Modeling and simulation of polypropylene particle size distribution in industrial horizontal stirred bed reactors
Identifieur interne : 000040 ( Istex/Checkpoint ); précédent : 000039; suivant : 000041Modeling and simulation of polypropylene particle size distribution in industrial horizontal stirred bed reactors
Auteurs : Zhou Tian [République populaire de Chine] ; Xue-Ping Gu [République populaire de Chine, France] ; Lian-Fang Feng [République populaire de Chine] ; Jean-Pierre Corriou [France] ; Guo-Hua Hu [France]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
This work aims at developing a steady‐state particle size distribution (PSD) model for predicting the size distribution of polypropylene particles in the outflow streams of propylene gas‐phase horizontal stirred bed reactors (HSBR), on the one hand and investigating the effect of the catalyst residence time distribution (RTD) on the polymer PSD, on the other hand. The polymer multilayer model (PMLM) is used to describe the growth of a single particle. Knowing the PSD and RTD of a Ziegler–Natta type of catalyst and polymerization kinetics, this model allows calculating the polymer PSD of propylene polymerization in the HSBRs. The calculated polypropylene PSDs agree well with those obtained from the industrial reactors. The results reveal that both the PSD and the RTD of the catalyst affect the polymer PSD but in different manners. The effect of RTD on the PSD is less significant in the case of a nonuniform size catalyst feed. This model also allows investigating the effects of other process parameters on the polymer PSD under steady‐state conditions, including intraparticle mass‐ and heat‐transfer limitations, initial catalyst size, and polymer crystallinity. © 2012 Wiley Periodicals, Inc. J Appl Polym Sci, 2012
Url:
DOI: 10.1002/app.36473
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
Links toward previous steps (curation, corpus...)
Links to Exploration step
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<term>Activation reaction</term>
<term>Active sites</term>
<term>Actual concentration</term>
<term>Actual monomer concentration</term>
<term>Amorphous polymer phase</term>
<term>Appl polym</term>
<term>Boundary conditions</term>
<term>Bulk phase</term>
<term>Catalyst</term>
<term>Catalyst concentration</term>
<term>Catalyst mass fraction</term>
<term>Catalyst number fraction</term>
<term>Catalyst particle</term>
<term>Catalyst particles</term>
<term>Catalyst residence time</term>
<term>Catalyst size</term>
<term>Chain activation</term>
<term>Chem</term>
<term>Chemical engineering</term>
<term>Coefficient</term>
<term>Concentration gradients</term>
<term>Contract grant number</term>
<term>Contract grant sponsor</term>
<term>Critical temperature</term>
<term>Crystallinity</term>
<term>Cstr</term>
<term>Deactivation</term>
<term>Deff</term>
<term>Different catalyst sizes</term>
<term>Different flow models</term>
<term>Different times</term>
<term>Early stages</term>
<term>Effective monomer diffusion coefficient</term>
<term>Equivolume cstrs</term>
<term>Exit stream</term>
<term>Flow models</term>
<term>Frequency factor</term>
<term>Growth rate</term>
<term>Heat capacity</term>
<term>Hsbr</term>
<term>Hsbrs</term>
<term>Industrial data</term>
<term>Initial catalyst size</term>
<term>Initial catalyst size increases</term>
<term>Internal mass transfer resistance</term>
<term>Intraparticle</term>
<term>Intraparticle mass</term>
<term>Intraparticle massand resistances</term>
<term>Kcal activation energy</term>
<term>Kinetic scheme</term>
<term>Larger particles</term>
<term>Liquid phase</term>
<term>Mass density function</term>
<term>Mechanical agitation</term>
<term>Modeling</term>
<term>Monomer</term>
<term>Monomer concentration</term>
<term>Monomer pressure</term>
<term>Monomer sorption</term>
<term>Nonuniform</term>
<term>Nonuniform catalyst feed</term>
<term>Nonuniform size catalyst feed</term>
<term>Olefin polymerization reactors</term>
<term>Other hand</term>
<term>Outflow streams</term>
<term>Particle</term>
<term>Particle agglomeration</term>
<term>Particle attrition</term>
<term>Particle breakage</term>
<term>Particle growth</term>
<term>Particle growth rate</term>
<term>Particle segregation</term>
<term>Particle size distribution</term>
<term>Pmlm</term>
<term>Polym</term>
<term>Polymer</term>
<term>Polymer chains</term>
<term>Polymer crystallinity</term>
<term>Polymer particle</term>
<term>Polymer particle size</term>
<term>Polymer particles</term>
<term>Polymer psds</term>
<term>Polymer science</term>
<term>Polymerization rate</term>
<term>Polypropylene</term>
<term>Polypropylene particles</term>
<term>Polypropylene process</term>
<term>Population balance equation</term>
<term>Potential catalyst</term>
<term>Probability density function</term>
<term>Propylene</term>
<term>Propylene concentration</term>
<term>Propylene concentration profiles</term>
<term>Propylene polymerization</term>
<term>Radial position</term>
<term>Reactor</term>
<term>Residence time</term>
<term>Residence time distribution</term>
<term>Schematic representation</term>
<term>Simulation</term>
<term>Single cstr</term>
<term>Single particle</term>
<term>Single particle growth</term>
<term>Size distribution</term>
<term>Size range</term>
<term>Standard deviation</term>
<term>Steady state</term>
<term>Temperature profiles</term>
<term>Thermal conductivity</term>
