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MODIFIED Y MOLECULAR SIEVE, CATALYTIC CRACKING CATALYST CONTAINING SAME, AND PREPARATION THEREFOR AND APPLICATION THEREOF

机译:改性Y分子筛,含有相同分子筛的催化裂化催化剂及其制备和应用

摘要

A modified Y molecular sieve, the preparation method therefor, a catalytic cracking catalyst, and the application thereof. In the modified Y molecular sieve, the rare earth content calculated on the basis of oxides is 4-11wt%, and the content of P calculated on the basis of P 2O 5 is 0.05-10wt%, the content of Na calculated on the basis of sodium oxide does not exceed about 0.5wt%, and the content of active elements calculated on the basis of oxides is 0.1-5wt%, and the active elements are gallium and / or boron. The total pore volume of the molecular sieve is 0.36-0.48mL/g, the pore volume of secondary pores with a pore diameter of 2-100nm accounts for 20-40% of the total pore volume, the cell constant is 2.440-2.455nm, and the lattice collapse temperature is not lower than about 1060 ° C, the percentage of non-framework aluminum content in the total aluminum content is not higher than about 10%, and the ratio of B acid to L acid in the strong acid amount is not lower than about 3.5. The modified Y molecular sieve is obtained through ion exchange with a rare earth salt solution, hydrothermal ultra-stable modification, gas-phase ultra-stable modification, acid treatment, phosphorus modification, and active element solution impregnation and baking. A catalytic cracking catalyst containing the modified Y molecular sieve, when used in catalytic cracking of hydrogenated light cycle oil (LCO), has higher hydrogenated LCO conversion rate, lower coke selectivity, and higher BTX light aromatic hydrocarbon enriched gasoline yield and the total yield of ethylene and propylene.
机译:改性的y分子筛,其制备方法,催化裂化催化剂及其应用。在改性Y分子筛中,以氧化物为基础计算的稀土含量为4-11wt%,以P 2 O 5 > 0.05-10wt%,基于氧化钠计算的Na的含量不超过约0.5wt%,并且基于氧化物计算的活性元素的含量为0.1-5wt%,并且活性元素为镓。和/或硼。分子筛的总孔体积为0.36-0.48mL / g,孔径为2-100nm的二级孔的孔体积占总孔体积的20-40%,细胞常数为2.440-2.455nm ,且晶格崩解温度不低于约1060℃,非骨架铝含量在总铝含量中的百分比不高于约10%,并且B酸与L酸的比例在强酸中不低于3.5。改性的Y分子筛是通过与稀土盐溶液进行离子交换,水热超稳定改性,气相超稳定改性,酸处理,磷改性以及活性元素溶液的浸渍和烘烤而获得的。含有改性Y分子筛的催化裂化催化剂用于氢化轻质循环油(LCO)的催化裂化时,具有较高的氢化LCO转化率,较低的焦炭选择性和较高的BTX轻质芳烃富集汽油收率和总收率。乙烯和丙烯。

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