Artículos de revistas
Fluidized-bed reactor modeling for polyethylene production
Registro en:
Journal Of Applied Polymer Science. John Wiley & Sons Inc, v. 81, n. 2, n. 321, n. 332, 2001.
0021-8995
WOS:000168593400006
10.1002/app.1442
Autor
Fernandes, FAN
Lona, LMF
Institución
Resumen
Gas-phase technology for polyethylene production has been widely used by industries around the world. A good model for the reactor fluid dynamics is essential to properly set the operating conditions of the fluidized-bed reactor. The fluidized-bed model developed in this work is based on a steady-state model, incorporating interactions between separate bubble, emulsion gas phase, and emulsion solid polymer particles. The model is capable not only of computing temperature and concentration gradients for bubble and emulsion phases, calculating polymer particle mean diameter throughout the bed and polyethylene production rate, but also of pinpointing the appearance of hot spots and polymer meltdown. The model differs from conventional well-mixed fluidized-bed models by assuming that the particles segregate within the bed according to size and weight differences. The model was validated using literature and patent data, presenting good representation of the behavior of the fluidized-bed reactor used in ethylene polymerization. (C) 2001 John Wiley & Sons, Inc. 81 2 321 332