Optimization of syngas production by non-catalytic partial oxidation of coke oven gas

被引：2
|
作者：
Zhang, G. [1 ,2 ,3 ]
Jia, Y. [1 ]
Xu, Y. [1 ]
Tian, C. [1 ]
Zhang, Y. [1 ]
机构：
[1] Taiyuan Univ Technol, Key Lab Coal Sci & Technol, Minist Educ & Shanxi Prov, Taiyuan 030024, Peoples R China
[2] Univ Western Australia, Ctr Energy, Crawley Perth, Australia
[3] State Key Lab Coal & CBM Co Min, Jincheng, Shanxi, Peoples R China
来源：
ENERGY SOURCES PART A-RECOVERY UTILIZATION AND ENVIRONMENTAL EFFECTS | 2016年 / 38卷 / 21期
基金：
中国国家自然科学基金;
关键词：
Coke oven gas; non-catalytic partial oxidation; optimization; self-designed reactor; syngas;
D O I：
10.1080/15567036.2015.1138002
中图分类号：
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号：
0807 ; 0820 ;
摘要：
Optimization of syngas production by non-catalytic partial oxidation of coke oven gas was carried out on a self-designed reactor. Tests were carried out to study the effects of volute and partial oxidation burners on the body the distribution of temperature and conversion. It was found that the partial oxidation burner can show desirable temperature distribution compared with the volute burner, under pure oxygen condition. As a result, it can improve the methane conversion and low oxygen consumption. Methane content in product gas can be reduced from 17 to 1%. The optimum operation conditions were: oxygen flow 9 m(3)/h, oxygen-coke oven gas 0.24-0.26, upper temperature of rector 1200-1250 degrees C, and outlet temperature 960-1000 degrees C.
引用
收藏
页码：3229 / 3235
页数：7
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