SCI和EI收录∣中国化工学会会刊

›› 2011, Vol. 19 ›› Issue (1): 89-96.

• • 上一篇    下一篇

Dynamic Simulation and Analysis of Industrial Purified Terephthalic Acid Solvent Dehydration Process

李澄非   

  1. Wuyi University, Jiangmen 529020, China
  • 收稿日期:2009-12-11 修回日期:2010-07-12 出版日期:2011-02-28 发布日期:2011-02-28
  • 通讯作者: LI Chengfei, E-mail: chengfeili@sina.com.cn
  • 基金资助:
    Supported by the National Natural Science Foundation of China(61072127);the Outstanding Young Innovative Personnel Project of Guangdong Colleges(LYM08098)

Dynamic Simulation and Analysis of Industrial Purified Terephthalic Acid Solvent Dehydration Process

LI Chengfei   

  1. Wuyi University, Jiangmen 529020, China
  • Received:2009-12-11 Revised:2010-07-12 Online:2011-02-28 Published:2011-02-28
  • Supported by:
    Supported by the National Natural Science Foundation of China(61072127);the Outstanding Young Innovative Personnel Project of Guangdong Colleges(LYM08098)

摘要: Dynamic model for dehydration process of industrial purified terephthalic acid solvent is investigated to understand and characterize the process.A temperature differential expression is presented,which ensures the equation to convergence and short computation time.The model is used to study the dynamic behavior of an azeotropic distillation column separating acetic acid and water using n-butyl acetate as the entrainer.Responses of the column to feed flow and aqueous reflux flow are simulated.The movement of temperature front is also simulated.The comparison between simulation and industrial values shows that the model and algorithm are effective.On the basis of simulation and analysis,control strategy,online optimization and so on can be implemented effectively in dehydration process of purified terephthalic acid solvent.

关键词: dynamic simulation, purified terephthalic acid, solvent dehydration, azeotropy

Abstract: Dynamic model for dehydration process of industrial purified terephthalic acid solvent is investigated to understand and characterize the process.A temperature differential expression is presented,which ensures the equation to convergence and short computation time.The model is used to study the dynamic behavior of an azeotropic distillation column separating acetic acid and water using n-butyl acetate as the entrainer.Responses of the column to feed flow and aqueous reflux flow are simulated.The movement of temperature front is also simulated.The comparison between simulation and industrial values shows that the model and algorithm are effective.On the basis of simulation and analysis,control strategy,online optimization and so on can be implemented effectively in dehydration process of purified terephthalic acid solvent.

Key words: dynamic simulation, purified terephthalic acid, solvent dehydration, azeotropy