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filingDate 2001-01-09-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 2010-06-08-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ea3348c0b5b7e41640059e0e1143154d
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publicationDate 2010-06-08-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber CA-2330461-C
titleOfInvention Petroleum fraction conversion process including a hydroconversion stage in a bubbling bed, a separation stage, a hydrodesulfuration stage and a cracking stage
abstract A process for converting a hydrocarbon fraction comprising a step a) of treating a hydrocarbon feedstock in the presence of hydrogen in at least one three-phase reactor (1), containing at least one ebullated bed hydroconversion catalyst, a step b) in which at least a portion of the effluent from step a) is sent to a separation zone (2) from which a fraction F1 usually containing at least a portion of the gas is obtained. gasoline, and the atmospheric gas oil contained in the effluent of step a), and a fraction F2 usually containing mainly compounds having boiling points higher than those of at-atmospheric gas oil, a step c) of hydrodesulphurization of at least a portion of the fraction F1 in at least one reactor (4) containing at least one fixed bed hydrotreatment catalyst under conditions for obtaining a reduced sulfur effluent, and a step d) of wherein at least a portion of the fraction F2 is sent to a catalytic cracking section (6).
isCitedBy http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2012066572-A2
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