石油炼制与化工 ›› 2016, Vol. 47 ›› Issue (6): 25-27.

• 加工工艺 • 上一篇    下一篇

胺液中Na+对脱硫过程的影响及对策

朱卫东,董克林   

  1. 大连西太平洋石油化工有限公司
  • 收稿日期:2016-04-26 修回日期:2016-04-12 出版日期:2016-06-12 发布日期:2016-06-02
  • 通讯作者: 朱卫东 E-mail:zhuweidong@wepec.com

INFLUENCE OF Na+ IN AMINE SOLUTION ON DESULFURIZATION AND COUNTERMEASURE

  • Received:2016-04-26 Revised:2016-04-12 Online:2016-06-12 Published:2016-06-02

摘要:

针对大连西太平洋石油化工有限公司硫磺装置胺液脱硫系统在运行过程中出现贫胺液中硫化氢含量过高,脱硫后气体中硫化氢含量超标等问题。研究发现胺液中含有大量的Na+(高达7 800 ?g/g)是导致上述现象的主要原因。经实验室多次试验后,确定采用离子交换方法脱除胺液中的Na+,工业应用后检测脱钠后的贫胺液中硫化氢含量由4.0 g/L降低到1.5 g/L,气体脱硫深度显著提高,同时脱硫系统蒸汽使用量减少8 t/h。

关键词: 钠离子, 贫胺液, 富胺液, 硫化氢

Abstract:

The problems which hydrogen sulfide (H2S) content in lean amine and desulfurized gas is not on-standard was appeared in West Pacific Petrochemical Co., Ltd. Dalian sulfur recovery plant amine desulfurization system during process operation. It is found that the main reason of the above problem is there was large amount of sodium ions (up to 7800ppm) in amine solution. With many experiments in lab, the ion exchange method is used to remove sodium ion from the amine solution. The hydrogen sulfide content analyzed in the sodium-removed lean amine solution reduced from 4g/L to 1.5g/L in industrial application, and gas desulphurization depth is increased significantly. Meanwhile desulfurization system steam usage decreased by 8t/h.

Key words: sodium ion, lean amine, rich amine solution, hydrogen sulfide