Predicate |
Object |
assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_50533b6a1a53d726bf5ee27904d86fda |
classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C2523-32 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C2523-24 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C2523-16 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C2521-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C2521-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C2521-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C2523-30 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C2523-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C2521-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C2529-06 |
classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C5-2512 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C6-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C11-107 |
classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C11-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07B61-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C6-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C11-107 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C11-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C5-25 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C4-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C4-06 |
filingDate |
2003-03-07-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate |
2008-09-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_3b9a52b1ac18b816c34571bf509b265c http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_e4e44c4448da05e72f65828b402f8c45 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0743fe4340043cd98fd7f8372bbcb5e7 |
publicationDate |
2008-09-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber |
CA-2477789-C |
titleOfInvention |
Process for producing propylene and hexene from c4 olefin streams |
abstract |
A C3 to C6 hydrogen cut from a cracking unit is processed for the conversion of olefins to propylene and hexene via autometathesis. The autometathesis of a mixed normal butenes feed in the presence of a metathesis catalyst operates without any ethylene in the feed mix to the metathesis reactor. Some fraction of the 2-butene feed may be isomerized to 1-butene and the 1-butene formed plus the 1-butene in the feed react rapidly with the 2-butene to form propylene and 2-pentene. The feed to the reactor also includes the recycle of the 2-pentene formed in the reactor with unreacted butenes to simultaneously form additional propylene and hexene. In one embodiment, some or all of the 3-hexene formed in the reaction is isomerized to 1-hexene. In another embodiment, some portion of the 3-hexene produced in the main metathesis reaction is reacted with ethylene to produce 1-butene without the need for superfractionation. In another embodiment, the 3-hexene product is hydrogenated and recycled back to the cracking heaters. |
priorityDate |
2002-03-07-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type |
http://data.epo.org/linked-data/def/patent/Publication |