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在常压下进行加氢脱氧反应,可将富含酚类的热解液体馏分转化为芳烃。

Hydro-deoxygenation at atmospheric pressure converts the phenolic-rich pyrolysis liquid fraction into aromatics.

机构信息

College of Chemical Engineering, Beijing University of Chemical Technology, 100029, Beijing, China.

College of Life Science and Technology, Beijing University of Chemical Technology, 100029, Beijing, China.

出版信息

J Environ Manage. 2022 Mar 15;306:114429. doi: 10.1016/j.jenvman.2022.114429. Epub 2022 Jan 7.

Abstract

Ambient pressure hydro-deoxygenation (HDO) of the phenolic-rich pyrolysis liquid fraction is a complex task due to the presence multiple phenolic compounds and light oxygenates. The phenolic-rich fraction differs from the overall pyrolysis liquid, known to be prone to re-polymerization and coking in the reactor or of the catalyst. In the present research, hydro-deoxygenation of oxygen-containing compounds in the phenolic fraction over Mo-based catalysts was carried out for the first time. It was found that Mo-based catalysts can successfully upgrade the phenolics into aromatics, the conversion rate was nearly 100%. The small amount of light oxygenates in the phenolic-rich fraction had no obvious effect on the hydro-deoxygenation reaction, the phenolic conversion was more than 95%. After assessing the performance for a representative phenolic model compound, the reaction was also successfully carried out on the phenolic fraction of the real pyrolysis liquid. It can be concluded that the catalysts can also be used for the HDO of the real pyrolysis liquid fraction at atmospheric pressure.

摘要

由于存在多种酚类化合物和轻含氧化合物,富含酚类的热解液体馏分的常压加氢脱氧(HDO)是一项复杂的任务。富含酚类的馏分与整体热解液体不同,已知其在反应器或催化剂中容易发生再聚合和结焦。在本研究中,首次在 Mo 基催化剂上对酚类馏分中的含氧化合物进行加氢脱氧。结果表明,Mo 基催化剂可以成功地将酚类化合物升级为芳烃,转化率接近 100%。酚类馏分中少量的轻含氧化合物对加氢脱氧反应没有明显影响,酚类转化率超过 95%。在对代表性酚类模型化合物的性能进行评估后,该反应也在实际热解液体的酚类馏分上成功进行。可以得出结论,催化剂也可以用于常压下的实际热解液体馏分的 HDO。

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