http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-108212029-B
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-584 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P30-40 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P30-20 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C11-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-388 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-38 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C11-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G3-57 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-28 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C1-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-32 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C15-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C10G3-00 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C10G3-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-38 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C11-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C1-20 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C11-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C07C15-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-32 |
| filingDate | 2017-02-03^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2020-09-11^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 2020-09-11^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-108212029-B |
| titleOfInvention | Catalytic conversion reaction method and reactor |
| abstract | The invention relates to the technical field of catalytic conversion processing of a methanol fluidized bed, in particular to a catalytic conversion reaction method and a reactor. The catalytic conversion reaction method is characterized in that the catalytic conversion reaction process of reaction raw materials is finished in a lower layer reactor (1) and an upper layer reactor (2) of a catalytic conversion reactor in parallel, and the reacted product gas of the lower layer reactor and the reacted product gas of the upper layer reactor respectively use independent cyclone separators arranged in a gas-solid separation zone (3) to separate catalysts and then flow out of the catalytic conversion reactor, or the catalysts are separated in a shared cyclone separator and then flow out of the catalytic conversion reactor. The invention adopts a mode of overlapping an upper layer and a lower layer in parallel, and can greatly improve the processing amount of the device on the premise of not increasing the diameter of the catalytic conversion reactor; when the gas-solid separation of the lower reactor and the upper reactor is independently arranged, the functions of two sets of catalytic conversion reactors can be completed, and the investment is saved. |
| priorityDate | 2017-02-03^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
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