| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_ece422ae3f802bb6acdb4a114c69e441 |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-52 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C1-04
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G2-334 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G2-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C1-04 |
| filingDate |
1996-02-01-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate |
1997-12-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c46f7b8b05a0fede4a0343586eba78bc
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_3159749c04ecbcb6501e030b920de21f
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_398992a96547ab0a58ea510a30698ae1
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_965e4225da8d9b169f267408cfb82ae0
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_010d11e680c3c75054cfea707861c9e5
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a18dd44302f8e800f833e7aeaadfb3eb
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c487e5d097540b442773e98433f7d0c7
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_3455096b23e14da06c1c17ae0c092a58
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0404bebc7f03cb10261e12c98ce7efb1 |
| publicationDate |
1997-12-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
RU-2100332-C1 |
| titleOfInvention |
Method for production of mixture of hydrocarbons $$$ |
| abstract |
FIELD: production of hydrocarbons of synthesis gas. SUBSTANCE: synthesis gas is prepared of mixture of hydrocarbons $$$ wherein fraction $$$ being saturated by isoparaffins, preliminary, by isopentane and isohexane. The process is carried out in zone of contact with catalyst whose particles has two components, namely, crystalline aluminosilicate ($$$ in it being 25-150; content of sodium oxide being 0.2-0.5 mass %; content of rare-earth elements being 0.1-5 mass %) and zinc-chromium component (atomic ratio Zn/Zn+Cr in it being from 1:9 to 1:1). Catalyst is reduced at temperature not higher than 400 C. Contact of synthesis gas (ratio CO/$$$ in it being 1-12) with catalyst takes place at 330-400 C and at pressure 6-15 MPa; volume rate of feeding of raw materials is 50-11000 $$$. EFFECT: increased yield of liquid isoparaffins, preferably, light isoparaffins. 2 tbl |
| priorityDate |
1996-02-01-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |