作者: Christos Chatzidoukas , Vassileios Kanellopoulos , Costas Kiparissides
关键词: Molar mass distribution 、 Gas phase 、 Copolymer 、 Copolymer composition 、 Chemical engineering 、 Polymer chemistry 、 Kinetic energy 、 Mass fraction 、 Catalysis 、 Fluidized bed 、 Chemistry
摘要: A comprehensive mathematical model is developed for the dynamic calculation of molecular distributed properties (i.e. MWD and CCD) in a gas-phase, catalytic, ethylene-1butene copolymerization, FBR, taking into account various kinetic, micro- macroscopic phenomena reactor. The effects two single-site catalyst mass fractions reactor operating conditions on production polyolefins with ‘tailor-made’ bimodal are investigated. It shown that PE grades either or CCD can be produced single using mixture catalysts under properly selected conditions.