| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_f72483451579f273fbd0af2c1e2242ed |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y10S423-22 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G35-095
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J29-061
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G59-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G65-08
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G45-64 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G65-08
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J29-44
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G59-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J29-06
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G45-64
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J29-035
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G47-16
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G35-095 |
| filingDate |
2000-10-04-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_d6d9dcefd38ce0496a0a78542a4e6e27
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ccbf55f8dd14fb0590be9a222ce8c1b8
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_8661050f3f0b287d8232aee484ed5cb2
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_016337095e085ef5fd7e3692b3ce5fc2
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c9ef32500ca7f6f68a1ce9febd3be06e
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9aefc556ff431899501348207b50533d
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_811182f752e1c18f415cb26c24429ce1 |
| publicationDate |
2006-09-13-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
CZ-297150-B6 |
| titleOfInvention |
A method for producing an n-alkane, a catalyst for carrying out this process and its use |
| abstract |
Process for the production of n-alkane from fractions of mineral oils rich in aromatics. According to the process, the mineral oil fraction reacts on a zeolite catalyst with a steric index SI. ≪ =. 20 and the modified constraint index CI.sup. *. N. > 1. The hydrogen pressure in the reaction is 0.5 to 20 MPa, the temperature is 150 to 550 ° C, the WHSV of the catalyst is 0.1 to 20 h.sup.-1.n. and cyclic hydrocarbons are converted to n-alkanes. Zeolite catalyst for carrying out this process. |
| priorityDate |
1999-10-13-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |