| Predicate |
Object |
| assignee |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_1df93ed61a1025e3fffb791365ebe6e4 |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-00991
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2208-00938 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F2-44
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F2-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F2-01
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-24
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-18
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-1818
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08F10-00 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-24
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08F10-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08F2-01
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08F2-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J8-18 |
| filingDate |
2017-12-15-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_c6e052bbbaf2680cced76210172989d5
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a3e49338a1557017cd5696afd935071f
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_193af1eef93ba73017d75db26f189d5f
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_7ff9ced3ff536b9221b908c9eee978c1
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_50a66f6a8f962f499f9f2bb4acfa88f1
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_46466f5120b5a376dc0b6fd24736faf5
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9af1ad6d535fe0dc657e4e44bae2fc3c |
| publicationDate |
2019-08-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
CN-110114133-A |
| titleOfInvention |
Process for Feeding Fluids to Gas Phase Polymerization Reactors |
| abstract |
The fluid is fed into the polymer bed of the fluidized bed gas phase polymerization reactor by introducing the fluid into the polymer bed through a distributor extending into the fluidized bed zone of the reactor and terminating at the discharge end. The position satisfies the following formula: d/D > 0.002, where d is the distance from the discharge end of the distributor to the reactor wall, and D is the diameter of the reactor in the fluidized bed zone. |
| priorityDate |
2017-01-20-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |