Teh Chung Ho - Bridgewater NJ Stuart Leon Soled - Pittstown NJ Sabato Miseo - Pittstown NJ Gary Brice McVicker - Califon NJ Michel Daage - Baton Rouge LA Viktor Buchholz - Branchburg NJ
Assignee:
Exxon Research and Engineering Company - Florham Park NJ
International Classification:
C07C 510
US Classification:
585266
Abstract:
The present invention is directed toward a catalyst composition prepared by a process comprising: (a) impregnating an oxide precursor selected from the group consisting of rare earth oxide precursors, yttria precursors and mixtures thereof, onto an inorganic refractory oxide support; (b) drying said support at a temperature of about 100. degree. to about 120. degree. C. followed by calcining said support at a temperature of about 400. degree. to about 600. degree. C. ; and (c) compositing or depositing on said support of step (b), a catalyst precursor salt represented by (ML)(Mo. sub. y W. sub. 1-y O. sub. 4). sub. a wherein M comprises Cr and/or one or more divalent promoter metals selected from the group consisting of Mn, Fe, Co, Ni, Cu, Zn and mixtures thereof, wherein y is any value ranging from 0 to 1, and wherein L is one or more neutral, nitrogen-containing ligands at least one of which is a chelating polydentate ligand; a=1 when chromium is not one of the promoter metals and 0. 5. ltoreq. a. ltoreq. 3 when Cr is one of the promoter metals. (d) sulfiding said deposited or composited support of step (c) with an excess amount of sulfur in the form of one or more sulfur bearing compounds and at a temperature of at least about 250. degree. C.
Dispersed Metal Sulfide Catalysts For Hydroprocessing
Teh Chung Ho - Bridgewater NJ Stuart Leon Soled - Pittstown NJ Sabato Miseo - Pittstown NJ Gary Brice Mc Vicker - Califon NJ Michel Daage - Baton Rouge LA Viktor Buchholz - Branchburg NJ
Assignee:
Exxon Research and Engineering Company - Florham Park NJ
International Classification:
B01J 27047 B01J 3100 B01J 27051 B01J 2363
US Classification:
502322
Abstract:
The present invention is directed toward a catalyst composition comprising a catalyst prepared by a process comprising: (a) impregnating an oxide precursor selected from the group consisting of rare earth oxide precursors, yttria precursors and mixtures thereof, onto an inorganic refractory oxide support; (b) drying said support at a temperature of about 100. degree. to about 120. degree. C. followed by calcining said support at a temperature of about 400. degree. to about 600. degree. C. ; and (c) compositing or depositing on said support of step (b), a catalyst precursor salt represented by (ML)(Mo. sub. y W. sub. 1-y O. sub. 4). sub. a wherein M comprises Cr and/or one or more divalent promoter metals selected from the group consisting of Mn, Fe, Co, Ni, Cu, Zn and mixtures thereof, wherein y is any value ranging from 0 to 1, and wherein L is one or more neutral, nitrogen-containing ligands at least one of which is a chelating polydentate ligand; a=1 when chromium is not one of the promoter metals and 0. 5. ltoreq. a. ltoreq. 3 when Cr is one of the promoter metals. (d) sulfiding said deposited or composited supports of step (c) with an excess amount of sulfur in the form of one or more sulfur bearing compounds and at a temperature of at least about 250. degree. C.
Dispersed Metal Sulfide Catalysts For Hydroprocessing
Teh Chung Ho - Bridgewater NJ Stuart Leon Soled - Pittstown NJ Sabato Miseo - Pittstown NJ Gary Brice McVicker - Califon NJ Michel Daage - Baton Rouge LA Viktor Buchholz - Branchburg NJ
Assignee:
Exxon Research and Engineering Company - Florham Park NJ
International Classification:
C07C 510
US Classification:
585270
Abstract:
The present invention is directed toward a catalyst composition comprising a catalyst prepared by a process comprising: (a) impregnating an oxide precursor selected from the group consisting of rare earth oxide precursors, yttria precursors and mixtures thereof, onto an inorganic refractory oxide support; (b) drying said support at a temperature of about 100. degree. to about 120. degree. C. followed by calcining said support at a temperature of about 400. degree. to about 600. degree. C. ; and (c) compositing or depositing on said support of step (b), a catalyst precursor salt represented by (ML)(Mo. sub. y W. sub. 1-y O. sub. 4). sub. a wherein M comprises Cr and/or one or more divalent promoter metals selected from the group consisting of Mn, Fe, Co, Ni, Cu, Zn and mixtures thereof, wherein y is any value ranging from 0 to 1, and wherein L is one or more neutral, nitrogen-containing ligands at least one of which is a chelating polydentate ligand; a=1 when chromium is not one of the promoter metals and 0. 5. ltoreq. a. ltoreq. 3 when Cr is one of the promoter metals. (d) sulfiding said deposited or composited supports of step (c) with an excess amount of sulfur in the form of one or more sulfur bearing compounds and at a temperature of at least about 250. degree. C.
