Modeling and simulation of polypropylene particle size distribution in industrial horizontal stirred bed reactors

Modeling and simulation of polypropylene particle size distribution in industrial horizontal stirred bed reactors

Source :

• Journal of Applied Polymer Science [ 0021-8995 ] ; 2012-08-15.

Descripteurs français

• Wicri :
  • topic : Polymère, Simulation.

English descriptors

• KwdEn :
  • Activation energy, Activation reaction, Active sites, Actual concentration, Actual monomer concentration, Amorphous polymer phase, Appl polym, Boundary conditions, Bulk phase, Catalyst, Catalyst concentration, Catalyst mass fraction, Catalyst number fraction, Catalyst particle, Catalyst particles, Catalyst residence time, Catalyst size, Chain activation, Chem, Chemical engineering, Coefficient, Concentration gradients, Contract grant number, Contract grant sponsor, Critical temperature, Crystallinity, Cstr, Deactivation, Deff, Different catalyst sizes, Different flow models, Different times, Early stages, Effective monomer diffusion coefficient, Equivolume cstrs, Exit stream, Flow models, Frequency factor, Growth rate, Heat capacity, Hsbr, Hsbrs, Industrial data, Initial catalyst size, Initial catalyst size increases, Internal mass transfer resistance, Intraparticle, Intraparticle mass, Intraparticle massand resistances, Kcal activation energy, Kinetic scheme, Larger particles, Liquid phase, Mass density function, Mechanical agitation, Modeling, Monomer, Monomer concentration, Monomer pressure, Monomer sorption, Nonuniform, Nonuniform catalyst feed, Nonuniform size catalyst feed, Olefin polymerization reactors, Other hand, Outflow streams, Particle, Particle agglomeration, Particle attrition, Particle breakage, Particle growth, Particle growth rate, Particle segregation, Particle size distribution, Pmlm, Polym, Polymer, Polymer chains, Polymer crystallinity, Polymer particle, Polymer particle size, Polymer particles, Polymer psds, Polymer science, Polymerization rate, Polypropylene, Polypropylene particles, Polypropylene process, Population balance equation, Potential catalyst, Probability density function, Propylene, Propylene concentration, Propylene concentration profiles, Propylene polymerization, Radial position, Reactor, Residence time, Residence time distribution, Schematic representation, Simulation, Single cstr, Single particle, Single particle growth, Size distribution, Size range, Standard deviation, Steady state, Temperature profiles, Thermal conductivity, Time interval, Uniform size catalyst feed, Unit volume, Wiley periodicals.
• Teeft :
  • Activation energy, Activation reaction, Active sites, Actual concentration, Actual monomer concentration, Amorphous polymer phase, Appl polym, Boundary conditions, Bulk phase, Catalyst, Catalyst concentration, Catalyst mass fraction, Catalyst number fraction, Catalyst particle, Catalyst particles, Catalyst residence time, Catalyst size, Chain activation, Chem, Chemical engineering, Coefficient, Concentration gradients, Contract grant number, Contract grant sponsor, Critical temperature, Crystallinity, Cstr, Deactivation, Deff, Different catalyst sizes, Different flow models, Different times, Early stages, Effective monomer diffusion coefficient, Equivolume cstrs, Exit stream, Flow models, Frequency factor, Growth rate, Heat capacity, Hsbr, Hsbrs, Industrial data, Initial catalyst size, Initial catalyst size increases, Internal mass transfer resistance, Intraparticle, Intraparticle mass, Intraparticle massand resistances, Kcal activation energy, Kinetic scheme, Larger particles, Liquid phase, Mass density function, Mechanical agitation, Modeling, Monomer, Monomer concentration, Monomer pressure, Monomer sorption, Nonuniform, Nonuniform catalyst feed, Nonuniform size catalyst feed, Olefin polymerization reactors, Other hand, Outflow streams, Particle, Particle agglomeration, Particle attrition, Particle breakage, Particle growth, Particle growth rate, Particle segregation, Particle size distribution, Pmlm, Polym, Polymer, Polymer chains, Polymer crystallinity, Polymer particle, Polymer particle size, Polymer particles, Polymer psds, Polymer science, Polymerization rate, Polypropylene, Polypropylene particles, Polypropylene process, Population balance equation, Potential catalyst, Probability density function, Propylene, Propylene concentration, Propylene concentration profiles, Propylene polymerization, Radial position, Reactor, Residence time, Residence time distribution, Schematic representation, Simulation, Single cstr, Single particle, Single particle growth, Size distribution, Size range, Standard deviation, Steady state, Temperature profiles, Thermal conductivity, Time interval, Uniform size catalyst feed, Unit volume, Wiley periodicals.

Abstract

• https://api.istex.fr/document/D483D0DDABA8EE0733217B254E909BCCE24099C6/fulltext/pdf

Affiliations:

• France, République populaire de Chine
• Grand Est, Lorraine (région), Zhejiang
• Hangzhou, Nancy
• Centre national de la recherche scientifique, Laboratoire réactions et génie des procédés, Université de Lorraine, Université de Zhejiang

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