http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CA-2178612-C
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_c65a7116bf9ee77e2f496602f259e04a |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G45-32 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G70-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C5-05 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C5-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C5-03 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07B61-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C9-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G45-40 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G70-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G45-32 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-44 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C11-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C5-09 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C5-05 |
| filingDate | 1994-07-21-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2002-10-01-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_14b7efffb525231f9518c1dcf216926d http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_82ec36aa19e750edd82b0f562cb886ed http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b3cd37136b3fc528e76f2c39cf363998 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_fc1af5e006deaedd313433c8f4fe05e1 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c471487afc126101781ca2ffc55bfcbe |
| publicationDate | 2002-10-01-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CA-2178612-C |
| titleOfInvention | Selective hydrogenation of highly unsaturated compounds in hydrocarbon streams |
| abstract | A process for the selective hydrogenation of the diolefins and acetylenic compounds in an olefin-rich aliphatic hydrocarbon stream (1) comprises contacting the feed stream (1) at 40-300 .degree.F under low hydrogen partial pressure of 0.1-70 psia at a total pressure of 0-350 psig in a distillation column reactor (10) containing a hydrogenation catalyst bed (12) which serves as a component of a distillation structure (10), such are supported PdO encased in a tubular wire mesh. Essentially no hydrogenation of the olefins occur. The feed stream (1) enters below or at the lower end of the catalyst bed (12), and is contacted with hydrogen fed through line (2) in the catalyst bed (12). The overhead (3) is obtained at the overhead, condensed in a condenser (20) and separated in a settler (30), and partially recycled back to catalyst bed (12) as a reflux stream (6). The bottom stream (11) is obtained at the lower end of the distillation reactor, and is partially recycled back as stream (4) after being heated in a heat exchanger (40) as recycle stream (13). Net hydrogenation effluent is obtained as stream (9) , and light gases as stream (7). |
| priorityDate | 1993-12-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 74.