石油炼制与化工 ›› 2019, Vol. 50 ›› Issue (4): 64-68.

• 控制与优化 • 上一篇    下一篇

丙烯精馏塔节能及扩能优化方案研究

戴薇薇,谢恪谦,张星,王英龙,吕丰财,刘晓燕   

  1. 中石油华东设计院有限公司
  • 收稿日期:2018-08-28 修回日期:2018-12-12 出版日期:2019-04-12 发布日期:2019-04-28
  • 通讯作者: 戴薇薇 E-mail:daiweiwei@cnpccei.cn
  • 基金资助:
     

STUDY ON OPTIMIZATION SCHEME OF ENERGY SAVING AND CAPACITY EXPANSION OF PROPYLENE DISTILLATION COLUMN

    

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  • Received:2018-08-28 Revised:2018-12-12 Online:2019-04-12 Published:2019-04-28
  • Supported by:
     

摘要: 为探讨丙烯精馏塔进料位置以及塔板数对能耗的影响,在控制最优进料位置变量的基础上,通过ProII软件流程模拟与Origin软件数据拟合,得到一定进料组成时,塔底重沸器负荷与塔板数的方程表达式,发现丙烯精馏塔的热负荷随着塔板数的增加而降低,且降低的幅度逐渐减小并最终到达极值。并结合公用工程与设备造价,为新建或改造丙烯精馏塔的具体方案提供一定的理论支持。在老厂改造时,可通过优化进料位置或增加塔板数,达到节能降耗及扩能增产的目的。

关键词: 丙烯精馏塔, 流程模拟, 节能优化, 扩能

Abstract: The influence of the feeding position and the number of trays on the energy consumption of the propylene fractionator was explored. Based on the control of the optimal feeding position variables,ProII process simulation and Origin data fitting were applied to obtain a certain feed composition and the expression of the reboiler load and the number of trays. The results showed that the thermal load of the propylene fractionator decreased with the increase of the number of trays,and the decreasing amplitude gradually decreased and finally reached a extreme value. Combined with the cost of utility and equipment,the work can provide certain theoretical support for the specific plan for the new-built or reformed propylene fractionator. When the old factory is reconstructed,the purpose of capacity expanding or reducing energy consumption can be achieved by optimizing the feeding position or increasing the number of trays.

Key words: propylene fractionator, process simulation, energy saving, capacity expansion

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