化工进展

• 应用技术 • 上一篇    下一篇

液化天然气分离的节能蒸馏工艺

吕向红   

  1. 华南师范大学化学与环境学院
  • 出版日期:2008-06-05 发布日期:2008-06-05

Energy-saving distillation for separation of LNG

LÜ Xianghong   

  1. School of Chemistry & Environment,South China Normal University
  • Online:2008-06-05 Published:2008-06-05

摘要: 采用严格模拟计算的方法,对液化天然气分离过程的现有常规蒸馏工艺与热耦蒸馏工艺、侧线提馏工艺、双效蒸馏工艺和热集成工艺进行了模拟,并比较了其能量消耗。模拟计算结果显示,复杂蒸馏工艺都比常规蒸馏工艺减少了能耗和操作成本。其中,热耦蒸馏工艺可比常规蒸馏工艺节能21.4%,侧线提馏工艺节约13.3%,双效蒸馏工艺可节约34.7%,热集成工艺节约则达37.6%左右,表明新工艺在此分离过程中都有较好的应用前景,尤以多效蒸馏和热耦蒸馏最有优势。

Abstract: The processes for liquefied natural gas separation,including conventional distillation,thermally coupled distillation,side-stripper,double-effect distillation and heat-integrated distillation were simulated by using rigorous models and their energy consumptions were compared. The simulated results showed that the complex distillation processes consume much less energy and operation cost than conventional distillation. The thermally coupled distillation saves energy by 21.4%,side-stripper by 13.3%,double-effect distillation by 34.7% while heat-integrated distillation by 37.6%,against the conventional process. All the complex distillation processes have good prospects of application and double-effect distillation and thermally coupled distillation arrangements are superior.

京ICP备12046843号-2;京公网安备 11010102001994号
版权所有 © 《化工进展》编辑部
地址:北京市东城区青年湖南街13号 邮编:100011
电子信箱:hgjz@cip.com.cn
本系统由北京玛格泰克科技发展有限公司设计开发 技术支持:support@magtech.com.cn