http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-102641737-B
Outgoing Links
| Predicate | Object |
|---|---|
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-89 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C29-156 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C29-157 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-78 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J23-83 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C31-02 |
| filingDate | 2012-03-21-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2016-08-17-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 2016-08-17-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-102641737-B |
| titleOfInvention | A kind of CO hydrogenation is directly synthesized C2-C10the catalyst of straight chain mixing primary alconol and preparation method and applications |
| abstract | A kind of for CO hydrogenation synthesis C 2 ‑C 10 The catalyst of straight chain mixing primary alconol.Catalyst is by active component, auxiliary agent and carrier composition.Active component is Co element, and auxiliary agent is one or more auxiliary agents in Li, Ce, Ca or Pd element, and carrier is activated carbon.Active component weight is 1～30%, and auxiliary agent weight is 0.01～10%.Infusion process is used to be supported on absorbent charcoal carrier by catalytic component.After catalyst drying, roasting, before using, carry out reduction activation.In slurry bed system or fixed bed reactors, under uniform temperature, pressure and under the effect of this catalyst, CO hydrogenation one-step synthesis is with C 2 ‑C 10 Straight chain mixing primary alconol is the product of primary product. |
| priorityDate | 2012-03-21-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 51.