Propylene/1-butene polymer alloys were prepared by in-situ slurry polymerization with spherical supported Ziegler-Natta catalyst and the technology of monomer composition switching method. Combining the kinetic model of propylene/1-butene copolymerization and the material balance
a reactor model with the monomer composition switching was developed by the moment method. The model parameters were fitted according to the real-time consumption rate of propylene obtained from experiments. The polymerization reactivity
the product's composition and their changes with switching frequency of monomer composition were simulated. The results show that the model can well describe the polymerization rate at different stages
the catalyst activity
the total content of 1-butene in the alloy
and the contents of random copolymer and “block” copolymer at various switching frequencies. It has been revealed also that the pulse feed of propylene in the copolymerization process is conducive to increasing the monomer diffusion to the active center
thereby increasing the polymerization rate and polymerization activity.
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Related Author
MA Yanhong
LU Jiangyin
HU Zizhao
WEI Shenghua
QIAO Liang
LI Shang
LIU Xinliang
WANG Ming
Related Institution
Key Laboratory of Oil & Gas Fine Chemicals, Ministry of Education, College of Chemistry and Chemical Engineering, Xinjiang University, Urumqi 830046, Xingjiang
Sinopec Senmei (Fujian) Petroleum Company Limited Nanping Branch Company
State Key Laboratory of Heavy Oil Processing, China University of Petroleum ( East China)
Southwest Gas Production Plant, Zhejiang Oilfield Company, China National Petroleum Corporation
Advanced Chemical Engineering and Energy Materials Research Center,China University of Petroleum (East China)