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filingDate 2004-07-13-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a93a702fd1dddc408ce0e7699c671166
publicationDate 2005-01-27-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber WO-2005007777-A2
titleOfInvention Desulfurization of a naphtha gasoline stream derived from a fluid catalytic cracking unit
abstract A process for reducing sulfur compounds in naphtha to produce gasoline of ultra-low sulfur content, i.e., containing from 10-30 ppm of sulfur, from a fluidized catalytic cracking reactor (10) effluent stream, withdraws a high sulfur content sidestream (20) of catalytically produced medium and heavy cat naphtha with an endpoint of +430°F that is fed to a side column (30) where any thiophenic and benzothiophenic compounds are catalytically reacted with hydrogen (32) to convert them to hydrogen sulfide. The desulfurized light and mid-cut naphtha (44) is returned to the main fractionation unit and the heavy catalytic naphtha is withdrawn as a product stream from the bottom of the side column (30).
priorityDate 2003-07-14-04:00^^<http://www.w3.org/2001/XMLSchema#date>
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