Coal desulfurization with sodium hypochlorite

被引:54
作者
Li, WD [1 ]
Cho, EH [1 ]
机构
[1] W Virginia Univ, Dept Chem Engn, Morgantown, WV 26506 USA
关键词
D O I
10.1021/ef0400767
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 [动力工程及工程热物理]; 0820 [石油与天然气工程];
摘要
Wet desulfurization of Pittsburgh No. 8 coal and Illinois No. 6 coal were conducted with sodium hypochlorite in the laboratory. Pittsburgh No. 8 coal was leached by hypochlorite at high pHs in one step only. The hypochlorite concentration varied from 0.2 M to 0.6 M, the sodium hydroxide (NaOH) concentration was 0.2-0.8 M, and temperature was 80 and 90 degrees C. The desulfurization of Illinois No. 6 coal was conducted in three consecutive steps of pretreatment in concentrated ammonia at room temperature, leaching with hypochlorite at room temperature and hydrolysis in a NaOH solution at 90 degrees C. In the leaching step, the hypochlorite concentration varied from 0.2 M to 0.8 M. The desulfurization method of Pittsburgh No. 8 coal was observed to reduce mainly pyritic sulfur. More than 70% of pyritic sulfur removal was achieved at the optimum conditions of 0.4 M hypochlorite, 0.4 M NaOH, and 90 degrees C. The desulfurization method for Illinois No. 6 coal was capable of reducing significant amounts of organic sulfur. The removal of organic sulfur achieved a 37.8% reduction at the optimum operation of leaching at 0.4 M hypochlorite and room temperature, followed by hydrolysis at 0.3 M NaOH and 90 degrees C. The chlorine content in the coal produced by the chlorination during leaching was kept below the threshold value of 0.3% under the optimum conditions of the desulfurization method for each coal.
引用
收藏
页码:499 / 507
页数:9
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