http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CA-2038824-C

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assignee http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_e31a7bcbf6b7edcaf10cca6f5400387f
classificationCPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G65-08
classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C5-27
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C9-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G65-08
filingDate 1991-03-21-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 2001-12-18-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_f06fa1812c382332fd78212c41c5904f
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ea9347a85ce498c55163243952010bcf
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_e4278e4ca22f3473dcf98a2d6601ea3b
publicationDate 2001-12-18-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber CA-2038824-C
titleOfInvention Combination process for hydrogenation and isomerization of benzene- and paraffin-containing feedstocks
abstract The benzene content in a gasoline pool is reduced by a process that hydrogenates a benzene-containing isomerization zone feedstream. In addition to reducing the benzene concentration, the hydrogenation zone is also used to heat the isomerization zone feed and thereby eliminate the need for an isomerization zone heater. The process employs mild saturation conditions which eliminates hydrocracking and prevents the loss of isoparaffin yield. Additional cyclic hydrocarbons produced by the saturation of benzene can be processed in the isomerization zone for ring opening to increase the available paraffinic feedstock or the isomerization zone can be operated to pass the cyclic hydrocarbons through to a product recovery section.
priorityDate 1989-12-29-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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