Catalyst composition for treating heavy feedstocks
AssigneeState Key Laboratory of Heavy Oil Processing
InventorsBaojian Shen, Jinsen Gao, Chunming Xu, Liang Zhao, Xianfeng Li, Pei Wu
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Abstract
The present invention provides a catalyst and a process for its preparation and its use in cracking heavy feedstocks. The catalyst comprises one or more zeolites having a controlled silica to alumina ratio and preferably treated with alkali in the presence of a matrix component selected from the group consisting of clays, synthetic matrix other than pillared clay, and mixtures thereof. The catalyst are particularly useful in treating heavy feedstock such as residues from oil sands processing.
Claims14
A process for preparing a modified zeolite catalyst comprising forming a slurry of from 15 to 55 weight % of a matrix component selected from the group consisting of clays, synthetic matrix other than pillared clay, and mixtures thereof and from 10 to 20 weight % of a sol or gel of a binder selected from the group consisting of oxides of aluminum, silicon, and mixtures thereof and from 0 to 15 weight % of an oxide of a group IVB or VB metal adding thereto from 10 to 75 weight % of a mixture of one or more zeolites selected from the group consisting of:
- (i) not less than 10 weight %, based on the total weight of zeolites, of a zeolite having a silica to alumina ratio from 25 to 200 and up to 12 rings in a structural unit which has been treated with less than 0.5 molar alkaline solution at a temperature from 20° C. to 350° C. to reduce the silica to alumina ratio to less than 45, said alkaline treated zeolite having a meso-large pore BET surface area of greater than 50 m2/g;
- (ii) a zeolite having a silica alumina ratio from 10 to 70 and up to 12 rings in a structural unit and a meso large pore size BET surface area less than 40 m2/g;
- (iii) a beta zeolite having a structure in which the silica to aluminum ratio is less than 100;
- (iv) a Y-faujasite type zeolite having a structure in which silica to alumina ratio is less than 30;
- the sum of components (i), (ii), (iii) and (iv) adding up to 100 weight % of the zeolite components in said catalysts,
- wherein one or more of said zeolite components have been subjected to one or more of the following treatments
- (a) impregnating said zeolite with a phosphorus compound to provide from 0.2 to 15 weight % calculated as P2O5 based on the weight of the zeolite and either currently or subsequently treating the impregnated zeolite with steam or water at a temperature from 110° C. to 800° C. at a pressure from 103.3 kPa to 6.89×103 kPa for a time from 0.1 to 20 hours;
- (b) treating said zeolite with one or more group IVB, VB, VIB and VIII metal compounds to provide from 0.1 to 10 weight % of the metal based on the weight of the zeolite;
- (c) treating said zeolite with one or more rare earth compounds to provide from 0.1 to 10 weight % of the oxide of the rare earth metal based on the weight of the zeolite;
- forming particulates of said catalyst having a size from 0.001 to 0.8 mm.
Dependencies are inferred from the claim text.