초록 ▼

An improved process is described for the hydrocracking of heavy hydrocarbon oil, such as oils extracted from tar sands. The charge oil in the presence of an excess of hydrogen is passed through a tubular hydrocracking zone, and the effluent emerging from the top of the zone is separated into a gaseo

An improved process is described for the hydrocracking of heavy hydrocarbon oil, such as oils extracted from tar sands. The charge oil in the presence of an excess of hydrogen is passed through a tubular hydrocracking zone, and the effluent emerging from the top of the zone is separated into a gaseous stream containing a wide boiling range material and a liquid stream containing heavy hydrocarbons. According to the novel feature, the hydrocracking process is carried out in the presence of a catalyst consisting of finely divided coal or other carbonaceous material carrying catalytically active metals from Group VIA and Group VIII of the Periodic Table of Elements, e.g. cobalt and molybdenum. The catalyst is slurried with the charge stock and has been found to greatly reduce coke precursors and thereby prevent the formation of carbonaceous deposits in the reaction zone while also being effective in reducing the sulfur concentration of the product.

대표청구항 ▼

A process for hydrocracking a heavy hydrocarbon oil, at least 50 wt. % of which boils above 524°C. which comprises: (a) passing a slurry of said heavy hydrocarbon oil and 0.01-5 wt. % of a catalyst comprising finely divided sub-bituminous coal carrying cobalt and molybdenum compounds in amounts of 0

A process for hydrocracking a heavy hydrocarbon oil, at least 50 wt. % of which boils above 524°C. which comprises: (a) passing a slurry of said heavy hydrocarbon oil and 0.01-5 wt. % of a catalyst comprising finely divided sub-bituminous coal carrying cobalt and molybdenum compounds in amounts of 0.2 to 10 wt. % Co and 0.4 and 20 wt. % Mo in the presence of 500-50,000 scf of hydrogen per barrel of said hydrocarbon oil upwardly through a tubular hydrocracking zone, said hydrocracking zone being maintained at a temperature between about 400°and 500°C., a pressure above 500 psig. and a space velocity between about 0.5 and 4.0 volumes of heavy hydrocarbon oil per hour per volume of hydrocracking zone capacity, (b) removing from said hydrocracking zone a mixed effluent containing a gaseous phase comprising hydrogen and vaporous hydrocarbons and a liquid phase comprising heavy hydrocarbons, and (c) separating said effluent into a gaseous stream containing hydrogen and vaporous hydrocarbons and a liquid stream containing heavy hydrocarbons.