05036nam 2201117z- 450 991057688080332120231214133033.0(CKB)5720000000008367(oapen)https://directory.doabooks.org/handle/20.500.12854/84474(EXLCZ)99572000000000836720202206d2022 |y 0engurmn|---annantxtrdacontentcrdamediacrrdacarrierIndustrial Chemistry Reactions: Kinetics, Mass Transfer and Industrial Reactor DesignBaselMDPI - Multidisciplinary Digital Publishing Institute20221 electronic resource (230 p.)3-0365-4155-1 3-0365-4156-X Nowadays, 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).Industrial Chemistry ReactionsTechnology: general issuesbicsscheat exchangermathematical modelenergy efficiencyinversion lossprocess designmass transferhydrogenationslurry reactormuconic acidadipic acidLHHW modelkineticsepoxidessoybean oilhydrogen peroxidering opening reactioncontinuous flow stirred tank reactor (CSTR)phase transfer catalysis (PTC)green chemistrymultiphase reactorliquid-liquid-liquid reactionsguaiacolepichlorohydringuaiacol glycidyl etherslow and rapid reactionsrobust parameter estimationdimethyl carbonategas-solid catalytic reactionschemical kineticsheat and mass transferpacked bed reactormultiphase systemphase-field LB modelcomplex channelflow patternbubble evolutionSuzuki cross-couplinghyper-cross-linked polystyrenepalladium nanoparticlescatalyst stabilitycarbonizationhalogenationspent resinkinetic analysisthermodynamic analysisnumerical optimizationultrasonic sprayingthree-phase reactortrioleintransesterificationCaOmethanol vapor1,1-diethoxybutaneheterogeneous catalystsadsorptionprocess intensificationsimulated moving bed reactordeoxygenation efficiencyvacuum-N2-H2O-O2 systemrotor-stator reactorcorrelationTechnology: general issuesSantacesaria Elioedt338684Tesser RiccardoedtRusso VincenzoedtSantacesaria ElioothTesser RiccardoothRusso VincenzoothBOOK9910576880803321Industrial Chemistry Reactions: Kinetics, Mass Transfer and Industrial Reactor Design3037562UNINA