A hydrotreating catalyst comprises molybdenum, nickel, and phosphorus components supported on gamma alumina precalcined at a temperature of at least 1375. degree. F.
Hydroprocessing Catalyst, Its Use, And Method Of Preparation
Howard D. Simpson - Irvine CA Suheil F. Abdo - Placentia CA
Assignee:
Union Oil Company of California - Los Angeles CA
International Classification:
B01J 2104
US Classification:
502315
Abstract:
A catalyst containing an overlayer of a catalytic promoter on a porous refractory support containing an underbedded Group VIII metal-containing component. The catalyst is prepared by sequential incorporation of the Group VIII metal followed by the additional catalytic promoter component, usually a Group VIB metal, with the porous refractory oxide support. The catalyst has a MoO. sub. 3 /NiO weight ratio less than 6 to 1 and more than 4 weight percent of NiO. The catalyst is especially useful for simultaneous hydrodenitrogenation and hydrodesulfurization of a gas oil, particularly when the refractory oxide support has a narrow pore size distribution.
Highly active cobalt-molybdenum-alumina desulfurization catalysts containing 18-30 weight-percent of MoO. sub. 3 are prepared by first comulling boehmite alumina with aqueous ammonium molybdate solution, drying the resulting mixture, then comulling with a soluble cobalt salt and water, thereafter forming the resulting mixture into extrudates, and finally calcining the extrudates under controlled temperature conditions correlated with the molybdenum content of the catalyst so as to preserve adequate surface area and prevent the formation of large crystallites of cobalt molybdate. This method of preparation permits effective utilization of molybdenum in amounts up to about 30 weight-percent MoO. sub. 3, a result not obtainable by conventional impregnation techniques.
Howard D. Simpson - Irvine CA Suheil F. Abdo - Placentia CA
Assignee:
UOP - Des Plaines IL
International Classification:
C10G 4904
US Classification:
208 46
Abstract:
A catalyst containing an overlayer of a catalytic promoter on a porous refractory support containing an underbedded Group VIII metal-containing component. The catalyst is prepared by sequential incorporation of the Group VIII metal followed by the additional catalytic promoter component, usually a Group VIB metal, with the porous refractory oxide support. The catalyst has a MoO. sub. 3 /NiO weight ratio less than 6 to 1 and more than 4 weight percent of NiO. The catalyst is especially useful for simultaneous hydrodenitrogenation and hydrodesulfurization of a gas oil, particularly when the refractory oxide support has a narrow pore size distribution.
Hydrotreating Catalyst And Process For Its Preparation
A hydrotreating catalyst comprises molybdenum, nickel, and phosphorus components supported on gamma alumina precalcined at a temperature of at least 1375. degree. F.
Pauline B. Ting - Brea CA Howard D. Simpson - Irvine CA
Assignee:
Union Oil Company of California - Los Angeles CA
International Classification:
C07C 3700
US Classification:
208 3
Abstract:
A hydrocarbon conversion catalyst containing a Group VIB metal on a porous refractory oxide is prepared by impregnating support particles with a solution containing Group VIB metal components and citric acid, followed by drying and calcining. The catalyst is useful for promoting a number of hydrocarbon conversion reactions, particularly those involving hydrogenative desulfurization, demetallization and denitrogenation.
Pauline B. Ting - Brea CA Howard D. Simpson - Irvine CA
Assignee:
Union Oil Company of California - Los Angeles CA
International Classification:
C10G 3504
US Classification:
208134
Abstract:
A hydrocarbon conversion catalyst containing a Group VIB metal on a porous refractory oxide is prepared by impregnating support particles with a solution containing Group VIB metal components and citric acid, followed by drying and calcining. The catalyst is useful for promoting a number of hydrocarbon conversion reactions, particularly those involving hydrogenative desulfurization, demetallization and denitrogenation.
Novel, high surface area cobalt-molybdenum-alumina desulfurization catalysts containing 20-30 weight-percent of MoO. sub. 3, and being free of X-ray-detectable cobalt molybdate crystallites, are disclosed. A preferred method of preparation thereof involves first comulling boehmite alumina with aqueous ammonium molybdate solution, drying the resulting mixture, then comulling with a soluble cobalt salt and water, thereafter forming the resulting mixture into extrudates, and finally calcining the extrudates under controlled temperature conditions correlated with the molybdenum content of the catalyst so as to preserve adequate surface area and prevent the formation of large crystallites of cobalt molybdate.
Name / Title
Company / Classification
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Howard Simpson
OHIO WILDLIFE STATION INC
Howard Simpson President
THE RIB RANCH, INC
799 W Broadway St, Lake Elsinore, CA 92530
Howard N. Simpson Managing
Simpson Enterprises, LLC Software Publishing
2117 Main St, Huntington Beach, CA 92648
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Howard Simpson
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Pearson Education - Digital Development Manager (2011)
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Live in Oxford, UK and enjoy all things related to technology, education, gadgets and innovation.Currently working as a Digital Development Manager at Pearson Education managing the development of sev...
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Driven, dynamic individual with an extensive knowledge of systems engineering, software development and technical architecture.
Howard Simpson
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Integrated Security & Communications (2010)
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Northeastern University
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Hello All! Howard Simpson Here. I am a simple and open minded person. I like to share knowledge and making new friends. I like Cricket, Tennis, Video Games.
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Husband, father of 2, MUFC follower and Editor of STV News
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HI! I am Howard Simpson Always interested in new technologies and tools. Working on free PDF Converter presently.
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