ISSN 1008-5548

CN 37-1316/TU

Journal Online  2018 Vol.24
<Go BackNo.1

Catalytic gasification of metallurgical coke

BAI Boyang, GUO Qingjie, HU Xiude, AN Mei, WU Wei, LI Yankun

(School of Chemistry and Chemical Engineering; State Key Laboratory of High-efficiency Coal Utilization and Green Chemical Engineering, Ningxia University, Yinchuan 750021,China)

Abstract:The effect of 3 kinds of cheap catalysts,Na2CO3,Fe(NO3)3 and CaO,on the steam gasification reaction of metallurgical broken coke were investigate using the thermo-gravimetric analyzer and the steam as the gasifier.The catalytic gasification kinetics was discussed.The results show that the gasification temperature of the coke decreases about 170 ℃after the addition of the catalyst.The catalytic activity of Na2CO3 is the highest among the three catalysts.With the increase of Na2CO3 loading (sodium ion loading are 1%, 3%, 5% and 10%, mass fractions) ,the gasification rate of the cokes are improved, about 5% of the Na2CO3 loading reaches saturation,the excess catalyst can't effectively improve the gasification rate of coke.The addition of Na2CO3 effectively reduces the activation energy of the coke gasification reaction,thus increasing the reaction rate.Gasification of coke with added Na2CO3,the shrinking core model can well reflect the kinetics of coke gasification.

Keywords: metallurgical coke; thermo-gravimetric analyzer; catalytic gasification; shrinking core model

中图分类号:TQ544          文献标志码:A

文章编号:1008-5548(2018)01-0041-05

DOI:10.13732/j.issn.1008-5548.2018.01.008

收稿日期:2017-07-28, 修回日期:2017-09-22,在线出版时间:2018-02-25。

基金项目:宁夏重点研发项目,编号:2016BY005。

第一作者简介:白柏杨(1994—),男,硕士研究生,研究方向为煤化学链气化。E-mail:baiboyang12315@163.com。

通信作者简介:郭庆杰(1967—),男,博士,教授,博士生导师,研究方向为清洁化工。E-mail:qingjie_guo@163.com。