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Catalytic depolymerization of a typical lignite for improving tar yield by Co and Zn catalyst

机译:钴和锌催化剂催化褐煤催化解聚提高焦油收率

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摘要

A novel process for improving tar yield through catalytic depolymerization of a typical lignite was put forward. The catalytic depolymerization of the lignite over CoCl2 and ZnCl2 catalyst in different concentrations were investigated by a Gray-King apparatus. The optimal catalyst concentrations of CoCl2 and ZnCl2 catalyst that could obtain the highest tar yield was achieved, by which the tar yield increased about 20.3% and 6.6% compared with that of the raw coal, respectively. Different with the traditional catalytic pyrolysis process for which the tar yield decreased, more tar was produced by the catalytic depolymerization method. The GC × GC-MS analysis showed that the components of alkanes and two-ring aromatics in tar increased dramatically with the addition of the optimal CoCl2 and ZnCl2 catalyst. The Raman measurement revealed that more large aromatic ring systems ( > 6 rings) were formed in the char from depolymerization with catalyst and the elemental analysis showed that the hydrogen content decreased slightly. The gas products analysis reflected the contents of methane showed an obvious decrease. All of this reflects that more fragments and small free radicals cracked were enhanced by catalysis in the catalytic depolymerization process, thereby leading to an enhancement of the tar formation possibilities.
机译:提出了一种通过催化褐煤催化解聚提高焦油收率的新方法。用Gray-King装置研究了褐煤在不同浓度的CoCl2和ZnCl2催化剂上的催化解聚反应。获得了能够获得最高焦油收率的最佳催化剂浓度的CoCl2和ZnCl2,与原煤相比,焦油收率分别提高了约20.3%和6.6%。与传统的焦油产率降低的传统催化热解方法不同,催化解聚方法可生产更多的焦油。 GC / MS分析表明,加入最佳的CoCl2和ZnCl2催化剂后,焦油中烷烃和二环芳烃的含量急剧增加。拉曼测量表明,用催化剂解聚后,在焦炭中形成了更大的芳环体系(> 6环),元素分析表明氢含量略有下降。气体产物分析表明甲烷含量呈明显下降趋势。所有这些反映出,在催化解聚过程中,通过催化作用,更多的碎片和裂开的小自由基被增强,从而导致焦油形成可能性的增加。

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