http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2013515730-A
Outgoing Links
Predicate | Object |
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classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C11-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07D303-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07D301-03 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07D301-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J23-36 |
classificationIPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07B61-00 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07D301-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07D303-02 |
filingDate | 2010-12-20-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationDate | 2013-05-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | JP-2013515730-A |
titleOfInvention | Start process of highly selective ethylene oxide catalyst |
abstract | A process for starting ethylene epoxidation is provided. The process includes initiating an epoxidation reaction by reacting a feed gas composition in a presence of an epoxidation catalyst at a first temperature of from about 180 ° C to about 210 ° C. The first temperature was raised to a second temperature of about 230 ° C. to about 290 ° C. over about 6 hours to about 50 hours simultaneously with addition of a sufficient concentration of moderator, and adsorbed to the catalyst after reaching the second temperature. The amount of moderator is about 10 to about 50 g / m 3 with respect to the catalyst. A second temperature is maintained while adjusting the feed gas composition to include about 0.5% to about 25% CO 2 for about 50 hours to about 350 hours. The moderator concentration is increased to a level exceeding the sufficient concentration, and at the same time the second temperature is lowered to the third temperature. |
priorityDate | 2009-12-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 55.