http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CA-2228889-C
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_802cb425a297a0766bc7d8cdc2f03898 |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J21-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-1061 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-1047 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-1042 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-1019 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J23-85 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G45-08 |
| classificationIPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J21-04 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J27-19 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-85 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J35-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G45-08 |
| filingDate | 1996-08-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2007-11-13-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_1a007a246d5963c15afa4437c83f51fe |
| publicationDate | 2007-11-13-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CA-2228889-C |
| titleOfInvention | Hydroconversion process employing a catalyst with specified pore size distribution and no added silica |
| abstract | A process for hydroconverting a hydrocarbon feed containing components boiling above 1000 °F (538 °C), sulphur, metals and carbon residue into product containing decreased levels of components having a boiling point greater than 1000 °F (538 °C), decreased levels of sulphur, particularly decreased sulphur contents in the unconverted 1000 °F+ (538 °C+) boiling point products and reduced sediment, which comprises: contacting said hydrocarbon feed with hydrogen at isothermal hydroprocessing conditions in the presence of, as catalyst, a porous alumina support containing <= 0.5 wt.% of silica, no silicon containing components being intentionally added, and bearing 2.2-6 wt.% of a Group VIII metal oxide, 7-24 wt.% of a Group VIB metal oxide and 0.0-2.0 wt.% of a phosphorus oxide, said catalyst having a Total Surface Area of 195-230 m2/g, a Total Pore Volume (TPV) of 0.82-98 cc/g, and a Pore Diameter Distribution wherein 27.0-34.0 % of the TPV are macropores of diameter > 250 .ANG., 66.0-73.0 % of the TPV are micropores of diameter 250 .ANG., 55-64.5 % of the Pore Volume in pores with diameters <=.50 .ANG. are micropores of diameter within ~ 25 .ANG. of a pore mode by volume of 110-130 .ANG., and < 0.05 cc/g of micropore volume are micropores with diameters < 80 .ANG.. |
| priorityDate | 1995-08-24-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 54.