University of California, Berkeley 1968 - 1969
Stanford University 1964 - 1968
Bachelors, Bachelor of Science, Chemical Engineering
University of California
Broomfield High School
Bruce E. Reynolds - Martinez CA Fred W. Lam - Oakland CA Julie Chabot - Novato CA Fernando J. Antezana - Tiburon CA Robert Bachtel - El Cerrito CA Kirk R. Gibson - El Cerrito CA Richard Threlkel - El Cerrito CA Pak C. Leung - Lafayette CA
Assignee:
Chevron U.S.A. Inc. - San Francisco CA
International Classification:
C10G 6502
US Classification:
208211, 208210, 208212, 208251 H, 208254 H
Abstract:
A reactor system and process for hydrotreating a heavy feedstock contaminated with metals sulfur and carbon residue using an upflow fixed bed reactor with at least two catalyst layers having different hydrogenation activity.
Kirk R. Gibson - El Cerrito CA, US Richard Threlkel - El Cerrito CA, US Pak C. Leung - Lafayette CA, US
Assignee:
Chevron U.S.A. Inc. - San Ramon CA
International Classification:
B01J 23/00 B01J 27/00
US Classification:
502322, 502211, 502213, 502314, 502315, 502323
Abstract:
An improved catalyst for hydrodesulfurization of heavy feedstocks is disclosed. The catalyst is adopted for on-stream catalyst replacement in upflow processing units. It is characterized by a smaller peak pore diameter than general purpose hydrotreating catalysts.
Hydroconversion Catalyst And Method For Making The Catalyst
Lawrence Schulz - Clarendon Hills IL, US Kirk Gibson - El Cerrito CA, US Julie Chabot - Novato CA, US Bruno Nesci - Oak Lawn IL, US
International Classification:
C10G045/04
US Classification:
502/313000, 208/217000, 208/21600R, 208/213000
Abstract:
A high-activity hydrotreating catalyst, having a low density, suitable for deep removal of sulfur, nitrogen, micro-carbon residue and organometallic contaminants from hydrocarbon feedstocks is disclosed. Further disclosed is a method of preparation of this catalyst, which may contain 0.3-10 wt % of a Group IVB metal promoter, 5-25 wt % of a Group VIB metal component, and 1-8 wt % of a Group VIII metal, along with a method of hydrotreating employing this catalyst.
A process for hydrotreating hydrocarbon feedstocks using shaped catalysts is disclosed. When the catalyst is used for diffusion limited reactions, and particularly when it is used for demetalation, shaped catalysts give longer catalyst lifetimes. Preferred shaped include oval and elliptical shapes, with and without bumps.
Hydroconversion Catalyst And Method For Making The Catalyst
Charles R. Wilson - San Francisco CA Kirk R. Gibson - El Cerrito CA
Assignee:
Chevron Research and Technology Company - San Francisco CA
International Classification:
B01J 2106 B01J 2385 B01J 2388
US Classification:
502309
Abstract:
A method for making a hydrotreating catalyst wherein the catalyst is prepared by mixing a peptized hydrated supporting oxide with a hydrated Group IVB metal oxide gel promoter. The Group VIII metals are mixed in with the Group IVB metal oxide gel promoter. A solution containing a soluble Group VIB metal and a basic compound is added. The catalyst is used for hydrodenitrogenation and Ramsbottom Carbon Residue reduction of a hydrocarbon feedstock.
The method of making a catalyst comprising alumina with GP VI and VIII components wherein the method comprises peptizing an alumina powder with an aqueous acid solution of a group VIII metal salt, neutralizing the peptized alumina/group VIII metal with an aqueous solution of a nitrogen-containing base with a dissolved group VI metal salt therein, extruding, drying, and calcining the catalytic particles.
Hydroconversion Catalyst And Method For Making The Catalyst
Charles R. Wilson - San Francisco CA Kirk R. Gibson - El Cerrito CA Chi-Wen Hung - San Rafael CA
Assignee:
Chevron Research and Technology Company - San Francisco CA
International Classification:
B01J 2106 B01J 2385 B01J 2388 B01J 27185
US Classification:
502211
Abstract:
A method of making a hydrotreating catalyst wherein the catalyst is prepared by mixing a peptized alumina support containing soluble Group IVB and Group VIII metal compounds with a solution containing a soluble Group VIB metal compound and a basic compound. The catalyst is used for hydrodenitrogenation and Ramsbottom Carbon Residue reduction of a hydrocarbon feedstock.
Process For The Removal Of Thiols From Hydrocarbon Oils
Robert L. Jacobson - Hercules CA Kirk R. Gibson - El Cerrito CA
Assignee:
Chevron Research Company - San Francisco CA
International Classification:
C10G 2916 C10G 2906 C10G 2904
US Classification:
208243
Abstract:
Thiol impurities are absorbed and removed from hydrocarbon oils by contacting the oil in the absence of molecular oxygen with a scavenger at a temperature in the range of about 120. degree. to 400. degree. C. The scavenger is a composite having a copper component and an inorganic porous carrier component and having a surface area in the range 20 to 1000 square meters per gram. The contacting must be discontinued when the thiol impurity content of the effluent product exceeds about 0. 3 ppm.
Kirk Harold Gibson (born May 28, 1957) is a former Major League Baseball player and currently the manager of the Arizona Diamondbacks. As a player, Gibson ...