http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-103702751-B
Outgoing Links
Predicate | Object |
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classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-00203 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-00557 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-00141 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-584 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-0084 |
classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C51-215 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C51-235 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J23-92 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C51-265 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C51-313 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C45-52 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J38-30 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-226 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-386 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C51-377 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-0055 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J27-285 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C07C45-38 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-1827 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-1818 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-1836 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-24 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J38-22 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-22 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-38 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-18 |
filingDate | 2012-07-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate | 2016-10-12-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationDate | 2016-10-12-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | CN-103702751-B |
titleOfInvention | Continuous catalyst regeneration in fluidized-bed reactor |
abstract | nullThe present invention relates to catalytic reactor,It includes room (1) and the segregation apparatus (2) being arranged in room (1),Described segregation apparatus limits at least one reaction zone (3) and at least one renewing zone (4),Reactant stream feed arrangement (15 is passed through in described reaction zone (3),16) supply and be connected with the first gas withdrawing device (13) in its exit,Described renewing zone (4) is supplied by recovery stream (17) and is connected with the second gas withdrawing device (10) in its exit,Described reactor is suitable to the fluidised bed of catalyst particles (5) being included in reaction zone (3),Described reactor makes catalyst granules can pass to described renewing zone (4) from described reaction zone (3),And described reactor makes to be moved to by catalyst granules the device of described renewing zone (4),It is enable to return it to described reaction zone (3).In reaction zone (3), the ratio between maximum cross-section and the maximum cross-section of renewing zone (4) of catalyst bed is 1 100.And, carry out that chemical reaction process makes the deactivation time (efficiency being defined as catalyst behind has reduced the response time of 25%) of catalyst be the recovery time (be defined as its initial efficiency behind and declined the recovery time that the catalyst of 25% returns to about the 100% of its initial efficiency) by this way in described reactor 1 20 times. |
priorityDate | 2011-07-12-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 99.