MTW-zeolite as support for second stage hydrocracking catalysts with improved selectivity and cold flow property of distillate products
AssigneeChevron U.S.A. Inc.
InventorsBi-Zeng Zhan, Tracy M. Davis, Ann Jia-Bao Liang
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Abstract
The present process comprises hydrocracking a hydrocarbon feed in a first stage. The catalyst in the first stage is a conventional hydrocracking catalyst. The product from the first stage can then be transferred to a second hydrocracking stage. The catalyst used in the second stage of the present hydrocracking process comprises a base impregnated with metals from Group 6 and Groups 8 through 10 of the Periodic Table. The base of the catalyst used in the present second hydrocracking stage comprises alumina, an amorphous silica-alumina (ASA) material, a USY zeolite and zeolite ZSM-12.
Claims22
A hydrocracking catalyst comprising a catalyst support base of alumina, an amorphous silicia-alumina, a USY zeolite and ZSM-12, wherein the hydrocracking catalyst comprises a modifying agent, and wherein the modifying agent is selected from the group consisting of compounds represented by structures (1) through (4), and condensated forms thereof:
- wherein:
- (1) R1, R2 and R3 are independently selected from the group consisting of hydrogen;
- hydroxyl;
- methyl;
- amine;
- and linear or branched, substituted or unsubstituted C1-C3 alkyl groups, C1-C3 alkenyl groups, C1-C3 hydroxyalkyl groups, C1-C3 alkoxyalkyl groups, C1-C3 aminoalkyl groups, C1-C3 oxoalkyl groups, C1-C3 carboxyalkyl groups, C1-C3 aminocarboxyalkyl groups and C1-C3 hydroxycarboxyalkyl groups;
- (2) R4 through R10 are independently selected from the group consisting of hydrogen;
- hydroxyl;
- and linear or branched, substituted or unsubstituted C2-C3 carboxyalkyl groups;
- and
- (3) R11 is selected from the group consisting of linear or branched, saturated and unsaturated, substituted or unsubstituted C1-C3 alkyl groups, C1-C3 hydroxyalkyl groups, and C1-C3 oxoalkyl groups.
Dependencies are inferred from the claim text.