhasproceededtocompletion.Batchprocessesaresuitableforsmall-scaleproduction(lessthan1,000,000lb/yr)and for processes where several different products or grades are to be produced inthesameequipment(Douglas,1988).Whenproductionvolumesarerelativelysmalland/orthechemistryisrelativelycomplex,batchprocessingprovidesanimportantmeansofqualitycontrol.12.2.2 Plugflowreactor(PFR)Aplugflowreactor(PFR)withtubulargeometryhasperfectradialmixingbutnoaxialmixing.Allmaterialshavethesameresidencetime,τ,andexperiencethesametem-peratureandconcentrationprofilesalongthereactor.TheequationforPFRsisgivenbydM=rdV,(12.1)https://doi.org/10.1515/9783110570137-012
© 2020 Walter de Gruyter GmbH, Berlin/Munich/Boston
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