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气相流化床聚乙烯颗粒粒径分布的定制

Customization of Particle Size Distribution in Continuous Polymerization Process
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摘要 基于气相法聚乙烯流化床反应器颗粒粒径分布的预测[1],提出了颗粒粒径分布定制模型。通过模型的优化计算,可得到催化剂粒径及其分布、操作气速、反应温度、乙烯浓度和丁烯浓度等生产操作参数,由此进行生产可获得具有良好流态化特性的聚乙烯颗粒粒径分布,能为生产具有特定粒径分布的聚乙烯颗粒提供理论指导。模型由工业装置的生产数据分析了计算结果的合理性。最后,以三种粒径分布的聚乙烯颗粒为例讨论了模型的可行性。同时,运用粒子群优化算法求解模型的非线性规划问题,算法具有调整参数少、收敛速度快和全局优化等优点。 Based on the steady-state particle size distribution model proposed in the previous paper published by authors for the industrial fluidized bed gas-phase polyethylene production process, a particle size distribution tailored model (PSD-tailored model) was presented. After considering the restriction of technology, such as operation parameter ranges, the novel PSD-tailored model was solved by using an algorithm named as Particle Swarm Optimization (PSO), and the polyethylene PSD of an assigned objective value could be attained by optimization of the manipulated variable values, such as PSD of catalyst particles, superficial gas velocity, polymerization temperature, the concentration of ethylene and butylenes, Using the above obtained optimized operation parameters, the optimal fluidization quality could be attained and the stability of the production could be improved greatly. Meanwhile, using the PSO method could reduce the parameters needed to be optimized, save the calculation time and attain the global optimization during the calculation, The examples of using the PSD tailored operation strategy for three types polyethylene PSD were illustrated separately, which clarify the optimal strategy of polyethylene PSD tailored production in detail. It is shown that the commercial process could be enormously benefited by the optimal strategy proposed.
出处 《高校化学工程学报》 EI CAS CSCD 北大核心 2006年第5期712-716,共5页 Journal of Chemical Engineering of Chinese Universities
基金 国家自然科学基金重大项目资助(20490200)。
关键词 流化床 聚乙烯 粒径分布 定制 粒子群优化算法 fluidized bed polyethylene particle size distrisution (PSD) tailored algorithm of particle swarm optimization
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参考文献6

  • 1Committee of Compilation(编写委员会).Handbook of Chemical Engineering,Vol.20-Fluidization(化工手册,第 20 卷流态化)[M].Beijing(北京):Chemical Industry Press(化学工业出版社),1989.
  • 2杨宝柱,江炜,王靖岱,阳永荣.气相流化床聚乙烯颗粒粒径分布模型的研究[J].高校化学工程学报,2005,19(4):461-467. 被引量:19
  • 3Choi Ku-yong,Zhao Xia,Tang Shi-hua.Population balance modeling for a continuous gas phase olefin polymerization reactor[J].J Appl Polym Sci,1994,53:1589-1597.
  • 4Hatzantonis H,Goulas A,Kiparissides C.A comprehensive model for the prediction of particle-size distribution in catalyzed olefin polymerization fluidized-bed reactors[J].Chemical Engineering Science,1998,53(18):3251-3267.
  • 5Kennedy J,Eberhart R C.Particle swarm optimization proc[A].IEEE Int'l Conf on Neural Networks[C].Piscataway,NJ:IEEE Service Center,1995,Vol.Ⅳ,pp.1942-1948.
  • 6HU Xiao-hui(胡晓辉).Introduction of particle swarm optimization(粒子群优化算法介绍)[J/OL].http://icdweb.cc.purdue.edu/~hux,2002-04.

二级参考文献11

  • 1Choi Ku Yong, Zhao Xia, Tang Shi-hua. Population balance modeling for a continuous gas phase olefin polymerization reactor [J]. J Appl Polym Sci, 1994, 53: 1589-1597.
  • 2Khang D Y, Lee H H. Particle size distribution in fluidized beds for catalyst polymerization [J]. Chemical Engineering Science, 1996, 52(3): 421-431.
  • 3Overturf B W. Computations for discrete cut particle size distribution in a fluidized bed reactor [J]. Powder Technology,1979, 23: 143-147.
  • 4Chen T P, Saxena S C. Particle size distribution in a fluidized bed reactor [J]. Powder Technology, 1976, 15: 283-285.
  • 5Hatzantonis H, Goulas A, Kiparissides C. A comprehensive model for the prediction of particle-size distribution in catalyzed olefin polymerization fluidized-bed reactors [J]. Chemical Engineering Science, 1998, 53(18): 3251-3267.
  • 6Levenspiel O, Kunii D, Fitzgerald T. The processing of solids of changing size in bubbling fluidized beds [J]. Powder Technology, 1968/69, 2: 87-96.
  • 7Kunii D, Levenspiel O. Fluidization Engineering [M]. Boston MA: Butterworth-Heinemann, 1991.
  • 8Haider A, Levenspiel O. Drag coefficient and terminal velocity of spherical and non-spherical particles [J]. Powder Technology, 1989, 58: 63-70.
  • 9霍超,任晓红,宗迎伟,阳永荣,戎顺熙.用分形方法研究负载型聚烯烃催化剂的表面形貌及其对聚合活性的影响[J].高校化学工程学报,2000,14(6):570-576. 被引量:10
  • 10王靖岱,陈纪忠,阳永荣.工业流化床聚乙烯树脂性能模型的研究[J].高校化学工程学报,2001,15(1):82-87. 被引量:17

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