SIMULATION OF GAS-PHASE POLYETHYLENE WITH CONDENSED MODE OPERATION(Ⅰ) ANALYSIS OF REACTOR PERFORMANCE
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SIMULATION OF GAS-PHASE POLYETHYLENE WITH CONDENSED MODE OPERATION(Ⅰ) ANALYSIS OF REACTOR PERFORMANCE
CIESC JournalIssue 10, (2001)
作者机构:
浙江大学化学工程与生物工程学系
作者简介:
基金信息:
DOI:
CLC:
Online First:25 October 2001,
Published:25 October 2001
稿件说明:
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YANG Jingquan, CHEN Wei, YANG Yongrong, et al. SIMULATION OF GAS-PHASE POLYETHYLENE WITH CONDENSED MODE OPERATION(Ⅰ) ANALYSIS OF REACTOR PERFORMANCE[J]. CIESC Journal, 2001, (10).
DOI:
YANG Jingquan, CHEN Wei, YANG Yongrong, et al. SIMULATION OF GAS-PHASE POLYETHYLENE WITH CONDENSED MODE OPERATION(Ⅰ) ANALYSIS OF REACTOR PERFORMANCE[J]. CIESC Journal, 2001, (10).DOI:
SIMULATION OF GAS-PHASE POLYETHYLENE WITH CONDENSED MODE OPERATION(Ⅰ) ANALYSIS OF REACTOR PERFORMANCE
A novel two-phase model for the fluidized bed of polyethylene with condensed mode operation was proposed.The model considered heat and mass conservation in emulsion phase and bubble phase
heat and mass transfer between emulsion phase and bubble phase
polymerization as well as resident time distribution of particles in emulsion phase.The relations between operating variables and reactor performance were investigated by the model.Simulation results agreed well with the industrial data.Simulation results indicate the productivity of reactor as well as ash in polymer will increase greatly
and low the temperature region will expand when the condensed mode is operating with the conventional catalyst.A type of catalyst which suits condensed mode operation was proposed.