华南理工大学学报(自然科学版) ›› 2007, Vol. 35 ›› Issue (7): 62-66.

• 化学化工 • 上一篇    下一篇

液化天然气中轻烃分离工艺的优化设计

熊永强 李亚军 华贲   

  1. 华南理工大学 强化传热与过程节能教育部重点实验室,广东 广州 510640
  • 收稿日期:2006-11-14 出版日期:2007-07-25 发布日期:2007-07-25
  • 通信作者: 熊永强(1978-),男,博士生,主要从事液化天然气利用研究. E-mail:yqxiongI978@163.com
  • 作者简介:熊永强(1978-),男,博士生,主要从事液化天然气利用研究.
  • 基金资助:

    国家重点基础研究开发规划项目( G2000026307 )

Optimized Design of Recovery Process of Light Hydrocarbons from LNG

Xiong Yong-qiang  Li ya-jun  Hua Ben   

  1. Key Laboratory of Enhanced Heat Transfer and Energy Conservation of the Ministry of Education ,South China Univ. of Tech. , Guangzhou 510640 , Guangdong , China
  • Received:2006-11-14 Online:2007-07-25 Published:2007-07-25
  • Contact: 熊永强(1978-),男,博士生,主要从事液化天然气利用研究. E-mail:yqxiongI978@163.com
  • About author:熊永强(1978-),男,博士生,主要从事液化天然气利用研究.
  • Supported by:

    国家重点基础研究开发规划项目( G2000026307 )

摘要: 根据液化天然气(LNG) 冷量的特性,按照冷量梯级利用的原则,设计了一种新的LNG 轻烃分离流程,其特征在于轻烃分离过程不需要使用压缩机,能耗较低,而且可利用LNG 的冷量将一部分分离完轻烃的甲烷再液化过冷并低压液相储存,使轻烃分离流程具有供气调峰功能,同时使分离获得的轻烃产品保持低压液相,方便产品的储运和销售.文中还以深圳项目进口的3.7 x106 t/a 澳大利亚LNG 为例,利用此流程进行轻烃分离的模拟计算.结果表明:相对现有L 艺,新流程功耗降低47.3% ,脱甲烷塔的热负荷降低27.3% ,且能够将20% 左右的甲烷低压储存用于供气调峰,经济效益明显;如将获得的C2 轻烃替代石脑油用于裂解制乙烯,可以降低乙烯装直的投资、生产能耗及成本.

关键词: 液化天然气, 冷量, C2轻烃分离, 流程优化, 流程设计

Abstract:

According to the characteristics of the cold energy of liquefied natural gas (LNG) , a new recovery process of light hydrocarbons from liquefied natural gas was presented based on the gradient utilization of cold energy.The proposed recovery process was performed without using any gas compressor , and the cold energy of LNG was used to re-liquefy the methane-rich residual gas and to re-condense and store the methane in tanks in low-pressure liquid phase , the process was of the function of peak shaving , and the recovered light hydrocarbons in low-pressure liquid phase were easy to store and sell. Then , a case study of applying the process was carried out for the imported3.7 X 106 t/a LNG from Australia by Shenzhen. The results indicate that , as compared with the conventional technologies, the proposed process can reduce the power consumption by 47.3% and decrease the heat load by 27.3% ,that approximately 20% of the methane-rich residual gas is re-condensed and stored in tanks in low-pressure liquid phase for the peak shaving of natural gas downstream system by vaporizing it , that the C2hydrocarbons recovered from LNG can be used as a substitution for naphtha and the feed of ethylene unit , with the advantages in decreasing the investment and saving the energy consumption and the cost.

Key words: liquefied natural gas, cold energy, C2 light hydrocarbon recovery, process optimization, process deslgn