乙烯工业 ›› 2023, Vol. 35 ›› Issue (3): 29-32.

• 工业技术 • 上一篇    下一篇

乙烯精馏塔降压操作影响研究

杨丽庆   

  1. 中国石化工程建设有限公司,北京 100101
  • 收稿日期:2023-02-28 修回日期:2023-03-18 出版日期:2023-09-25 发布日期:2023-09-27
  • 作者简介:杨丽庆,女,2016年毕业于中石化石油化工科学研究院应用化学专业,硕士,主要从事乙烯分离工艺技术开发和设计工作,工程师。

Study on Influence of Depressurization Operation of Ethylene Rectification Tower

Yang Liqing   

  1. SINOPEC Engineering Incorporation, Beijing, P.C.100101
  • Received:2023-02-28 Revised:2023-03-18 Online:2023-09-25 Published:2023-09-27

摘要:

通过考察某石化乙烯装置乙烯精馏塔降压操作对塔顶冷凝器、乙烯球罐、塔负荷及循环乙烷冷量回收等方面的影响,发现塔顶冷凝器和乙烯球罐为乙烯精馏塔降压操作主要瓶颈。将塔顶冷凝和乙烯球罐改造后,乙烯精馏塔可降压(表)至1.63 MPa,节省操作费用450万元/a,改造所投入的2 700万元,预计6 a可回收投资成本。

关键词: 乙烯精馏塔  , 高压精馏  , 降压操作  , 瓶颈

Abstract:

Through investigating the influence of depressurization operation of the ethylene rectification tower in an ethylene plant on overhead condenser, ethylene sphere tank, tower load and cooling capacity recovery of cycle ethane, it is found that overhead condenser and ethylene sphere tank are the main bottlenecks of the depressurization operation. After revamping the overhead condenser and the ethylene sphere tank, the ethylene rectification tower can be depressurized to 1.63 MPa (G), saving the operating cost by 4.5 million yuan per year. It is estimated that the revamping cost of 27 million yuan can be recovered in nearly 6 years.

Key words: ethylene rectification tower, high-pressure rectification, depressurization operation, bottleneck