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US 10,703,990 B2Granted
Process for slurry hydrocracking using catalyst with low diaspore alumina
AssigneeUop LLC
InventorsFred G. Sollberger, Phuong T. M. Do, Alakananda Bhattacharyya, Lance A. Baird
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Abstract
A process is disclosed for using an iron oxide and alumina catalyst with no more than more than about 55 wt % of the alumina in the diaspore phase or in the alpha phase in SHC. Alpha alumina is less effective catalyst component for slurry hydrocracking in terms of TIOR conversion. Drying procedures should avoid more than about 51 wt % of the alumina change to the alpha phase. The SHC catalyst is for converting heavy hydrocarbon feed into lighter hydrocarbon products.
Claims5
A process for converting heavy hydrocarbon feed into lighter hydrocarbon products comprising:
- providing catalyst particles comprising iron oxide and alumina;
- heat treating said catalyst particles at a temperature between about 150° C. and about 800° C. in air to provide dried catalyst particles comprising no more than about 51 wt % of the alumina in the alpha phase;
- mixing said heavy hydrocarbon feed with hydrogen and said catalyst particles to form a heavy hydrocarbon slurry comprising hydrocarbon liquid and said catalyst particles;
- hydrocracking hydrocarbons in said heavy hydrocarbon slurry in the presence of said hydrogen and said catalyst particles in a hydrocracking reactor to produce a hydrocracked slurry product comprising lighter hydrocarbon products;
- and
- withdrawing said hydrocracked slurry product from said hydrocracking reactor.
3 more elements
Dependencies are inferred from the claim text.