Abstract: A catalytic hydrocracking process which comprises (a) introducing a reduced crude into a fractionation zone to produce a vacuum gas oil stream having a propensity to form polynuclear aromatic compounds in a hydrocracking zone and a slop wax stream; (b) contacting the vacuum gas oil stream in a hydrocracking zone with added hydrogen and a metal promoted hydrocracking catalyst at elevated temperature and pressure sufficient to gain a substantial conversion to lower boiling products; (c) partially condensing the hydrocarbon effluent from the hydrocracking zone and separating the same into a low boiling hydrocarbon product stream and an unconverted hydrocarbon stream boiling above about 650.degree. F. (343.degree. C.

Abstract: A process is disclosed for the fluid catalytic cracking of a hydrocarbon oil which comprises contacting said oil at fluid catalytic cracking conditions with a catalyst consisting of silica, a rare earth metal component and a dealuminated zeolitic aluminosilicate having a SiO.sub.2 /Al.sub.2 O.sub.3 molar ratio of from 4.5 to 35, the essential X-ray powder diffraction pattern of zeolite Y, an ion exchange capacity of not greater than 0.070, a unit cell dimension a.sub.o of from 24.20 to 24.45 A, a surface area of at least 350 m.sup.2 /g (B-E-T), a sorptive capacity for water vapor at 25.degree. C. and a p/p.sub.o value of 0.10 of less than 4.00 weight percent and a Residual Butanol Test value of not more than 0.40 weight percent.

Abstract: A catalytic composite comprising a metal chelate mercaptan oxidation catalyst and a solid carrier material having an average particle size of less than about 110 mesh.

Abstract: A process for the removal of trace quantities of hydrocarbonaceous compounds from an aqueous stream which comprises the steps of: (a) contacting a solvent, which in the supercritical state is effective to dissolve the hydrocarbonaceous compounds from the aqueous stream, with the aqueous stream, for a time sufficient at supercritical solvent conditions to dissolve at least a portion of the hydrocarbonaceous compounds and to produce an aqueous stream having a reduced hydrocarbonaceous compound concentration; (b) separating the hydrocarbonaceous compounds from the solvent at subcritical conditions; and (c) recovering the hydrocarbonaceous compounds.

Abstract: A process for sweetening a sour hydrocarbon fraction containing mercaptan which comprises reacting mercaptans contained in the hydrocarbon fraction with an oxidizing agent by passing said hydrocarbon fraction and said oxidizing agent into contact with a heterogeneous admixture of a metal chelate mercaptan oxidation catalyst and a solid desiccant.

Abstract: A process for sweetening a sour hydrocarbon fraction containing mercaptan which comprises reacting mercaptans contained in the hydrocarbon fraction with an oxidizing agent by passing the hydrocarbon fraction and the oxidizing agent into contact with a bed of metal chelate mercaptan oxidation catalyst and a solid carrier material having an average particle size of less than about 110 mesh.

Abstract: A process for the conversion of a hydrocarbon charge stock which comprises contacting said charge stock at hydrocarbon conversion conditions with a catalytic composite comprising a combination of a carrier material, a Group VIB metal component and Group VIII metal component wherein said Group VIB metal component and said Group VIII metal component are incorporated in said catalytic composite by means of a non-aqueous organic solution of a Group VIB metal compound and a Group VIII metal compound, wherein said non-aqueous organic solution comprises dimethylformamide, formamide, diethylformamide, ethylformamide, methylformamide, pyridine, aniline or toluene and wherein said catalytic composite is calcined in a non-oxidizing atmosphere.

Abstract: A process for the conversion of a hydrocarbon charge stock is disclosed which process comprises reacting the charge stock with hydrogen at hydrocracking conditions in contact with a catalytic composite having improved selectivity to middle distillate product during hydrocracking which comprises alumina, a crystalline aluminosilicate, a Group VIB metal component and a Group VIII metal component and which catalytic composite is prepared by the method comprising admixing the alumina and crystalline aluminosilicate with a peptizing agent and an aqueous solution of a modified linear aliphatic polyether surfactant to form a dough; extruding the dough into discrete particles; and calcining and drying the particles.

Abstract: A process is disclosed for oxidizing difficultly oxidizable mercaptans contained in a hydrocarbon fraction which comprises adding a hydrocarbon soluble alkali metal compound, capable of forming the alkali metal mercaptides of the difficultly oxidized mercaptans, to the hydrocarbon fraction; and contacting the resulting hydrocarbon fraction containing the hydrocarbon soluble alkali metal compound with a metal chelate catalyst disposed on an adsorptive support in the presence of a hydrated oxygen-containing gas and in the absence of a separate water phase.

Abstract: A process for deashing primary coal liquids with a selective hydrocarbon solvent separation wherein the coal liquids and selective hydrocarbon solvent are contacted initially at a temperature greater than the temperature at which the deashing separation occurs. More particularly, a process for the production of deashed coal liquid which comprises the sequential steps of: (a) admixing a primary coal liquid containing ash and a hydrocarbon deashing solvent having no hydrogen-transferring ability at a selected admixing temperature from about 250.degree. F. to about 575.degree. F.; (b) reducing the temperature of the entire resulting admixture of the primary coal liquid and hydrocarbon deashing solvent to a deashing temperature about 50.degree. F. to about 125.degree. F. less than the admixing temperature of step (a); and deashing the primary coal liquid with the deashing solvent at the deashing temperature of step (b).