<term>Time interval</term>
<term>Uniform size catalyst feed</term>
<term>Unit volume</term>
<term>Wiley periodicals</term>
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<term>Activation reaction</term>
<term>Active sites</term>
<term>Actual concentration</term>
<term>Actual monomer concentration</term>
<term>Amorphous polymer phase</term>
<term>Appl polym</term>
<term>Boundary conditions</term>
<term>Bulk phase</term>
<term>Catalyst</term>
<term>Catalyst concentration</term>
<term>Catalyst mass fraction</term>
<term>Catalyst number fraction</term>
<term>Catalyst particle</term>
<term>Catalyst particles</term>
<term>Catalyst residence time</term>
<term>Catalyst size</term>
<term>Chain activation</term>
<term>Chem</term>
<term>Chemical engineering</term>
<term>Coefficient</term>
<term>Concentration gradients</term>
<term>Contract grant number</term>
<term>Contract grant sponsor</term>
<term>Critical temperature</term>
<term>Crystallinity</term>
<term>Cstr</term>
<term>Deactivation</term>
<term>Deff</term>
<term>Different catalyst sizes</term>
<term>Different flow models</term>
<term>Different times</term>
<term>Early stages</term>
<term>Effective monomer diffusion coefficient</term>
<term>Equivolume cstrs</term>
<term>Exit stream</term>
<term>Flow models</term>
<term>Frequency factor</term>
<term>Growth rate</term>
<term>Heat capacity</term>
<term>Hsbr</term>
<term>Hsbrs</term>
<term>Industrial data</term>
<term>Initial catalyst size</term>
<term>Initial catalyst size increases</term>
<term>Internal mass transfer resistance</term>
<term>Intraparticle</term>
<term>Intraparticle mass</term>
<term>Intraparticle massand resistances</term>
<term>Kcal activation energy</term>
<term>Kinetic scheme</term>
<term>Larger particles</term>
<term>Liquid phase</term>
<term>Mass density function</term>
<term>Mechanical agitation</term>
<term>Modeling</term>
<term>Monomer</term>
<term>Monomer concentration</term>
<term>Monomer pressure</term>
<term>Monomer sorption</term>
<term>Nonuniform</term>
<term>Nonuniform catalyst feed</term>
<term>Nonuniform size catalyst feed</term>
<term>Olefin polymerization reactors</term>
<term>Other hand</term>
<term>Outflow streams</term>
<term>Particle</term>
<term>Particle agglomeration</term>
<term>Particle attrition</term>
<term>Particle breakage</term>
<term>Particle growth</term>
<term>Particle growth rate</term>
<term>Particle segregation</term>
<term>Particle size distribution</term>
<term>Pmlm</term>
<term>Polym</term>
<term>Polymer</term>
<term>Polymer chains</term>
<term>Polymer crystallinity</term>
<term>Polymer particle</term>
<term>Polymer particle size</term>
<term>Polymer particles</term>
<term>Polymer psds</term>
<term>Polymer science</term>
<term>Polymerization rate</term>
<term>Polypropylene</term>
<term>Polypropylene particles</term>
<term>Polypropylene process</term>
<term>Population balance equation</term>
<term>Potential catalyst</term>
<term>Probability density function</term>
<term>Propylene</term>
<term>Propylene concentration</term>
<term>Propylene concentration profiles</term>
<term>Propylene polymerization</term>
<term>Radial position</term>
<term>Reactor</term>
<term>Residence time</term>
<term>Residence time distribution</term>
<term>Schematic representation</term>
<term>Simulation</term>
<term>Single cstr</term>
<term>Single particle</term>
<term>Single particle growth</term>
<term>Size distribution</term>
<term>Size range</term>
<term>Standard deviation</term>
<term>Steady state</term>
<term>Temperature profiles</term>
<term>Thermal conductivity</term>
<term>Time interval</term>
<term>Uniform size catalyst feed</term>
<term>Unit volume</term>
<term>Wiley periodicals</term>
</keywords>
<keywords scheme="Wicri" type="topic" xml:lang="fr"><term>Polymère</term>
<term>Simulation</term>
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<front><div type="abstract" xml:lang="en">This work aims at developing a steady‐state particle size distribution (PSD) model for predicting the size distribution of polypropylene particles in the outflow streams of propylene gas‐phase horizontal stirred bed reactors (HSBR), on the one hand and investigating the effect of the catalyst residence time distribution (RTD) on the polymer PSD, on the other hand. The polymer multilayer model (PMLM) is used to describe the growth of a single particle. Knowing the PSD and RTD of a Ziegler–Natta type of catalyst and polymerization kinetics, this model allows calculating the polymer PSD of propylene polymerization in the HSBRs. The calculated polypropylene PSDs agree well with those obtained from the industrial reactors. The results reveal that both the PSD and the RTD of the catalyst affect the polymer PSD but in different manners. The effect of RTD on the PSD is less significant in the case of a nonuniform size catalyst feed. This model also allows investigating the effects of other process parameters on the polymer PSD under steady‐state conditions, including intraparticle mass‐ and heat‐transfer limitations, initial catalyst size, and polymer crystallinity. © 2012 Wiley Periodicals, Inc. J Appl Polym Sci, 2012</div>
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<name sortKey="Hu, Guo Ua" sort="Hu, Guo Ua" uniqKey="Hu G" first="Guo-Hua" last="Hu">Guo-Hua Hu</name>
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</tree>
</affiliations>
</record>
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