http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-104072376-B
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-141 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C68-04 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C68-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C69-96 |
| filingDate | 2013-03-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2015-12-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 2015-12-23-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-104072376-B |
| titleOfInvention | A kind of by CO 2with the method for methanol-fueled CLC methylcarbonate |
| abstract | The present invention is open a kind of by COn 2 with the method for methanol-fueled CLC methylcarbonate, synthesize as follows: by methyl alcohol, CO and COn 2 , with CeOn 2 -Aln 2 on 3 and CuO-ZnO-Aln 2 on 3 for catalyzer, be 50 ~ 300 DEG C in temperature, pressure is 0.1 ~ 10MPa, and air speed is 500 ~ 5000hn -1 condition under react to obtain methylcarbonate, described methyl alcohol, CO and COn 2 mol ratio be (0.1 ~ 10): (0.01 ~ 0.5): 1, CeOn 2 -Aln 2 on 3 and CuO-ZnO-Aln 2 on 3 volume ratio be (0.1 ~ 10): 1.The present invention is at COn 2 introduce CO water gas shift reaction with in the process of methanol-fueled CLC methylcarbonate, eliminate the water of by-product in reaction process, broken the Equilibrium limit of reaction, significantly improved methanol conversion and methylcarbonate selectivity. |
| isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/EP-4011857-A1 |
| priorityDate | 2013-03-27-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 23.