http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-207786344-U
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_a928f156bb574b14330a02dec339e742 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-56 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-86 |
| filingDate | 2017-12-19-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2018-08-31-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6bd05ebf77065167160f97bed54627c9 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_dfbf012d3788ffa856979dd74998cdd2 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_32a9c25170fef98baca36546bb94de40 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_4c838dfffa12e65eca6e571574c49a33 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_646fed117b3ae1eaab20ea080a2899b7 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_62df3ec2ca752b6e1843f5a7b0ef7e22 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_ba24d0cc36568bab77e0fcdaf743339b http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b000fd7d2100f7a23f3a7adfeca106b5 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_818cdca612190c036e724c385a24f560 |
| publicationDate | 2018-08-31-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-207786344-U |
| titleOfInvention | A kind of quenched denitration device of glass furnace |
| abstract | The utility model essentially discloses a kind of quenched denitration device of glass furnace, technical solution：Including flue gas system, spray ammonia system, high-temperature heat-exchanging, Benitration reactor, compressed air cylinder and tail portion heat exchanger, the flue gas system includes flue, high-temperature heat-exchanging is installed at the flue entrance, it is connect with Benitration reactor at the flue outlet, the spray ammonia system is located at high-temperature heat-exchanging outlet end side, and it is connect with flue by pipeline, flue tail end side is internally provided with fluidisation mixer, it is located in the flue below fluidisation mixer and lime silo and fluidized air blower is connected with by pipeline, the Benitration reactor is internally provided with the first catalyst layer, second catalyst layer and preparing catalyst layer, the utility model has simple in structure, the advantages of controlling flue-gas temperature and promoting denitration efficiency. |
| isCitedBy | http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-115727341-A http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-115727341-B |
| priorityDate | 2017-12-19-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 28.