Explore
Industrial Chemistry Reactions: Kinetics, Mass Transfer and Industrial Reactor Design
0 Ungluers have
Faved this Work
Login to Fave
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).
This book is included in DOAB.
Why read this book? Have your say.
You must be logged in to comment.
Rights Information
Are you the author or publisher of this work? If so, you can claim it as yours by registering as an Unglue.it rights holder.Downloads
This work has been downloaded 65 times via unglue.it ebook links.
- 65 - pdf (CC BY) at Unglue.it.
Keywords
- 1,1-diethoxybutane
- adipic acid
- adsorption
- bubble evolution
- CaO
- carbonization
- catalyst stability
- Chemical Kinetics
- complex channel
- continuous flow stirred tank reactor (CSTR)
- correlation
- deoxygenation efficiency
- dimethyl carbonate
- Energy Efficiency
- epichlorohydrin
- epoxides
- flow pattern
- gas–solid catalytic reactions
- Green chemistry
- guaiacol
- guaiacol glycidyl ether
- halogenation
- heat and mass transfer
- heat exchanger
- heterogeneous catalysts
- hydrogen peroxide
- hydrogenation
- hyper-cross-linked polystyrene
- inversion loss
- kinetic analysis
- kinetics
- LHHW model
- liquid–liquid–liquid reactions
- mass transfer
- Mathematical model
- methanol vapor
- muconic acid
- multiphase reactor
- multiphase system
- n/a
- Numerical Optimization
- packed bed reactor
- palladium nanoparticles
- phase transfer catalysis (PTC)
- phase-field LB model
- process design
- process intensification
- ring opening reaction
- robust parameter estimation
- rotor–stator reactor
- simulated moving bed reactor
- slow and rapid reactions
- slurry reactor
- soybean oil
- spent resin
- Suzuki cross-coupling
- Technology, engineering, agriculture
- Technology: general issues
- thermodynamic analysis
- three-phase reactor
- transesterification
- triolein
- ultrasonic spraying
- vacuum–N2–H2O–O2 system
Links
DOI: 10.3390/books978-3-0365-4156-3Editions