http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-210528467-U
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_4e00c9660dfe8eb6bd334b1d1fa14939 |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P20-129 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01B17-04 |
| filingDate | 2019-08-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2020-05-15-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_03a90303e833003173792033f4b2074a http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_d69014d2a66470ae44a18646c1f1c8d8 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_046edbdf0b27a4110bcf5d87bda8d157 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_bbd8abf3c7fed039a63710a630178c36 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_266ccf6e6568a86ec2628686b305d2d7 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_89b77d5ad866acbacc3a33469fe69d1c http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_9ff68eed70aac74e3d670210650fcbaa http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_965873df2d73e289029e0413cf0dcce6 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_149dbeb4d7ded8005de538b8aa93d29d |
| publicationDate | 2020-05-15-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-210528467-U |
| titleOfInvention | Selective oxidation sulfur recovery device |
| abstract | The utility model belongs to the technical field of coal chemical industry, and relates to a selective oxidation sulfur recovery device, which comprises a mixed gas unit, a primary reactor, a waste heat boiler, a condensation sulfur collector, a secondary reactor and a cooling recovery unit; the mixed gas unit comprises a separation tank, a fan, a heating tank and a mixing tank which are connected in sequence; the cooling and recovering unit comprises a condenser and a sulfur trap which are connected in sequence; the outlet of the mixed gas unit is finally connected with the inlet of the cold sulfur agglutinator through the tube side of the primary reactor and the tube side of the waste heat boiler; the outlet of the cold sulfur agglutinating device is respectively connected with the inlet of the heating tank of the mixed gas unit and the inlet of the secondary reactor; and the outlet of the secondary reactor is sequentially connected with a condenser and a sulfur trap. The utility model discloses simple process equipment is few, and the investment is little, and running cost is low, the rate of recovery is high, can the recovery processing different concentration hydrogen sulfide gas body. |
| priorityDate | 2019-08-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 29.