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dc.contributor.editorSantacesaria, Elio
dc.contributor.editorTesser, Riccardo
dc.contributor.editorRusso, Vincenzo
dc.date.accessioned2022-06-21T08:37:39Z
dc.date.available2022-06-21T08:37:39Z
dc.date.issued2022
dc.identifierONIX_20220621_9783036541556_52
dc.identifier.urihttps://directory.doabooks.org/handle/20.500.12854/84474
dc.description.abstractNowadays, the impressive progress of commercially available computers allows us to solve complicated mathematical problems in many scientific and technical fields. This revolution has reinvigorated all aspects of chemical engineering science. More sophisticated approaches to catalysis, kinetics, reactor design, and simulation have been developed thanks to the powerful calculation methods that have recently become available. It is well known that many chemical reactions are of great interest for industrial processes and must be conducted on a large scale in order to obtain needed information in thermodynamics, kinetics, and transport phenomena related to mass, energy, and momentum. For a reliable industrial-scale reactor design, all of this information must be employed in appropriate equations and mathematical models that allow for accurate and reliable simulations for scaling up purposes. The aim of this proposed Special Issue was to collect worldwide contributions from experts in the field of industrial reactor design based on kinetic and mass transfer studies. The following areas/sections were covered by the call for original papers: Kinetic studies on complex reaction schemes (multiphase systems); Kinetics and mass transfer in multifunctional reactors; Reactions in mass transfer-dominated regimes (fluid–solid and intraparticle diffusive limitations); Kinetic and mass transfer modeling using alternative approaches (ex. stochastic modeling); Simulations in pilot plants and industrial-sized reactors and scale-up studies based on kinetic studies (lab-to-plant approach).
dc.languageEnglish
dc.subject.classificationthema EDItEUR::T Technology, Engineering, Agriculture, Industrial processes::TB Technology: general issuesen_US
dc.subject.otherheat exchanger
dc.subject.othermathematical model
dc.subject.otherenergy efficiency
dc.subject.otherinversion loss
dc.subject.otherprocess design
dc.subject.othermass transfer
dc.subject.otherhydrogenation
dc.subject.otherslurry reactor
dc.subject.othermuconic acid
dc.subject.otheradipic acid
dc.subject.otherLHHW model
dc.subject.otherkinetics
dc.subject.otherepoxides
dc.subject.othersoybean oil
dc.subject.otherhydrogen peroxide
dc.subject.otherring opening reaction
dc.subject.othercontinuous flow stirred tank reactor (CSTR)
dc.subject.otherphase transfer catalysis (PTC)
dc.subject.othergreen chemistry
dc.subject.othermultiphase reactor
dc.subject.otherliquid–liquid–liquid reactions
dc.subject.otherguaiacol
dc.subject.otherepichlorohydrin
dc.subject.otherguaiacol glycidyl ether
dc.subject.otherslow and rapid reactions
dc.subject.otherrobust parameter estimation
dc.subject.otherdimethyl carbonate
dc.subject.othergas–solid catalytic reactions
dc.subject.otherchemical kinetics
dc.subject.otherheat and mass transfer
dc.subject.otherpacked bed reactor
dc.subject.othermultiphase system
dc.subject.otherphase-field LB model
dc.subject.othercomplex channel
dc.subject.otherflow pattern
dc.subject.otherbubble evolution
dc.subject.otherSuzuki cross-coupling
dc.subject.otherhyper-cross-linked polystyrene
dc.subject.otherpalladium nanoparticles
dc.subject.othercatalyst stability
dc.subject.othercarbonization
dc.subject.otherhalogenation
dc.subject.otherspent resin
dc.subject.otherkinetic analysis
dc.subject.otherthermodynamic analysis
dc.subject.othernumerical optimization
dc.subject.otherultrasonic spraying
dc.subject.otherthree-phase reactor
dc.subject.othertriolein
dc.subject.othertransesterification
dc.subject.otherCaO
dc.subject.othermethanol vapor
dc.subject.other1,1-diethoxybutane
dc.subject.otherheterogeneous catalysts
dc.subject.otheradsorption
dc.subject.otherprocess intensification
dc.subject.othersimulated moving bed reactor
dc.subject.otherdeoxygenation efficiency
dc.subject.othervacuum–N2–H2O–O2 system
dc.subject.otherrotor–stator reactor
dc.subject.othercorrelation
dc.subject.othern/a
dc.titleIndustrial Chemistry Reactions: Kinetics, Mass Transfer and Industrial Reactor Design
dc.typebook
oapen.identifier.doi10.3390/books978-3-0365-4156-3
oapen.relation.isPublishedBy46cabcaa-dd94-4bfe-87b4-55023c1b36d0
oapen.relation.isbn9783036541556
oapen.relation.isbn9783036541563
oapen.pages230
oapen.place.publicationBasel


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