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基于多策略扰动机制的飞蛾火焰算法及在乙烯聚合过程动力学参数估计中的应用 被引量:1

Moth-Flame Optimization Algorithm Based on Multi-Strategy Disturbance and its Application in Kinetic Parameter Estimation of Ethylene Polymerization
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摘要 针对飞蛾火焰算法(MFO)早熟和易陷入局部最优的缺点,研究提出了一种基于多策略扰动机制的飞蛾火焰算法(MSMFO)。该算法通过莱维飞行和布朗运动两种机制的随机选择对飞蛾粒子进行重新定位,以克服种群后期多样性严重下降的缺陷。通过对8个测试函数的仿真对比,MSMFO具有更高的收敛精度和更好的全局收敛能力。将MSMFO算法用于工业乙烯聚合过程动力学参数估计。以聚合反应动力学参数为决策变量,模型输出的数均分子量和重均分子量与实际值之间的相对误差平方为目标。结果证明,MSMFO算法具有更好的收敛性。 A moth flame algorithm method based on multi-strategy disturbance(MSMFO) was proposed to overcome shortcomings of maturation and local convergence of typical moth flame algorithm(MFO). This algorithm selects new positions of the moth particles by random selection of Levy flight and Brownian movement, which can overcome the decline of population diversity in late periods. As proved by simulation of eight test functions, MSMFO has higher convergence accuracy and better global convergence. Moreover, MSMFO was used in polyethylene production to minimize the square sum of relative error between the number-average molecular weight and the weight-average molecular weight with kinetic parameters as decision variables. The simulation results show that MSMFO has better convergence when comparing with ELPSO and DE algorithms.
作者 安许锋 田洲 钱锋 AN Xu-feng;TIAN Zhou;QIAN Feng(Key Laboratory of Advanced Control and Optimization for Chemical Process,Ministry of Education,East China University of Science and Technology,Shanghai 200237,Chin)
出处 《高校化学工程学报》 EI CAS CSCD 北大核心 2018年第4期918-925,共8页 Journal of Chemical Engineering of Chinese Universities
基金 国家科技支撑计划项目(2015BAF22B02) 国家自然科学基金(61725301 61333010) 中央高校基本科研业务费(222201714054)
关键词 飞蛾火焰算法 莱维飞行 布朗运动 动力学参数估计 MFO Levy flight Brownian movement kinetic parameters estimation
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  • 1UNIPOL. Proven plexible polyethylene technology[R] . 1998.
  • 2BP - AMOCO. Innovene - the polyethylene process[R]. 1999.10.
  • 3Montell polyefins. Spherilene - Montell swing LLDPE/HDPE gas technology - a new frontier in polyethelenes[R]. 1999.8.
  • 4Boreails. Borstar - The polyethylene technology[ R]. 1998. 10.
  • 5Choi 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.
  • 6Khang D Y, Lee H H. Particle size distribution in fluidized beds for catalyst polymerization [J]. Chemical Engineering Science, 1996, 52(3): 421-431.
  • 7Overturf B W. Computations for discrete cut particle size distribution in a fluidized bed reactor [J]. Powder Technology,1979, 23: 143-147.
  • 8Chen T P, Saxena S C. Particle size distribution in a fluidized bed reactor [J]. Powder Technology, 1976, 15: 283-285.
  • 9Hatzantonis 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.
  • 10Levenspiel O, Kunii D, Fitzgerald T. The processing of solids of changing size in bubbling fluidized beds [J]. Powder Technology, 1968/69, 2: 87-96.

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