化工进展

• 化工过程与装备 • 上一篇    下一篇

铁基活性组分对COS的吸附及催化转化作用

任秀蓉1,2,王海堂1,3,常丽萍1   

  1. 1太原理工大学煤科学与技术教育部和山西省重点实验室,山西 太原 030024;2太原理工大学现代科技学院,山西 太原 030021;3山西焦化设计研究院,山西 太原 030024
  • 出版日期:2011-10-05 发布日期:2011-10-05

Adsorption performance and catalytic conversion of iron-based active components on COS

REN Xiurong1,2,WANG Haitang1,3,CHANG Liping1   

  1. 1Key Laboratory of Coal Science and Technology,Taiyuan University of Technology,Taiyuan 030024,Shanxi,China;2Polytechnic Institute,Taiyuan University of Technology,Taiyuan 030021,Shanxi,China;3 Coking Design Institute of Shanxi Taiyuan 030024,Shanxi,China
  • Online:2011-10-05 Published:2011-10-05

摘要:

采用共沉淀法制备了脱硫用铁基吸附剂的主要活性组分Fe2O3,并对其进行还原处理,制备了不同价态的含铁组分Fe3O4Fe。使用固定床反应装置分别考察了三者在400500 范围内、COS / N2H2 / COS / N2两种气氛下对COS的吸附和催化转化的行为。结果表明:在COS / N2气氛下,三者对COS均有吸附,其吸附能力随温度的变化而异,不同温度下三者对COS吸附的硫容顺序为:Fe2O3>Fe3O4>Fe400450);Fe3O4> Fe2O3>Fe500)。H2 /COS / N2 /气氛下,COS的氢解反应随着温度的升高而增强,各活性组分的硫化产物对COS的氢解反应都具有一定的催化作用,这对于抑制H2SCOS转化具有积极的作用。

Abstract:

The iron-based active componentFe2O3was prepared by co-precipitation method. Fe3O4 and Fewere also prepared by reducing Fe2O3 at different temperature for different time. The adsorption behavior of them was investigated in COS/N2 and H2/COS/N2 gas streams using the fixed bed reactor at 400 450 and 500 respectively. The results show that all three active components can adsorb COS and their adsorption ability varies with temperature. At 500 the sulfur capacity of Fe3O4 is the highestand that of Fe is the lowest. While at the temperatures of 450 and 400 the sulfur capacity has the following sequenceFe2O3 > Fe3O4 > Fe. In H2/COS/N2 gas streamthe reaction of COS hydrogenolysis is enhanced by increasing temperature. The iron sulfides have certain catalysis on COS hydrogenolysis and it has an active influence on inhibition of conversion from H2S to COS.

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