http://rdf.ncbi.nlm.nih.gov/pubchem/patent/ES-271857-A1

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classificationCPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J23-883
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classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-883
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G47-00
filingDate 1961-11-09-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationDate 1962-04-01-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber ES-271857-A1
titleOfInvention A PROCEDURE FOR CONVERTING A HIGH BOILING POINT HYDROCARBON OIL INTO MORE VALUABLE LOWER BOILING POINT HYDROCARBON PRODUCTS
abstract The hydrocracking of hydrocarbon oils boiling at least predominantly above 343 DEG C. is effected by mixing with recycle oil and 35,6-178 normal cubic metres of hydrogen per hectolitre of oil mixture, passing at least 0,5 vol./vol./hr., 316 DEG -454 DEG C., and 54,5-204 atmospheres over a catalyst comprising a carrier containing 20-50% silica and 50-80% alumina and molybdenum and p nickel or compounds thereof in amounts, calculated as element and based on the weight of the carrier, of more than 10% but not more than 30% of molybdenum and 1-6% of nickel, and separating hydrogen sulphide and ammonia, a hydrogen-rich recycle gas, gasoline and middle-distillate fractions and a recycle oil boiling above 343 DEG -371 DEG C. The volume ratio of oil mixture passed to the reaction zone to fresh feed may be 1-3 and the space velocity 0,5-2 vol./vol./hr. Preferably after removing gases the effluent is distilled in a first column to recover hexanes and lower boiling materials and a gasoline fraction and optionally a kerosene fraction and in a second column the bottoms are separated into middle-distillate and recycle oil.
priorityDate 1960-11-09-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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