Conversion of crude oil feeds by catalytic cracking
AssigneeUop LLC
InventorsGary N. Long, Regis J. Pellet, Jule A. Rabo
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Abstract
The process for conversion of crude oil feeds in the presence of a silicoaluminophosphate molecular sieve of U.S. Pat. No. 4,440,871 and/or an aluminophosphate molecular sieve of U.S. Pat. No. 4,310,440 and at least one zeolitic aluminosilicate.
Claims11
The catalytic cracking process for converting a crude oil feed to hydrocarbon products including gasolines comprising contacting a crude oil feed at effective catalytic cracking conditions at an effective catalytic cracking temperature between about 400.degree. F. and about 1400.degree. F. with a catalyst comprising at least one crystalline zeolitic aluminosilicate cracking catalyst selected from the group consisting of Zeolite Y, zeolite LZ-210 and Zeolite LZ-10 and at least one molecular sieve selected from the group consisting of the silicoaluminophosphates SAPO-5 and SAPO-11.
The catalytic cracking process for converting a crude oil feed to hydrocarbon products including gasolines comprising contacting a crude oil feed at effective catalytic cracking conditions at an effective catalytic cracking temperature between about 500.degree. F. and about 1400.degree. F. with a catalyst comprising at least one crystalline zeolitic aluminosilicate cracking catalyst selected from the group consisting of zeolite LZ-210 and zeolite LZ-10 and at least one molecular sieve selected from the group consisting of the silicoaluminophosphates SAPO-5 and SAPO-11.
The catalytic cracking process for converting a crude oil feed to hydrocarbon products including gasolines comprising contacting said feed at effective catalytic cracking conditions with a catalyst comprising at least one crystalline zeolitic aluminosilicate cracking catalyst comprising zeolite Y and at least one molecular sieve selected from the group consisting of the silicoaluminophosphates SAPO-5 and SAPO-11.
The catalytic cracking process for converting a crude oil feed to hydrocarbon products comprising gasolines comprising contacting said feed at effective catalytic cracking conditions with a catalyst comprising at least one crystalline zeolitic aluminosilicate comprising at least one of zeolite LZ-210 and zeolite LZ-10 and at least one molecular sieve comprising at least one of the silicoaluminophosphates SAPO-5 and SAPO-11.
The catalytic cracking process for converting a catalytic cracking feed to hydrocarbon products including gasolines comprising contacting said feed at effective catalytic cracking conditions with a catalyst comprising at least one crystalline zeolitic aluminosilicate cracking catalyst selected from the group consisting of zeolite LZ-210 and zeolite LZ-10 and at least one molecular sieve selected from the group consisting of SAPO-5 and SAPO-11.
Dependencies are inferred from the claim text.