Abstract: The catalytic hydrocracking, hydrodesulfurization, and/or hydrodenitrogenation of organic compounds is carried out in the presence of a catalyst composition comprising zeolite, zinc, titanium, and at least one promoter selected from the group consisting of vanadium, chromium, cobalt, nickel, molybdenum, tungsten, rhenium, platinum, palladium, rhodium, ruthenium and compounds thereof.

Abstract: The catalytic hydrodesulfurization of organic compounds containing sulfur is carried out in the presence of a catalyst composition comprising zinc titanate and at least one promoter selected from the group consisting of vanadium, chromium, cobalt, nickel, molybdenum, tungsten, rhenium, platinum, palladium, rhodium, ruthenium, and compounds thereof.

Abstract: A hydrotreating catalyst comprising nickel, molybdenum, and phosphorus active components supported on gamma alumina is prepared with gamma alumina support particles partially hydrated with water vapor while the support particles are in motion relative to each other, as by passage of steam through an ebulliating bed of particulate gamma alumina.

Abstract: In processes for the catalytic treatment of hydrocarbon feedstream containing organic sulfur comprising contacting said feedstream with a catalyst for a time at a temperature and pressure sufficient to effect the desired catalytic change on the feedstream, the improvement comprising using as the catalyst a layered composition of the formula MX.sub.y wherein M is a transition metal selected from the group consisting of Group IVb, Vb, VIb, VIIb and uranium, X is a chalcogen selected from the group consisting of sulfur, selenium, tellurium, and mixtures thereof, y is a number ranging from about 1.5 to about 3. The catalyst is prepared by reacting neat or in the presence of a nonaqueous solvent a Group IVb to VIIb or uranium metal salt, and a source of sulfide, selenide or telluride ions, and mixing the reactants at temperatures below 400.degree. C. and at atmospheric pressures.

Abstract: The catalytic hydrodesulfurization and/or hydrodenitrogenation of organic compounds containing sulfur and/or nitrogen is carried out in the presence of a catalyst composition comprising zinc, titanium and at least one promoter selected from the group consisting of vanadium, chromium, cobalt, nickel, molybdenum, tungsten, rhenium, platinum, palladium, rhodium, ruthenium, and compounds thereof.

Abstract: The catalytic hydrocracking, hydrodesulfurization, and/or hydrodenitrogenation of organic compounds is carried out in the presence of a catalyst composition comprising zeolite, zinc, titanium, and at least one promoter selected from the group consisting of vanadium, chromium, cobalt, nickel, molybdenum, tungsten, rhenium, platinum, palladium, rhodium, ruthenium and compounds thereof.

Abstract: Hydrogen sulfide is removed from a fluid stream by contacting the fluid stream which contains hydrogen sulfide with an absorbing composition comprising zinc, titanium and at least one promoter selected from the group consisting of vanadium, chromium, manganese, iron, cobalt, nickel, molybdenum, rhenium, and compounds thereof. If organic sulfur compounds are present in the fluid stream, the absorbing composition acts as a hydrodesulfurization catalyst to convert the sulfur in the organic sulfur compounds to hydrogen sulfide which is subsequently removed from the fluid stream by the absorbing composition. If olefin contaminants are present in the fluid stream, the absorbing composition acts as hydrogenation catalyst to hydrogenate the olefin contaminants to paraffins.

Abstract: Cyclic hydrotreating of resids with low pressure, short term on-stream periods yields desirable products.

Abstract: The catalytic hydrodesulfurization and/or hydrodenitrogenation of an organic sulfur compound and/or an organic nitrogen compound is carried out in the presence of a catalyst composition comprising catalytic grade alumina, titanium, cobalt, zinc and molybdenum.

Abstract: A method of hydrorefining an asphaltenic charge stock is described which comprises effecting said reaction utilizing a titanium sulfide catalyst in a hydrogen sulfide-containing H.sub.2 atmosphere. The catalyst may be employed in slurry form or composited with a high surface area coke support. Preferably chloride is also present in the catalyst. The hydrogen sulfide suitably is present in the gas phase in an amount of from about 10 to about 25 mol. percent based on the moles of H.sub.2 present.

Abstract: A non-stoichiometric vanadium sulfide catalyst utilized in a process for hydrorefining a hydrocarbon feed stock is prepared by (1) contacting vanadium oxide with ammonium sulfide to form an ammonium salt of vanadium sulfide and (2) the salt is neutralized with an acid in a non-oxidative atmosphere to form the vanadium sulfide catalyst. The acid used in the neutralizing step may be sulfuric acid or carbonic acid and the non-oxidative atmosphere may be hydrogen or nitrogen.

Abstract: A non-stoichiometric vanadium sulfide catalyst utilized in a hydrocarbon hydrorefining process is prepared by contacting a sulfur-bearing gas, such as H.sub.2 S, into an alkali metal hydroxide solution containing vanadium oxide to form a soluble alkali metal vanadium sulfide. The vanadium sulfide is precipitated from the soluble alkali metal vanadium sulfide with an acid, such as sulfuric acid or carbonic acid.

