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An improvement of MCM-41 supported phosphoric acid catalyst for alkylation desulfurization of fluid catalytic cracking gasoline

机译:MCM-41负载型磷酸催化剂对流化催化裂化汽油烷基化脱硫的改进

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摘要

The theoretical calculation about the catalytic mechanism of MCM-41 supported phosphoric acid (SPAM) in the alkylation desulfurization of fluid catalytic cracking (FCC) gasoline demonstrated that properly reducing the amount of effective acid on the surface was beneficial to further enhancing the catalyst performance. Based on the previously optimized preparation of SPAM (weight ratio of total acid/MCM-41 6:1, calcination temperature 773 K and weigh ratio of H_3PO_4/H_4P_2O_7 1:2.5), an improvement by diluting the concentration of mixed phosphoric acids in the impregnating solution was carried out in this work. The surface structure and catalytic behavior of improved SPAM were investigated by structural characterization and experimental verification, respectively. The results proved that decreasing the concentration of mixed phosphoric acids in the impregnating solution in the preparation of SPAM could effectively reduce the existing acid amount on the catalyst surface by increasing the catalyst crystallinity, and both the surface acid strength and the total acids amount of SPAM were reduced. Moreover, the catalytic activity and selectivity of improved SPAM for thiophenic sulfurs alkylation in the alkylation desulfurization were enhanced and the olefins polymerization reactions were suppressed to a lower extent. Besides, the theoretical calculation was verified by this study, which opened a particularly appealing opportunity for the application of SPAM in the industrial alkylation desulfurization of gasoline.
机译:关于MCM-41负载磷酸(SPAM)在流化催化裂化(FCC)汽油的烷基化脱硫中催化机理的理论计算表明,适当减少表面有效酸的量有利于进一步提高催化剂的性能。基于先前优化的SPAM制备方法(总酸/ MCM-41的重量比为6:1,煅烧温度为773 K,H_3PO_4 / H_4P_2O_7的重量比为1:2.5),通过稀释混合磷酸的浓度来进行改进。在这项工作中进行了浸渍溶液。分别通过结构表征和实验验证研究了改性SPAM的表面结构和催化性能。结果表明,降低SPAM制备过程中浸渍液中混合磷酸的浓度,可以通过增加催化剂的结晶度,有效减少催化剂表面上现有的酸量,同时提高SPAM的表面酸强度和总酸量。减少了。此外,在烷基化脱硫中,改进的SPAM对噻吩硫烷基化的催化活性和选择性得到增强,并且烯烃聚合反应被抑制到较低程度。此外,本研究验证了理论计算,为SPAM在汽油工业烷基化脱硫中的应用提供了特别有吸引力的机会。

著录项

  • 来源
    《Fuel》 |2015年第1期|504-511|共8页
  • 作者单位

    Key Laboratory of Poyang Lake Environment and Resource Utilization, School of Environmental and Chemistry Engineering, Nanchang University, Nanchang 330031, PR China;

    Key Laboratory of Poyang Lake Environment and Resource Utilization, School of Environmental and Chemistry Engineering, Nanchang University, Nanchang 330031, PR China;

    Key Laboratory for Green Chemical Technology, School of Chemical Engineering & Technology, Tianjin University, Tianjin 300072, PR China;

    Department of Chemistry, Nankai University, Tianjin 300071, PR China;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Alkylation; Desulfurization; FCC gasoline; Solid phosphoric acid catalyst;

    机译:烷基化;脱硫FCC汽油;固体磷酸催化剂;

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