馏分油浆态床加氢处理研究 I 催化剂制备方法

A study on slurrybed hydrotreating process of distillate oil:I Catalyst preparation

  • 摘要: 对浆态床加氢催化剂的制备方法、助剂和活性组分负载量进行了考察。研究结果表明,最佳的催化剂(SP25)制备方法为,采用一定粒度的γ-Al2O3微球作载体,浸渍四硫代钼酸铵的络合剂水溶液,120℃干燥12h,然后浸渍硝酸镍和磷酸二氢铵的水溶液,120℃干燥12h,在氮气气氛中500℃焙烧3h。SP25催化剂的主要物性为比表面积212.3m2/g,孔径11.3nm,孔容0.60mL/g,平均粒度17.3μm,骨架密度2.79g/cm3。制成的催化剂活性组分为硫化态,使用时不需进行预硫化。XRD和H2TPR表征结果表明,浸渍液中加入络合剂可以提高MoS2在载体表面的分散度。在反应温度350℃,压力6MPa,反应时间2h,催化剂加入量6%(占原料油质量)的反应条件下,催化剂对FCC柴油的脱硫率为85.1%,脱氮率为82.0%。

     

    Abstract: The catalyst for slurrybed hydrotreating of distillate oil was prepared; the preparation parameters like the loading of active components and phosphorus additive on the hydrotreating performance were investigated. The optimum catalyst (SP25) was obtained through impregnation of γ-Al2O3 particles with an aqueous solution of ammonium tetrathiomolybdate (ATTM) and certain complexing agent, drying at 120℃ for 12h, then impregnation with an aqueous solution nickel nitrate and ammonium dihydrogen phosphate, drying at 120℃ for 12h, at last calcined at 500℃ in N2 atmosphere for 3h. The as-prepared catalyst SP25 exhibited a specific surface area of 212.3m2/g, pore diameter of 11.3nm, pore volume of 0.60mL/g, particle size of 17.3μm, skeleton density of 2.79g/cm3; the active components in the asprepared catalyst were in sulfided form and presulfurization was not necessary before using. XRD and H2TPR suggested that the addition of complexing agent during impregnation could enhance the dispersion of MoS2 on γAl2O3. Under the conditions of 350℃, 6MPa, wcatal/woil = 6%, reaction time 2h, the efficiencies of hydrodesulfurization and hydrodenitrogenation for FCC diesel oil reached 85.1% and 82.0%, respectively.

     

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