Abstract: A novel method of preparing a non-stochiometric vanadium sulfide catalyst utilized in the processing of hydrocarbon feedstocks containing asphaltenes and organometallic compounds.

Abstract: The present invention relates to an improved method of catalyst presulfiding, wherein the catalyst is treated with elemental sulfur. The use of elemental sulfur as a catalyst presulfiding agent is a means of rapidly and reproducibly attaining a highly active catalyst.

Abstract: In the catalytic hydrogenation of a substance in a water-immiscible organic liquid medium, a metallic hydrogenation catalyst is conveniently and effectively dispersed in the reaction mixture by addition as an emulsion of an aqueous solution of a salt of the metal in the liquid medium. The method is particularly applicable to the liquefaction of coal.

Abstract: Carbonaceous liquids boiling above about 300.degree. C such as tars, petroleum residuals, shale oils and coal-derived liquids are catalytically hydrotreated by introducing the carbonaceous liquid into a reaction zone at a temperature in the range of 300.degree. to 450.degree. C and a pressure in the range of 300 to 4000 psig for effecting contact between the carbonaceous liquid and a catalytic transition metal sulfide in the reaction zone as a layer on a hydrogen permeable transition metal substrate and then introducing hydrogen into the reaction zone by diffusing the hydrogen through the substrate to effect the hydrogenation of the carbonaceous liquid in the presence of the catalytic sulfide layer.

Abstract: Low concentrations of Group VIB metal salts of fatty acids will catalyze the hydroconversion of sulfur-containing heavy petroleum oils producing a lighter oil fraction having a lower sulfur concentration than the heavy oil and a tar fraction containing a higher sulfur concentration than the heavy oil. Catalyst concentrations of 300 to 1,000 ppm, calculated as the elemental metal, are used. Molybdenum octoate is a preferred catalyst. This is a continuation, of application Ser. No. 400,866, filed Sept. 26, 1973, and now abandoned.

Abstract: A synthetic halloysite which is substantially iron-free is obtained by crystallization from a reaction mixture containing hydrous alumina gel and aqueous silica sol. Metal substituted synthetic halloysites can be prepared by coprecipitation of metal hydroxides with the alumina gel. Hydrocarbons are converted over cracking catalysts derived from these halloysites.

Abstract: A desulfurization catalyst is activated by being heated to a temperature between about 750.degree. and 850.degree. F. in the presence of the charge stock to be desulfurized during the initial stages of the on-stream period. In a preferred embodiment the catalyst, prior to the heat treatment, is sulfided at a low temperature and low pressure. The resulting catalyst effectively desulfurizes a petroleum hydrocarbon charge stock with reduced hydrogen consumption.

Abstract: A heavy hydrocarbonaceous oil is converted to lower boiling hydrocarbon products by treatment with hydrogen in the presence of a catalyst comprising a metal phthalocyanine and a particulate iron component.

Abstract: A catalytic hydroconversion process is effected by reacting with hydrogen a heavy hydrocarbonaceous oil containing a catalyst comprising an iron component and a catalytically active other metal component prepared by dissolving an oil soluble metal compound in the oil and converting the metal compound in the oil to the corresponding catalytically active metal component. Preferred oil soluble compounds are molybdenum compounds.

Abstract: The disclosure provides a novel catalyst support, a method of making said support by treatment of prior art crystalline catalyst supports with hydroxy-aluminum solution and hydrocarbon conversion processes wherein the catalyst used therein includes said support.

Abstract: A novel process for the demetallization of petroleum feedstocks comprising contacting a petroleum feedstock at elevated pressures and temperatures, and preferably in the presence of hydrogen, with a catalyst comprising a manganese component composited with alumina, said catalyst having a surface area in excess of 175 m.sup.2 /gm and having at least 60% of its pore volume in pores having diameters between 50 and 200 A. Preferred catalysts comprise between about 2 and 15 weight-percent manganese. Removal of more than 25%, usually more than 50%, of the organometallic impurities can be achieved.

Abstract: The conversion of hydrocarbons in the presence of hydrogen occurs under hydrocarbon conversion conditions in the presence of a subgroup of a certain class of metal-substituted semi-crystalline aluminosilicates which are synthetic and which are predominantly ordered in two directions, that is, which are laminar or have a layered or stacked sheet structure. The metal substituted for the aluminum in the trioctahedral sites is nickel, cobalt, or mixtures thereof. The catalysts are preferably used in hydroisomerization and hydrocracking processes.

Abstract: A hydrogenation process utilizing a hydrogenation catalyst in an oxidized state which catalyst is activated by a method which yields a superior performing hydrogenation catalyst. The hydrogenation catalyst is reduced, sulfided and stripped by a procedure which allows a more economical and time-saving start-up procedure.

Abstract: A hydrogenation catalyst in an oxidized state is activated by a method which yields a superior performing hydrogenation catalyst. The hydrogenation catalyst is reduced, sulfided and stripped by a procedure which allows a more economical and time-saving start-up procedure.