Predicate |
Object |
assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_fd160b48bd4cc483cafd142249836250 |
classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G45-64 |
classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G49-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G45-64 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G47-12 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G73-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G71-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G73-44 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G65-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G65-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G67-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G65-12 |
filingDate |
1995-12-02-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b8a2656174e73ba8f08a15ff4c01263b http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_12072c5f14f775f5e646b6d64e0ebcdb http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_3765bdd244f67331374393940635edce http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_766fe52550d9d420e11672b4243140d8 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9a7905fa328ea14095ab03cee7d0e5d8 |
publicationDate |
1997-10-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber |
EP-0799082-A1 |
titleOfInvention |
Wax hydroisomerization process |
abstract |
This invention discloses a process for producing a high Viscosity Index lubricant having a VI of at least 125 from a waxy hydrocarbon feed having a wax content of at least 40 wt.%. The process comprises catalytically dewaxing waxy paraffins present in the feed by isomerization in the presence of hydrogen and in the presence of a low acidity large pore zeolite isomerization catalyst. This catalyst has a ratio of SiO2/Al2O3, as synthesized, of at least 200:1, wherein the catalyst is prepared in the absence of boron. The feed may be hydrocracked prior to dewaxing with the large pore zeolite. The effluent of the process may also be further dewaxed by either solvent or catalytic means in order to achieve target pour point. |
priorityDate |
1994-12-19-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type |
http://data.epo.org/linked-data/def/patent/Publication |