LEADER 05036nam 2201117z- 450 001 9910576880803321 005 20231214133033.0 035 $a(CKB)5720000000008367 035 $a(oapen)https://directory.doabooks.org/handle/20.500.12854/84474 035 $a(EXLCZ)995720000000008367 100 $a20202206d2022 |y 0 101 0 $aeng 135 $aurmn|---annan 181 $ctxt$2rdacontent 182 $cc$2rdamedia 183 $acr$2rdacarrier 200 10$aIndustrial Chemistry Reactions: Kinetics, Mass Transfer and Industrial Reactor Design 210 $aBasel$cMDPI - Multidisciplinary Digital Publishing Institute$d2022 215 $a1 electronic resource (230 p.) 311 $a3-0365-4155-1 311 $a3-0365-4156-X 330 $aNowadays, 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). 517 $aIndustrial Chemistry Reactions 606 $aTechnology: general issues$2bicssc 610 $aheat exchanger 610 $amathematical model 610 $aenergy efficiency 610 $ainversion loss 610 $aprocess design 610 $amass transfer 610 $ahydrogenation 610 $aslurry reactor 610 $amuconic acid 610 $aadipic acid 610 $aLHHW model 610 $akinetics 610 $aepoxides 610 $asoybean oil 610 $ahydrogen peroxide 610 $aring opening reaction 610 $acontinuous flow stirred tank reactor (CSTR) 610 $aphase transfer catalysis (PTC) 610 $agreen chemistry 610 $amultiphase reactor 610 $aliquid-liquid-liquid reactions 610 $aguaiacol 610 $aepichlorohydrin 610 $aguaiacol glycidyl ether 610 $aslow and rapid reactions 610 $arobust parameter estimation 610 $adimethyl carbonate 610 $agas-solid catalytic reactions 610 $achemical kinetics 610 $aheat and mass transfer 610 $apacked bed reactor 610 $amultiphase system 610 $aphase-field LB model 610 $acomplex channel 610 $aflow pattern 610 $abubble evolution 610 $aSuzuki cross-coupling 610 $ahyper-cross-linked polystyrene 610 $apalladium nanoparticles 610 $acatalyst stability 610 $acarbonization 610 $ahalogenation 610 $aspent resin 610 $akinetic analysis 610 $athermodynamic analysis 610 $anumerical optimization 610 $aultrasonic spraying 610 $athree-phase reactor 610 $atriolein 610 $atransesterification 610 $aCaO 610 $amethanol vapor 610 $a1,1-diethoxybutane 610 $aheterogeneous catalysts 610 $aadsorption 610 $aprocess intensification 610 $asimulated moving bed reactor 610 $adeoxygenation efficiency 610 $avacuum-N2-H2O-O2 system 610 $arotor-stator reactor 610 $acorrelation 615 7$aTechnology: general issues 700 $aSantacesaria$b Elio$4edt$0338684 702 $aTesser$b Riccardo$4edt 702 $aRusso$b Vincenzo$4edt 702 $aSantacesaria$b Elio$4oth 702 $aTesser$b Riccardo$4oth 702 $aRusso$b Vincenzo$4oth 906 $aBOOK 912 $a9910576880803321 996 $aIndustrial Chemistry Reactions: Kinetics, Mass Transfer and Industrial Reactor Design$93037562 997 $aUNINA