http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-105618061-B
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-1019 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10L3-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-1061 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J35-1042 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J23-755 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J35-10 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10L3-08 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-755 |
| filingDate | 2016-01-29-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2018-03-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 2018-03-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-105618061-B |
| titleOfInvention | A kind of slurry bed system carbon dioxide methanation bimetallic catalyst and its preparation method and application |
| abstract | A kind of slurry bed system carbon dioxide methanation bimetallic catalyst and its preparation method and application.The present invention relates to a kind of bimetallic catalyst applied to slurry bed system carbon dioxide methanation, and the preparation method of the bimetallic catalyst and its application in the reaction of slurry bed system carbon dioxide methanation.The present invention is prepared for regular mesoporous nickel cobalt bimetallic aluminium oxide catalyst by the step of evaporation induced self-assembly method one.Wherein, by mass percentage consisting of：The wt.% of active component Ni 20 ~ 60, the wt.% of active component Co 0.1 ~ 8, the wt.% of alumina support 39 ~ 78；The specific surface area of prepared catalyst is 100 ~ 500 m 2 / g, pore volume are 0.2 ~ 1.0 cm 3 / g, the nm of aperture 5 ~ 15.Preparation process of the present invention is simple, and nickel cobalt active component is more dispersed in carrier surface and duct in catalyst, enhances the interaction of active component and carrier, applied under slurry bed system carbon dioxide methanation reaction condition, CO 2 Conversion ratio may be up to 81.5%, CH 4 Selectivity reaches more than 99.7%. |
| priorityDate | 2016-01-29-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 62.