James L. Carter - Westfield NJ Allan E. Barnett - Westfield NJ John H. Sinfelt - Berkeley Heights NJ
Assignee:
Exxon Research & Engineering Co. - Florham Park NJ
International Classification:
B01J 2010 B01J 2370 B01J 2100
US Classification:
252452
Abstract:
Supported coprecipitated nickel-cobalt-silica and nickel-cobalt-copper-silica hydrogenation catalysts are disclosed. The catalysts are prepared by preparing an aqueous reaction mixture containing nickel and cobalt cations (and optionally copper cations), silicate anions and solid porous carrier particles under agitation to form a coprecipitate of the nickel, cobalt (and optionally copper) and silicate ions onto said solid porous support particles; heating the aqueous reaction mixture; and adding an alkaline precipitating agent to further precipitate the nickel, cobalt (and optionally copper) and silicate anions onto said solid porous carrier particles.
Process For Hydrogenating Organic Compounds By Use Of Group Viii Aluminum-Silicate Catalysts
Allan E. Barnett - Westfield NJ Albert P. Halluin - Westfield NJ
Assignee:
Exxon Research and Engineering Co. - Florham Park NJ
International Classification:
C07C 8511 C07C 8512
US Classification:
564415
Abstract:
Supported catalysts comprised of one or more metals of Group VIII, optionally one or more metals from Group IB and IIA, aluminum and silicate are used for hydrogenating hydrogenatable organic compounds. The catalysts can be produced by coprecipitating metal ions from Group VIII, optionally metal ions from Groups IB and IIA, aluminum ions, and silicate ions, in the presence of solid porous particles.
Coprecipitated Copper-Nickel-Silica Catalysts, Preparation And Use Thereof
James L. Carter - Westfield NJ Allan E. Barnett - Westfield NJ
Assignee:
Exxon Research & Engineering Co. - Florham Park NJ
International Classification:
B01J 2108 B01J 2370
US Classification:
252452
Abstract:
A copper promoted massive nickel catalyst is disclosed which is capable of having a reduced nickel surface area ranging from about 55 to about 100 m. sup. 2 /g as determined by hydrogen chemisorption, after reduction at 400. degree. C. , and a B. E. T. total surface area ranging from about 150 to about 300 m. sup. 2 /g, wherein the amount of copper in the catalyst ranges from about 2 wt. % to about 10 wt. and the amount of nickel ranges from about 25 wt. % to about 50 wt. %, said wt. % of copper and nickle metal are based on the total weight of the catalyst. The copper promoted massive catalysts are prepared by the steps comprising comingling a solution containing copper and nickel cations with another solution containing silicate anions and coprecipitating the copper, nickel and silicate ions in an aqueous solution onto solid carrier particles. The catalysts are useful in hydrogenation processes.
Hydrogenation Process Using Supported Nickel-Cobalt-Silica Coprecipitated Catalyst
James L. Carter - Westfield NJ Allan E. Barnett - Westfield NJ John H. Sinfelt - Berkeley Heights NJ
Assignee:
Exxon Research & Engineering Co. - Florham Park NJ
International Classification:
C07C 1504 C07C 510
US Classification:
564422
Abstract:
Supported coprecipitated nickel-cobalt-silica and nickel-cobalt-copper-silica hydrogenation catalysts are disclosed. The catalysts are prepared by preparing an aqueous reaction mixture containing nickel and cobalt cations (and optionally copper cations), silicate anions and solid porous carrier particles under agitation to form a coprecipitate of the nickel, cobalt (and optionally copper) and silicate ions onto said solid porous support particles; heating the aqueous reaction mixture; and adding an alkaline precipitating agent to further precipitate the nickel, cobalt (and optionally copper) and silicate anions onto said solid porous carrier particles.
Method For Preparing Reduced Metal Catalyst Having Metal Surface Area
James L. Carter - Westfield NJ Allan E. Barnett - Westfield NJ
Assignee:
Exxon Research & Engineering Co. - Linden NJ
International Classification:
B01J 2900 B01J 2910
US Classification:
252454
Abstract:
This invention pertains to a method of stabilizing, with respect to atmospheric air, a bed containing pyrophoric reduced metal catalyst with high active metal surface area formed by reduction of a compound of said metal at an elevated temperature ranging from 200. degree. to 500. degree. C. which comprises: (a) continuously circulating through said bed a stream of inert gas while maintaining a catalyst temperature of at least 300. degree. F. (149. degree. C. ); (b) cooling the catalyst throughout the bed with said inert gas until the catalyst in said bed attains a temperature ranging from 50. degree. F. (10. degree. C. ) to 100. degree. F. (38. degree. C. ); (c) decreasing the inert gas flow and progressively adding CO. sub. 2 until the CO. sub. 2 concentration in the gas stream is at least 80%; (d) adding O. sub.
Process For Hydrogenating Organic Compounds With A Supported Cobalt-Silica Coprecipitated Hydrogenation Catalyst
James L. Carter - Westfield NJ Allan E. Barnett - Westfield NJ
Assignee:
Exxon Research and Engineering Co. - Florham Park NJ
International Classification:
C07C 510
US Classification:
585269
Abstract:
Supported coprecipitated cobalt-silica hydrogenation catalysts are disclosed. The catalysts are prepared by: preparing an aqueous reaction mixture containing cobalt cations, silicate anions and solid porous carrier particles under agitation to form a coprecipitate of the cobalt and silicate ions onto said solid porous support particles; heating the aqueous reaction mixture; and adding an alkaline precipitating agent to further precipitate the cobalt and silicate ions onto said solid porous carrier particles. The aqueous reaction mixture may additionally include copper cations.
Process For Hydrogenating Organic Compounds With Coprecipitated Copper-Nickel-Silica Catalysts
James L. Carter - Westfield NJ Allan E. Barnett - Westfield NJ
Assignee:
Exxon Research & Engineering Co. - Florham Park NJ
International Classification:
C07C 510 C07C 502
US Classification:
568814
Abstract:
A copper promoted massive nickel catalyst is disclosed which is capable of having a reduced nickel surface area ranging from about 55 to about 100 m. sup. 2 /g as determined by hydrogen chemisorption, after reduction at 400. degree. C. , and a B. E. T. total surface area ranging from about 150 to about 300 m. sup. 2 /g, wherein the amount of copper in the catalyst ranges from about 2 wt. % to about 10 wt. % and the amount of nickel ranges from about 25 wt. % to about 50 wt. %, said wt. % of copper and nickel metal are based on the total weight of the catalyst. The copper promoted massive catalysts are prepared by the steps comprising comingling a solution containing copper and nickel cations with another solution containing silicate anions and coprecipitating the copper, nickel and silicate ions in an aqueous solution onto solid carrier particles. The catalysts are useful in hydrogenation processes.
Process For Hydrogenating Organic Compounds By Use Of Non-Ferrous Group Viii Aluminum Coprecipitated Catalysts
Allan E. Barnett - Westfield NJ Albert P. Halluin - Westfield NJ
Assignee:
Exxon Research & Engineering Co. - Florham Park NJ
International Classification:
C07C 8512 C07C 510 C07C 2914 C11C 312
US Classification:
564358
Abstract:
Supported coprecipitated non-ferrous Group VIII metal aluminum catalysts are used for hydrogenating hydrogenatable organic compounds. The catalysts are produced by preparing an aqueous mixture containing the metal ions, aluminum ions and solid porous support particles under agitation to form a coprecipitate of the metal ions and aluminum ions with the solid porous support particles; heating the aqueous reaction mixture; and adding precipitating agent to further precipitate the metal ions and aluminum ions onto the solid support.
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