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首页> 外文期刊>The Canadian Journal of Chemical Engineering >CATALYTIC GASIFICATION OF LIGNITE WITH KOH IN SUPERCRITICAL WATER
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CATALYTIC GASIFICATION OF LIGNITE WITH KOH IN SUPERCRITICAL WATER

机译:超临界水中KOH对褐煤的催化气化

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Supercritical water gasification of lignite with KOH was investigated in a batch autoclave on a wide range of conditions, that is residence time (5-30 min), mass ratio of H2O to lignite (0.5-10), temperature (400-600°C) and mass ratio of KOH to lignite (0-20%). Although lignite is difficult to be gasified in supercritical water, the results indicated that gasification efficiency about 47% was achieved at 30 min, 550°C with 10% KOH. Higher mass ratio of H2O to lignite and temperature can lead to higher gas yields and GE. It is also observed that the solid residue was dispersed at low feed concentration and consolidated at high concentration. Besides KOH's improvement of water-gas shift reaction, in this case, it is also observed that KOH also enhances the gasification of aromatics of lignite in supercritical water, which leads to higher gasification efficiency of lignite.
机译:在间歇式高压釜中,在以下条件下研究了褐煤与KOH的超临界水气化:停留时间(5-30分钟),H2O与褐煤的质量比(0.5-10),温度(400-600°C) )和KOH与褐煤的质量比(0-20%)。尽管褐煤难以在超临界水中气化,但结果表明,在550°C,30%,10%KOH的条件下,气化效率达到了约47%。较高的H2O与褐煤质量比和温度可导致较高的气体收率和GE。还观察到固体残余物在低进料浓度下分散并在高浓度下固结。在这种情况下,除了KOH改善了水煤气变换反应之外,还观察到KOH还增强了褐煤在超临界水中的芳烃的气化,从而导致褐煤的气化效率更高。

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