Aromatics Hydrogenation With A New Class Of Metal Oxides
Teh Chung Ho - Bridgewater NJ Charles R. Symon - Rahway NJ Viktor Buchholz - Branchburg NJ Michel Daage - Baton Rouge LA
Assignee:
Exxon Research and Engineering Company - Florham Park NJ
International Classification:
B01J 27051 C10G 4702 C07C 510
US Classification:
502220
Abstract:
The present invention is directed toward a highly active aromatics hydrogenation catalyst and its use. The catalyst composition is prepared by: (a) decomposing a catalyst precursor selected from the group consisting of metal amine molybdates, metal amine tungstates and mixtures thereof, wherein said metal amine catalyst precursor has the general formula ML(Mo. sub. y W. sub. 1-y O. sub. 4)a where M is Cr and/or one or more divalent promoter metals selected from the group consisting of Mn, Fe, Co, Ni, Cu and Zn; L is one or more neutral nitrogen containing ligands at least one of which is a chelating polydentate ligand; 0. ltoreq. y. ltoreq. 1; and a=1 for non-chromium containing catalysts and wherein 0. 5. ltoreq. a. ltoreq. 3 for chromium containing catalysts, at a temperature of about 200. degree. to about 400. degree. C.
Process For Deep Desulfurization Using Combined Hydrotreating-Oxidation
Teh Chung Ho - Bridgewater NJ Chang Samuel Hsu - Bridgewater NJ Gerald Dennis Dupre - Baton Rouge LA Ronald Liotta - Kingswood TX Viktor Buchholz - Clinton NJ
Assignee:
Exxon Research and Engineering Co - Florham Park NJ
International Classification:
C10G 2900
US Classification:
208240
Abstract:
The instant invention is directed to a process for removing hard sulfurs from hydrocarbon streams by selectively oxidizing hard sulfurs in a hydrotreated stream, under oxidizing conditions in the presence of an effective amount of an oxidizing agent, wherein the oxidizing agent is a peroxometal complex and wherein the hard sulfurs are oxidized into the corresponding sulfoxides and sulfones.
Desulfurization Process For Removal Of Refractory Organosulfur Heterocycles From Petroleum Streams
Gary B. McVicker - Califon NJ Teh C. Ho - Bridgewater NJ Stuart Soled - Pittstown NJ Michel Daage - Baton Rouge LA Roman Krycak - Annandale NJ Sabato Miseo - Pittstown NJ Viktor Buchholz - Branchburg NJ William E. Lewis - Baton Rouge LA
Assignee:
Exxon Research and Engineering Co. - Florham Park NJ
International Classification:
C10G 4504
US Classification:
208215
Abstract:
Hydrocarbon feeds are upgraded by contact of the stream under hydrodesulfurization (HDS) conditions with a catalyst system comprising a sulfided, transition metal promoted tungsten/molybdenum HDS catalyst, e. g. , Ni/Co--Mo/Al. sub. 2 O. sub. 3 and a solid acid catalyst which is effective for the isomerization/disproportionation/transalkylation of alkyl substituted, condensed ring heterocyclic sulfur compounds present in the feedstream, e. g. zeolite or a heteropolyacid compound. Isomerization, disproportionation and transalkylation reactions convert refractory sulfur compounds such as 4- or 4,6-alkyl dibenzothiophenes into corresponding isomers or disproportionated isomers which can be more readily desulfurized by conventional HDS catalysts to H. sub. 2 S and other products.
Aromatics Hydrogenation With A New Class Of Metal Oxides
Teh Chung Ho - Bridgewater NJ Charles Ralph Symon - Rahway NJ Viktor Buchholz - Branchburg NJ Michel Daage - Baton Rouge LA
Assignee:
Exxon Research and Engineering Company - Florham Park NJ
International Classification:
C07C 510 B01J 3100
US Classification:
585269
Abstract:
The present invention is directed toward a hydrogenation process using a highly active aromatics hydrogenation catalyst. The catalyst is prepared by decomposing a catalyst precursor selected from the group consisting of metal amine molybdates, metal amine tungstates and mixtures thereof, wherein said metal amine catalyst precursor has the general formula ML (Mo. sub. y W. sub. 1-y O. sub. 4). sub. a where M is Cr and/or one or more divalent promoter metals selected from the group consisting of Mn, Fe, Co, Ni, Cu and Zn; L is one or more neutral nitrogen-containing ligands at least one of which is a chelating polydentate ligand; 0. ltoreq. y. ltoreq. 1; and a=1 for non-chromium containing catalysts and wherein 0. 5. ltoreq. a. ltoreq. 3 for chromium containing catalysts, at a temperature of about 200. degree. C. to about 400. degree. C.
Self-Assembled Propylene-Based Compositions And Methods Of Production Thereof
- Baytown TX, US John R. Hagadorn - Houston TX, US Viktor Buchholz - Clinton NJ, US Peijun Jiang - League City TX, US
International Classification:
C08K 7/08 B32B 27/06 C08F 110/06
Abstract:
Disclosed are self-assembled propylene-based bi-layer compositions having a skin layer comprising a propylene-based elastomer-toughened composition and a core layer comprising a propylene-based fiber-reinforced composition, wherein the propylene-based elastomer-toughened composition and propylene-based fiber-reinforced composition self-assemble upon mixing into the skin layer and the core layer. Processes for producing these self-assembled propylene-based compositions are also disclosed.