Modeling the Effect of Polymerization Rate on the Intraparticle Mass and Heat Transfer during Propylene Polymerization in a Loop Reactor
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[1] W. H. Ray,et al. Reactor residence time distribution effects on the multistage polymerization of olefins—I. Basic principles and illustrative examples, polypropylene , 1996 .
[2] A. Hamielec,et al. GENERAL DYNAMIC MATHEMATICAL MODELING OF HETEROGENEOUS ZIEGLER-NATTA AND METALLOCENE CATALYZED COPOLYMERIZATION WITH MULTIPLE SITE TYPES AND MASS AND HEAT TRANSFER RESISTANCES , 1995 .
[3] C. Kiparissides,et al. Recent developments in the particle size distribution modeling of fluidized-bed olefin polymerization reactors , 2001 .
[4] J. R. Street,et al. Polymerization in expanding catalyst particles , 1971 .
[5] W. Ray,et al. Polymerization of olefines through heterogeneous catalysis IV. Modeling of heat and mass transfer resistance in the polymer particle boundary layer , 1986 .
[6] R. Galván,et al. Orthogonal collocation applied to analysis of heterogeneous Ziegler-Natta polymerization , 1986 .
[7] W. V. Swaaij,et al. Propene bulk polymerization kinetics: Role of prepolymerization and hydrogen , 2003 .
[8] Xinggao Liu,et al. Modeling mass transport of propylene polymerization on Ziegler–Natta catalyst , 2005 .
[9] W. H. Ray,et al. Polymerization of olefins through heterogeneous catalysis X: Modeling of particle growth and morphology , 1992 .
[10] U. Veera. Mass transport models for a single particle in gas-phase propylene polymerisation , 2003 .
[11] Timothy F. L. McKenna,et al. Single particle modelling for olefin polymerization on supported catalysts: A review and proposals for future developments , 2001 .