Abstract: A hydrocarbon conversion catalyst is disclosed which catalyst comprises a refractory inorganic oxide, a Group VIB metal component, a Group VIII metal component and a fluoride component wherein the last step in the catalyst preparation is the incorporation of the fluorine component and a subsequent calcination in contact with a flowing gas. Other embodiments of the present invention describe the use of the catalyst for hydrocarbon conversion and preferred methods of catalyst manufacture.

Abstract: A process for the recovery of hydrocarbonaceous oil from oil shale is disclosed. The process comprises: (a) heating the shale in the presence of a gas comprising hydrogen sulfide at subcritical conditions of said gas including a temperature from about 650.degree. F. to about 825.degree. F. to produce a solvent extractable material and to liberate at least a first portion of the hydrocarbon contained therein; and (b) contacting the resulting solvent extractable material with a normally-liquid solvent at subcritical, reflux conditions of said solvent to liberate at least a second portion of the hydrocarbon contained in the solvent extractable material.

Abstract: A method for the in situ conversion and recovery of heavy hydrocarbonaceous crude oil containing indigenous trace metal from two adjacent non-communicating hydrocarbon reservoirs which are alternately pressured and recovered which method comprises: (a) heating the heavy hydrocarbonaceous crude oil in a first reservoir to a hydrocarbon conversion temperature; (b) contacting the first reservoir with elemental essentially-anhydrous hydrogen at a pressure from about 200 to about 10,000 psig; (c) heating the heavy hydrocarbonaceous crude oil in a second reservoir to a hydrocarbon conversion temperature; (d) depressuring the first reservoir to yield an effluent comprising hydrocarbonaceous crude oil and unreacted elemental hydrogen; (e) separating the effluent from the first reservoir to recover a hydrocarbonaceous crude oil and a gaseous component comprising elemental hydrogen; (f) contacting the second reservoir with elemental essentially-anhydrous hydrogen, a portion of which is recovered in step (e), at a press

Abstract: A hydrocarbon conversion catalyst is disclosed which comprises a combination of a carrier material, a Group VIB metal component and Group VIII metal component wherein said group VIB metal component and said Group VIII metal component are incorporated in said catalytic composite by means of a non-aqueous organic solution of a Group VIB metal compound and a Group VIII metal compound, wherein said non-aqueous organic solution comprises dimethylformamide, formamide, diethylformamide, ethylformamide, methylformamide, pyridine, aniline or toluene and wherein said catalytic composite is calcined in a non-oxidizing atmosphere. Other embodiments of the present invention describe the use of the catalyst for hydrocarbon conversion and preferred methods of catalyst manufacture.

Abstract: A method is disclosed for hydrocracking a hydrocarbon feedstock having a propensity to form polynuclear aromatic compounds without excessively fouling the processing unit. The hydrocracking method includes contacting the hydrocarbon feedstock with a crystalline zeolite hydrocracking catalyst, contacting at least a portion of the resulting unconverted hydrocarbon oil containing polynuclear aromatic compounds with an adsorbent which selectively retains polynuclear aromatic compounds and recycling unconverted hydrocarbon oil having a reduced concentration of polynuclear aromatic compounds to the hydrocracking zone.

Abstract: A process for the in situ conversion of heavy hydrocarbonaceous crude oil containing indigenous trace metal which comprises heating said heavy hydrocarbonaceous oil in situ to a hydrocarbon conversion temperature, contacting the hot hydrocarbonaceous oil with hydrogen at a pressure from about 200 to about 5000 psig, and recovering the resulting converted hydrocarbonaceous oil.

Abstract: A process for the direct catalytic conversion of hydrocarbon oil is disclosed wherein the hydrocarbon feedstock, hydrogen and hot solid catalyst particles are contacted at a temperature from about 600.degree. F. to about 995.degree. F. to form a suspension in a riser reactor thereby producing lower boiling hydrocarbon components.

Abstract: A process for the recovery of hydrocarbonaceous oil from oil shale is disclosed. The process comprises: (a) heating the shale in the presence of a non-combustion supporting, non oil-miscible gas at subcritical conditions of said gas and at a temperature from about 650.degree. F. to about 825.degree. F. to produce a solvent extractable material and to liberate at least a first portion of the hydrocarbon contained therein; and (b) contacting the resulting solvent extractable material with a normally-liquid solvent at subcritical, reflux conditions of said solvent to liberate at least a second portion of the hydrocarbon contained in said solvent extractable material.

Abstract: A process for producing hydrogen-enriched hydrocarbonaceous products from coal which comprises: (a) contacting the coal in a solvent extraction zone at solvent extraction conditions with a coal solvent, hydrogen and a first residual oil containing asphaltenes and at least one finely divided, unsupported metal sulfide to provide a liquid effluent slurry which includes a low boiling hydrocarbon soluble fraction; (b) contacting at least a portion of the liquid effluent slurry from the solvent extraction zone of step (a) with a low boiling hydrocarbon solvent in a solvent separation zone at solvent separation conditions to separate the low boiling hydrocarbon soluble fraction from a low boiling hydrocarbon insoluble fraction which comprises ash, unconverted asphaltenes and finely divided, unsupported metal sulfide; (c) contacting the low boiling hydrocarbon soluble fraction from step (b) with hydrogen and a second residual oil containing asphaltenes and at least one finely divided, unsupported metal sulfide in a

Abstract: A catalytic composite is disclosed which catalyst comprises a silica-alumina carrier material, a nickel component and a vanadium component, and which catalyst is useful for the conversion of hydrocarbons. A preferred method of preparation comprises the incorporation of the vanadium component from an alcoholic solution of a vanadium compound.