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Amorphous TiO_2 and SiO_2 Modified Alumina as Catalyst Support for Hydroprocessing of Maya Crude Oil Heavy Fractions

机译:非晶态TiO_2和SiO_2改性的氧化铝作为玛雅原油重馏分加氢处理的催化剂载体

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A series of aluminas modified with 3-15 wt% SiO_2 (AMASAs) and 2-9 wt% TiO_2 (AMATAs) were prepared by a deposition and/or coprecipitation methods. The pore size distribution was varied by means of a pH-swing procedure where alternating pH acid-alkaline values generated 100-200 A pores, particularly in the AMASAs case. However, the incorporation of TiO_2 in the AMATAs even after the pH-swing procedure results in a pore size and volume decrease The degree of TiO_2 reduction is much higher in AMATAs obtained by deposition than those obtained by coprecipitation. The use of AMASAs as catalyst supports of 2.4 wt% Ni and 8.8 wt% Mo in the hydroconversion of a vacuum distillation residue brings about 1.5 times higher conversion to lighter fractions in comparison with a commercial alumina-based catalyst. AMATA-based catalyst shows similar activity and selectivity to the commercial catalyst. However, the presence of TiO_2 (6 wt%) considerably increases the N and V removal, and decreases the formation of sediments.
机译:通过沉积和/或共沉淀方法制备了一系列用3-15 wt%SiO_2(AMASAs)和2-9 wt%TiO_2(AMATAs)改性的氧化铝。孔径分布是通过pH摇摆程序改变的,其中交替的pH酸碱性值会生成100-200 A的孔,尤其是在AMASAs情况下。但是,即使在pH波动程序之后,在AMATA中掺入TiO_2也会导致孔径和体积减小。通过沉积获得的AMATA中的TiO_2还原度比通过共沉淀获得的TiO_2还原度高得多。与市售氧化铝基催化剂相比,在真空蒸馏残渣的加氢转化中使用AMASAs作为2.4 wt%Ni和8.8 wt%Mo的催化剂载体,转化为轻质馏分的转化率高约1.5倍。 AMATA基催化剂显示出与市售催化剂相似的活性和选择性。但是,TiO_2(6 wt%)的存在显着增加了N和V的去除,并减少了沉积物的形成。

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