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Recycling the CoMo/Al2O3 catalyst for effectively hydro-upgrading shale oil with high sulfur content and viscosity

机译:再循环COMO / AL2O3催化剂,以具有高硫含量和粘度的高压升级页岩油

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Hydrotreatment is an effective upgrading technology for removing contaminants and saturating double bonds. Still, few studies have reported the hydro-upgrading of shale oil, with unusually high sulfur (13200 ppm) content, using the CoMo/Al _(2) O _(3) catalyst. Here we report an extensive study on the upgrading of shale oil by hydrotreatment in a stirred batch autoclave reactor (500 ml) for sulfur removal and viscosity reduction. From a preliminary optimization of the reaction factors, the best-operating conditions were 400 °C, an initial H _(2) -pressure of 5 MPa, and an agitation rate of 800 rpm, a catalyst-to-oil ratio of 0.1, and a reaction time of 1 h. We could achieve a sulfur removal efficiency of 87.1% and 88.2% viscosity reduction under the optimal conditions. After that, the spent CoMo/Al _(2) O _(3) was repeatedly used for subsequent upgrading tests without any form of pre-treatment. The results showed an increase in the sulfur removal efficiency with an increase in the number of catalyst runs. Ultimately, 99.5–99.9% sulfur removal from the shale oil was achieved by recycling the spent material. Both the fresh and the spent CoMo/Al _(2) O _(3) were characterized and analyzed to ascertain their transformation levels by XRD, TEM, TG, XPS, TPD and N _(2) adsorption analysis. The increasing HDS efficiency is attributed to the continuing rise in the sulfidation degree of the catalyst in the sulfur-rich shale oil. The light fraction component in the liquid products (IBP–180 °C) was 30–37 vol% higher than in the fresh shale oil. The product oil can meet the sulfur content requirement of the national standard marine fuel (GB17411-2015/XG1-2018) of China.
机译:加氢处理是一种用于去除污染物和饱和双键的有效升级技术。尽管如此,仍有少数研究报告了岩油油的升级,具有异常高的硫(13200ppm)含量,使用COMO / Al _(2)O _(3)催化剂。在这里,我们报告了对搅拌批量高压釜反应器(500mL)中的加氢处理升级的岩土油的广泛研究,用于硫去除和粘度降低。从反应因子的初步优化,最佳操作条件为400°C,初始H _(2)缓和5MPa,搅拌速率为800 rpm,催化剂与油比为0.1,和1小时的反应时间。我们可以在最佳条件下达到87.1%和88.2%粘度降低87.1%和88.2%的粘度降低。之后,在没有任何形式的预处理的情况下重复使用废物COM / Al _(2)O _(3)进行后续升级试验。结果表明硫去除效率的增加随着催化剂的数量的增加而增加。最终,通过回收废料,实现了来自页岩油的99.5-99.9%硫去除。特征和分析新鲜和废的COMO / AL _(2)O _(3),以通过XRD,TEM,TG,XPS,TPD和N _(2)吸附分析来确定其转化水平。随着HDS效率的增加归因于富含硫的页岩油中催化剂的硫化程度的持续上升。液体产物(IBP-180℃)中的光馏分组分比新鲜页岩油高30-37体积%。产品油可以满足中国国家标准海洋燃料(GB17411-2015 / XG1-2018)的硫磺含量要求。

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