Abstract: High surface area aluminum phosphate-alumina compositions are prepared by reaction of a mixture comprising an aluminum alkoxide and an organic phosphate such as trialkyl or triaryl phosphate, in the presence of moist air to form a precipitate, separating the precipitate from the mixture, drying and calcining the precipitate and recovering a high surface area aluminum phosphate-alumina product which can be used as catalyst support or catalyst component, especially for hydrocarbon treating and conversion processes.
Abstract: A high pressure fluid hydrocoking process is provided in which certain metal compounds which act as coke forming inhibitors are dispersed in the coker chargestock. Preferred compounds are molybdenum compounds, for example, molybdenum naphthenate. The hydrogen-containing fluidizing gas may also comprise hydrogen sulfide.
Abstract: A catalytic hydroconversion process for a hydrocarbonaceous oil is effected by dissolving an oil-soluble metal compound in the oil, converting the compound to a solid, non-colloidal catalyst within the oil and reacting the oil containing the catalyst with hydrogen. Preferred compounds are molybdenum compounds.
Abstract: Coronene deposits are removed from a heat exchange zone of the reforming process by recycling a portion of the normally liquid reformate to the heat exchange zone to dissolve the coronene deposits.
Abstract: A startup method for a catalytic reforming process wherein the catalyst is maintained in a bed is provided in which a catalyst comprising an iridium component and at least one additional metal component such as a platinum group metal component is reduced, sulfided and contacted with hydrogen at specified conditions whereby the sulfur is distributed uniformly throughout the catalyst bed prior to contacting the catalyst with the hydrocarbon feed.
Abstract: In an integrated fluid coking and gasification process wherein a stream of fluidized solids is passed from a fluidized bed coking zone to a second fluidized bed and wherein entrained solid fines are recovered by a wet scrubbing process and wherein the resulting solids-liquid slurry is stripped to remove acidic gases, the stripped vapors of the stripping zone are sent to the gas cleanup stage of the gasification product gas. The improved stripping integration is particularly useful in the combination coal liquefaction process, fluid coking of bottoms of the coal liquefaction zone and gasification of the product coke.
Abstract: Coronene deposits are removed from a heat exchange zone disposed in two parallel trains of heat exchangers in a reforming process by reducing the flow of reforming zone effluent in one of the trains of heat exchangers sufficiently to effect condensation of a portion of the reforming zone effluent in said one train of heat exchangers where the coronene is deposited while simultaneously increasing the flow of reforming zone effluent in the second train of heat exchangers. Control means are provided in each of the heat exchange trains.
Abstract: The heat requirements of a fluid coking zone are provided by introducing a hot vaporous hydrocarbon stream into the coking zone instead of the conventional hot coke stream. The fluid coking process may be integrated with a coke gasification process.
Abstract: A catalyst support is prepared by grinding a calcined alumina to a powder, compacting the powder at an elevated pressure, recracking the compressed powder to a predetermined size particle and acid extracting the particle. The support can be composited with catalytic components such as hydrogenation components and/or zeolites and used in a variety of hydrocarbon treating processes, such as hydrorefining, hydrodesulfurization, hydroconversion, reforming, and catalytic cracking.
Abstract: A perovskite is added to a conventional hydrocarbon cracking catalyst comprising a zeolite and an inorganic oxide gel matrix. The perovskite is present in said catalyst in an amount up to about 10 weight percent based on the total catalyst.
Abstract: A combination slurry hydroconversion, coking and coke gasification process is provided wherein carbonaceous solids having an average particle size of less than 10 microns in diameter or the ashes thereof are used as a catalyst in the hydroconversion stage.
Type:
Grant
Filed:
September 15, 1978
Date of Patent:
May 27, 1980
Assignee:
Exxon Research & Engineering Co.
Inventors:
William J. Metrailer, Roby Bearden, Jr., Clyde L. Aldridge
Abstract: A low density particulate vanadium-containing metallic ash concentrate, at least 50 percent of the articles of said concentrate having a diameter not greater than about 1 micron, is produced from a partially gasified coke comprising metallic components including vanadium components by heating the partially gasified coke in an oxidizing atmosphere at a temperataure below the fusion point of the metallic components.
Abstract: Coronene deposits are removed from a heat exchange zone of a reforming process by operating the reforming zone at conditions such that at least a portion of the reformer effluent condenses in the heat exchange zone where the coronene deposit occurs.
Abstract: In the hydrodesulfurization of sulfur-containing heavy hydrocarbon oils, water is injected into the hydrotreating gas and vaporized at a temperature below 450.degree. F. to produce a steam-containing hydrotreating gas which is combined subsequently with the sulfur-containing heavy hydrocarbon oil.
Abstract: In the hydroconversion of carbonaceous materials such as hydrocarbonaceous oils and coal or mixtures thereof, in which inorganic poly acids comprising molybdenum or tungsten or salts thereof are used as catalyst precursors which are converted to catalysts, the use of a combination of phosphoric acid and said poly acids or salts thereof as catalyst precursor wherein the amount of phosphoric acid is such as to provide from about 0.5 to about 3.5 atoms of phosphorus per atom of molybdenum or tungsten results in a catalyst having improved activity.
Abstract: A catalytic hydrocracking process for a hydrocarbonaceous oil is effected by dispersing a thermally decomposable metal compound in the oil, heating the compound in the presence of a hydrogen-containing gas to form a solid, non-colloidal catalyst within the oil and reacting the oil containing the catalyst with hydrogen. Preferred thermally decomposable compound are molybdenum compounds.
Abstract: A catalyst suitable for treating hydrocarbons comprising (1) particles of a crystalline aluminosilicate zeolite, (2) particles of a substantially catalytically inert inorganic oxide having a size of less than 10 microns in diameter, and (3) a catalytic inorganic oxide gel matrix.
Abstract: A perovskite is added to a conventional hydrocarbon cracking catalyst comprising a zeolite and an inorganic oxide gel matrix. The perovskite is present in said catalyst in an amount up to about 10 weight percent based on the total catalyst.
Abstract: A combination slurry hydroconversion, coking and coke gasification process is provided wherein solid fines having an average particle size of less than 10 microns in diameter or the ashes thereof recovered from a gaseous product derived from the coke gasification are used as a catalyst in the hydroconversion stage in combination with a catalyst produced from an oil soluble metal compound in situ in the chargestock of the hydroconversion zone.
Type:
Grant
Filed:
June 7, 1978
Date of Patent:
December 11, 1979
Assignee:
Exxon Research & Engineering Co.
Inventors:
William J. Metrailer, Roby Bearden, Jr., Clyde L. Aldridge