http://rdf.ncbi.nlm.nih.gov/pubchem/patent/RU-2408659-C1
Outgoing Links
Predicate | Object |
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assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_8f56eff9e5991176e38bf4abbc3f4a61 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C5-22 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G65-02 |
filingDate | 2009-07-20-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate | 2011-01-10-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9f0ca09380128f0071214e6e4829462a http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_09ea2bb59796e226d67764dfd5976011 |
publicationDate | 2011-01-10-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | RU-2408659-C1 |
titleOfInvention | Method for isomerisation of light gasoline fractions containing c7-c8 paraffin hydrocarbons |
abstract | FIELD: chemistry. ^ SUBSTANCE: invention relates to a method for isomerisation of light gasoline fractions containing C7-C8 paraffin hydrocarbons by extracting the C7-C8 fraction from wide gasoline fractions and bringing said C7-C8 fraction into contact with a catalyst containing a hydrogenating-dehydrogenating component on an oxide support in a hydrogen medium at high temperature and pressure in two reactors, fractionation to obtain a product fraction and a fraction of n-paraffins, monomethyl-substituted paraffins and methylcyclohexane which is recirculated into the gas-raw material mixture. The C7-C8 fraction (raw material) is extracted such that its content of C5-C6 hydrocarbons is equal to 0.1-15 wt %, while that of C8 hydrocarbons is equal to 0.1-20 wt %, by mixing the extracted C7-C8 fraction with hydrogen in molar ratio hydrogen: raw material equal to 0.5-4, with formation of a gas-raw material mixture and feeding said mixture into the first of two series-connected isomerisation reactors at temperature 160-250C, pressure 1.0-4.0 MPa, and bulk speed for feeding material equal to 1-5 h-1. Quenched hydrogen at 40-60C is fed into the second reactor, with molar ratio hydrogen: raw material equal to (0.1-1.0):1, and the oxide support is a composition of metal oxides: aAI2O3bZrO2cWO3dTiO2eMnO2, where weight ratios of the oxides are as follows: a=0.04-0.30; b=0.60-0.90; c=0.05-0.15; d=0.001-0.10; e=0.001-0.01. ^ EFFECT: obtaining isomerisate with high octane number. ^ 2 cl, 3 tbl, 17 ex |
isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/WO-2015167841-A3 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/RU-2533810-C2 http://rdf.ncbi.nlm.nih.gov/pubchem/patent/RU-2753968-C1 |
priorityDate | 2009-07-20-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 101.