Industrial Chemistry Reactions: Kinetics, Mass Transfer and Industrial Reactor Design
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, rea...
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| 格式: | Online |
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| 語言: | 英语 |
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MDPI - Multidisciplinary Digital Publishing Institute
2022
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| 在線閱讀: | ONIX_20220621_9783036541556_52 |
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| collection | Directory of Open Access Books |
| description | 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). |
| format | Online |
| id | doab-20.500.12854ir-84474 |
| institution | Directory of Open Access Books |
| language | eng |
| publishDate | 2022 |
| publishDateRange | 2022 |
| publishDateSort | 2022 |
| publisher | MDPI - Multidisciplinary Digital Publishing Institute |
| publisherStr | MDPI - Multidisciplinary Digital Publishing Institute |
| record_format | ojs |
| spelling | doab-20.500.12854ir-844742024-04-09T23:16:40Z Industrial Chemistry Reactions: Kinetics, Mass Transfer and Industrial Reactor Design Santacesaria, Elio Tesser, Riccardo Russo, Vincenzo heat exchanger mathematical model energy efficiency inversion loss process design mass transfer hydrogenation slurry reactor muconic acid adipic acid LHHW model kinetics epoxides soybean oil hydrogen peroxide ring opening reaction continuous flow stirred tank reactor (CSTR) phase transfer catalysis (PTC) green chemistry multiphase reactor liquid–liquid–liquid reactions guaiacol epichlorohydrin guaiacol glycidyl ether slow and rapid reactions robust parameter estimation dimethyl carbonate gas–solid catalytic reactions chemical kinetics heat and mass transfer packed bed reactor multiphase system phase-field LB model complex channel flow pattern bubble evolution Suzuki cross-coupling hyper-cross-linked polystyrene palladium nanoparticles catalyst stability carbonization halogenation spent resin kinetic analysis thermodynamic analysis numerical optimization ultrasonic spraying three-phase reactor triolein transesterification CaO methanol vapor 1,1-diethoxybutane heterogeneous catalysts adsorption process intensification simulated moving bed reactor deoxygenation efficiency vacuum–N2–H2O–O2 system rotor–stator reactor correlation n/a thema EDItEUR::T Technology, Engineering, Agriculture, Industrial processes::TB Technology: general issues 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). 2022-06-21T08:37:39Z 2022-06-21T08:37:39Z 2022 book ONIX_20220621_9783036541556_52 9783036541556 9783036541563 https://directory.doabooks.org/handle/20.500.12854/84474 eng application/octet-stream Attribution 4.0 International https://mdpi.com/books/pdfview/book/5457 https://mdpi.com/books/pdfview/book/5457 MDPI - Multidisciplinary Digital Publishing Institute 10.3390/books978-3-0365-4156-3 10.3390/books978-3-0365-4156-3 46cabcaa-dd94-4bfe-87b4-55023c1b36d0 9783036541556 9783036541563 230 Basel open access |
| spellingShingle | heat exchanger mathematical model energy efficiency inversion loss process design mass transfer hydrogenation slurry reactor muconic acid adipic acid LHHW model kinetics epoxides soybean oil hydrogen peroxide ring opening reaction continuous flow stirred tank reactor (CSTR) phase transfer catalysis (PTC) green chemistry multiphase reactor liquid–liquid–liquid reactions guaiacol epichlorohydrin guaiacol glycidyl ether slow and rapid reactions robust parameter estimation dimethyl carbonate gas–solid catalytic reactions chemical kinetics heat and mass transfer packed bed reactor multiphase system phase-field LB model complex channel flow pattern bubble evolution Suzuki cross-coupling hyper-cross-linked polystyrene palladium nanoparticles catalyst stability carbonization halogenation spent resin kinetic analysis thermodynamic analysis numerical optimization ultrasonic spraying three-phase reactor triolein transesterification CaO methanol vapor 1,1-diethoxybutane heterogeneous catalysts adsorption process intensification simulated moving bed reactor deoxygenation efficiency vacuum–N2–H2O–O2 system rotor–stator reactor correlation n/a thema EDItEUR::T Technology, Engineering, Agriculture, Industrial processes::TB Technology: general issues Industrial Chemistry Reactions: Kinetics, Mass Transfer and Industrial Reactor Design |
| title | Industrial Chemistry Reactions: Kinetics, Mass Transfer and Industrial Reactor Design |
| title_full | Industrial Chemistry Reactions: Kinetics, Mass Transfer and Industrial Reactor Design |
| title_fullStr | Industrial Chemistry Reactions: Kinetics, Mass Transfer and Industrial Reactor Design |
| title_full_unstemmed | Industrial Chemistry Reactions: Kinetics, Mass Transfer and Industrial Reactor Design |
| title_short | Industrial Chemistry Reactions: Kinetics, Mass Transfer and Industrial Reactor Design |
| title_sort | industrial chemistry reactions kinetics mass transfer and industrial reactor design |
| topic | heat exchanger mathematical model energy efficiency inversion loss process design mass transfer hydrogenation slurry reactor muconic acid adipic acid LHHW model kinetics epoxides soybean oil hydrogen peroxide ring opening reaction continuous flow stirred tank reactor (CSTR) phase transfer catalysis (PTC) green chemistry multiphase reactor liquid–liquid–liquid reactions guaiacol epichlorohydrin guaiacol glycidyl ether slow and rapid reactions robust parameter estimation dimethyl carbonate gas–solid catalytic reactions chemical kinetics heat and mass transfer packed bed reactor multiphase system phase-field LB model complex channel flow pattern bubble evolution Suzuki cross-coupling hyper-cross-linked polystyrene palladium nanoparticles catalyst stability carbonization halogenation spent resin kinetic analysis thermodynamic analysis numerical optimization ultrasonic spraying three-phase reactor triolein transesterification CaO methanol vapor 1,1-diethoxybutane heterogeneous catalysts adsorption process intensification simulated moving bed reactor deoxygenation efficiency vacuum–N2–H2O–O2 system rotor–stator reactor correlation n/a thema EDItEUR::T Technology, Engineering, Agriculture, Industrial processes::TB Technology: general issues |
| topic_facet | heat exchanger mathematical model energy efficiency inversion loss process design mass transfer hydrogenation slurry reactor muconic acid adipic acid LHHW model kinetics epoxides soybean oil hydrogen peroxide ring opening reaction continuous flow stirred tank reactor (CSTR) phase transfer catalysis (PTC) green chemistry multiphase reactor liquid–liquid–liquid reactions guaiacol epichlorohydrin guaiacol glycidyl ether slow and rapid reactions robust parameter estimation dimethyl carbonate gas–solid catalytic reactions chemical kinetics heat and mass transfer packed bed reactor multiphase system phase-field LB model complex channel flow pattern bubble evolution Suzuki cross-coupling hyper-cross-linked polystyrene palladium nanoparticles catalyst stability carbonization halogenation spent resin kinetic analysis thermodynamic analysis numerical optimization ultrasonic spraying three-phase reactor triolein transesterification CaO methanol vapor 1,1-diethoxybutane heterogeneous catalysts adsorption process intensification simulated moving bed reactor deoxygenation efficiency vacuum–N2–H2O–O2 system rotor–stator reactor correlation n/a thema EDItEUR::T Technology, Engineering, Agriculture, Industrial processes::TB Technology: general issues |
| url | ONIX_20220621_9783036541556_52 |