Reactor Modeling And Physical-chemical Properties Characterization In Polyethylene Fluidized-bed Reactor

[No abstract available]433621624Choi, K.Y., Ray, W.H., The dynamic behaviour of fluidized bed reactors for solid catalyzed gas phase olefin polymerization (1985) Chem.Eng.Sci., 40, pp. 2261-2279DeCarvalho, A.B., Gloor, P.E., Hamielec, A.E., A Kinectic Mathematical Model for Heterogeneous Ziegler-Natta Copolymerization (1989) Polymer, 30, p. 280Kissin, Y.V., (1987) Isospecific Polymerization of Olefins with Heterogeneous Ziegler-Natta Catalysts, , Springer-Verlag, New YorkMcAuley, K.B., MacGregor, J.F., Hamielec, A.E., A kinetic model for industrial gas-phase ethylene copolymerization (1990) A.I.Ch.E.J., 36 (6), pp. 837-850McAuley, K.B., Talbot, J.P., Harris, T.J., A comparison of two-phase and well-mixed models for fluidized-bed polyethylene reactors (1994) Chem.Eng.Sci., 49 (13), pp. 2035-2045Zabisky, R.C.M., Chan, W.M., Gloor, P.E., Hamielec, A.E., A kinetic model for olefin polymerization in high-pressure tubular reactors: A review and update (1992) Polymer, 33, pp. 2243-226

Fluidized-bed Reactor And Physicalchemical Properties Modeling For Polyethylene Production

A new steady-state model incorporating interactions between separate bubble and emulsion phases inside the reactor bed and a polymer physical-chemical characterization model were developed. A computer program, FBPOL, was also developed to accomplish the linkage of these two models, in order to predict the polymer grade that can be produced by different operational conditions. © 1999 Elsevier Science Ltd.23SUPPL. 1S803S806Choi, K.Y., Ray, W.H., The Dynamic Behaviour of Fluidized Bed Reactors for Solid Catalyzed Gas Phase Olefin Polymerization (1985) Chem.Eng.Sci., 40, pp. 2261-2279deCarvalho, A.B., Gloor, P.E., Hamielec, A.E., A Kinetic Mathematical Model for Heterogeneous Ziegler-Natta Copolymerization (1989) Polymer, 30, p. 280Kissin, Y.V., (1987) Isospecijic Polymerization of Olefins with Heterogeneous Ziegler-Natta Catalysts, , SpringerVerlag, New YorkMcAuley, K.B., MacGregor, I.F., Hamielec, A.E., A Kinetic Model for Industrial Gas-Phase Ethylene Copolymerization (1990) A. J. Ch. E. J., 36, pp. 837-850McAuley, K.B., Talbot, J.P., Harris, T.J., A Comparison of Two-Phase and Well-Mixed Models for Fluidized-Bed Polyethylene Reactors (1994) Chem. Eng. Sci., 49, pp. 2035-2045Zabisky, R.C.M., Chan, W.M., Gloor, P.E., Hamielec, A.E., A Kinetic Model for Olefin Polymerization in High-Pressure Tubular Reactors: a Review and Update (1992) Polymer, 33, pp. 2243-226