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U.S. Department of Energy
Office of Scientific and Technical Information

Hydrocracking process utilizing a catalyst having a reduced zeolite content

Patent ·
OSTI ID:5426244
This patent describes a process for refining hydrocarbon feedback containing organonitrogen components, organosulfur components or a mixture thereof. The process comprises: contacting the feedback with molecular hydrogen under hydrotreating conditions in the presence of a hydrotreating catalyst comprising a Group VIB metal component and a Group VIII metal component such that a subtantial proportion of the organonitrogen components, organosulfur components or mixture thereof is converted to ammonia, hydrogen sulfide or a mixture thereof; contacting substantially all of the effluent from the first step with molecular hydrogen in a first hydrocracking zone in the presence of a first hydrocracking catalyst comprising a zeolite and a hydrogeneration component to produce a hydrocracking product of substantially lower boiling point; separating the hydrocracking product into a higher boiling fraction and a lower boiling fraction; contacting the higher boiling fraction with molecular hydrogen in a second hydrocracking zone under hydrocracking conditions in an atmosphere which contains no more than about 200 ppmv ammonia and in the presence of a second hydrocracking catalyst to convert the higher boiling fraction into lower boiling products. The second hydrocracking catalysts comprises; a porous, inorganic refractory oxide component; and between about 40 weight percent and about 70 weight percent of a crystalline aluminosilicate Y zeolite having a silica-to-alumina mole ratio above about 6.0 intimately mixed with the refractory oxide component. The crystalline aluminosilicate Y zeolite having been ion-exchanged with Group VIII noble metal cations.
Assignee:
Union Oil Co. of California, Los Angeles, CA
Patent Number(s):
US 4857169
Application Number:
PPN: US 7119168A
OSTI ID:
5426244
Country of Publication:
United States
Language:
English