燃料与化工 ›› 2010, Vol. 41 ›› Issue (2): 42-.

• 煤气净化与化学产品加工 • 上一篇    下一篇

邻二甲苯制取苯酐工艺流程模拟

康振东   

  1. 上海焦化有限公司,上海 200241
  • 出版日期:2010-03-20

Simulation of producing benzene anhydride with o-xylene    

Kang    Zhendong   

  1. Shanghai Coking Company, Ltd., Shanghai   200241,  China
  • Online:2010-03-20

摘要:

利用Aspen软件对邻二甲苯制取4万t/a苯酐工艺流程进行了模拟,并对模拟结果进行了分析。轻组分塔T201中顺酐、苯甲酸、苯酞都在塔顶被除去,其中塔顶组成:苯酐25.74%,顺酐39.11%,苯甲酸25.37%,苯酞9.78%。产品塔T202塔顶除含有极少量苯甲酸、苯酞外,其余均为苯酐,塔底为重组分,满足分离要求。在实际生产中,轻组分中苯酐含量约为50%,因此生产操作中可以加大回流比,优化操作。

Abstract:

The process of producing 40 000 t/a benzene anhydride with o-xylene by means of Aspen software was simulated, and the simulation results were analyzed. Cis-butendioic anhydride, benzoic acid and phthalide in light fraction column T201 were removed on the column top, the overhead component: benezene anhydride 25.74%, cis-butendioic anhydride 39.11%,  benzoic acid 25.37%, phthalide 9.78%. For product column T202 top, except that very small amount of benzoic acid and  phthalide were contained, the rest was benzene anhydride, the column bottom was heavy component, which can meet the separation requirement. In actual production, benzene anhydride content in light fraction was about 50%, therefore the reflux ratio in production operation can be enlarged, which can optimize the operation.

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