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Preparation of Y Zeolite-Based Catalysts and Their Catalytic Cracking Performances of Venezuelan Heavy Oil

机译:基于沸石的催化剂的制备及其促甲醛重油的催化裂化性能

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Five kinds of modified Y zeolite-based fluid catalytic cracking (FCC) catalysts were prepared. The N_2 adsorption desorption and NH_3 temperature-programmed-desorption (NH_3-TPD) were used to investigate the pore structure and acidic properties of the catalysts. The effects of pore structure and acidic properties of catalysts on the catalytic cracking performance of Venezuelan heavy oil were carried out using an advanced cracking evaluation unit. The results of N_2 adsorption desorption and NH_3-TPD show that CAT-A and CAT-B catalysts with rundle pore distribution have a similar pore sizes and acidic properties. The catalytic cracking results show that the acidic properties and the pore distribution of the catalysts have obvious effects on the conversion and product distribution. The light oil yield and total liquid oil yield can reach 58.75 wt% and 73.83 wt%, respectively, under reaction temperature of 520°C.
机译:制备五种改性Y沸石的流体催化裂化(FCC)催化剂。使用N_2吸附解吸和NH_3温度编程 - 解吸(NH_3-TPD)来研究催化剂的孔结构和酸性特性。使用先进的裂解评价单位进行孔结构对委内瑞拉重油催化裂化性能的孔结构和酸性特性。 N_2吸附解吸和NH_3-TPD的结果表明,具有匝孔孔分布的CAT-A和CAT-B催化剂具有类似的孔径和酸性特性。催化裂化结果表明,催化剂的酸性特性和孔径对转化和产物分布具有明显的影响。轻质油产量和总液体油状物分别在520℃的反应温度下分别达到58.75wt%和73.83wt%。

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