华南理工大学学报(自然科学版) ›› 2009, Vol. 37 ›› Issue (3): 62-66.

• 化学化工 • 上一篇    下一篇

乙烯深冷分离工艺中LNG冷能的利用

李亚军 尹华   

  1. 华南理工大学 传热强化与过程节能教育部重点实验室, 广东 广州 510640
  • 收稿日期:2008-04-01 修回日期:2008-06-02 出版日期:2009-03-25 发布日期:2009-03-25
  • 通信作者: 李亚军(1969-),女,副教授,主要从事化工过程能量优化、天然气高效利用的研究 E-mail:liyajun@scut.edu.cn
  • 作者简介:李亚军(1969-),女,副教授,主要从事化工过程能量优化、天然气高效利用的研究.

Utilization of Cryogenic Energy of LNG in Ethylene Cryogenic Separation Process

Li Ya-jun  Yin Hua   

  1. Key Laboratory of Enhanced Heat Transfer and Energy Conservation of the Ministry of Education, South China University of Technology, Guangzhou 510640, Guangdong, China
  • Received:2008-04-01 Revised:2008-06-02 Online:2009-03-25 Published:2009-03-25
  • Contact: 李亚军(1969-),女,副教授,主要从事化工过程能量优化、天然气高效利用的研究 E-mail:liyajun@scut.edu.cn
  • About author:李亚军(1969-),女,副教授,主要从事化工过程能量优化、天然气高效利用的研究.

摘要: 为解决传统乙烯深冷分离工艺中压缩制冷系统能耗高的问题,以30万吨/年乙烯深冷分离装置为研究对象,将液化天然气(LNG)冷能用于乙烯深冷分离工艺,取代部分压缩制冷负荷.研究结果表明:LNG冷能在乙烯分离工艺中的利用率达76.5%,可替代原工艺中约22 472 kW的冷量负荷,节省约11 968 kW的冷剂压缩制冷系统功耗,大幅度降低乙烯深冷分离装置的能耗成本.

关键词: 液化天然气, 冷能利用, 乙烯, 深冷分离, 压缩制冷

Abstract:

In the conventional ethylene cryogenic separation process, the compression refrigeration system consumes a lot of cryogenic energy. In order to solve this problem, the cryogenic energy of liquefied natural gas (LNG) is applied to ethylene cryogenic separation process to reduce the compression refrigeration load. Experimental results of a ethylene cryogenic separation system with an annual output of 300kt/a indicate that the utilization rate of LNG cryogenic energy in the separation process reaches 76. 5%, and that LNG provides a cryogenic energy of 22472 kW, which results in a direct compression power saving of 11968 kW and greatly reduces the energy consumption of ethylene cryogenic separation process.

Key words: liquefied natural gas, cryogenic energy utilization, ethylene, cryogenic separation, compression refrigeration