http://rdf.ncbi.nlm.nih.gov/pubchem/patent/RU-2032652-C1
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_67f8f23b17c6830bfdf26a1c36fc31b4 |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-584 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C39-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C15-02 |
| filingDate | 1992-05-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 1995-04-10-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9afcbf0fba9c97652e48c1c442deb45a http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_2cc1d1dae287243021fa3f7f77dc6d09 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_90d874e133c025875ff62cd5fa902a0c http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_0c87c052a8b8ec725b13cb3629b64b87 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9a993c020672d89fb23cfeee2dbe060e http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9465c0883db73089e8d9a3cad65a8dc9 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c5ecb050cb2bc2788e38ae3ed63a5a3c http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_bdc5fbc49f9e9bdd251668175b71dd3c http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_5cb9a978708fd20eeaadd3d227c56838 |
| publicationDate | 1995-04-10-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | RU-2032652-C1 |
| titleOfInvention | Process for preparing aromatic c6-c9-hydrocarbon fractions |
| abstract | FIELD: petrochemical and chemical industries. SUBSTANCE: aromatic γ-Al 2 O 3 hydrocarbon fractions. The starting raw material includes phenol resin waste resulting from the production of phenol and acetone, 2-isopropylbenzene or a recirculate resulting from the production of phenol and acetone, catalysts have the following composition (wt %): (1) 0.75 Si-Pd; 5 crystalline magnesium silicate; up to 100 MoO 3 (2) 5 NiO 15 γ-Al 2 O 3 ; 10 crystalline magnesium (3) 45 ZSM-8 type zeolite; 1.0 ZnO: up to 100 γ-Al 2 O 3 1000; (4) 0.45 Pt; 0.25 Sn; 0.25 F; 5 zeolite 25M-8 or ZSM-23 type; and up to 100 γ-Al 2 O 3 . Conditions; the process is carried out subsequently by contacting the raw material with the four catalysts indicated above in two reactors. The catalyst weight ratios are 1:2, 1:9 and 3:4, 1:9; 300-380 C; 2.0 4.0 MPa, the raw material volumetric feed rate is 1,5-2,5 h -1 ; the phenol resin to recirculate volumetric ratio is 1:1, and the hydrogen to raw material volumetric ratio is (900-1600):1. EFFECT: improved process. 2 cl, 1 tbl |
| priorityDate | 1992-05-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 55.