http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-105709598-B
Outgoing Links
| Predicate | Object |
|---|---|
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2258-0283 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-8625 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-60 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-78 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-86 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-78 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-60 |
| filingDate | 2016-04-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2018-08-24-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate | 2018-08-24-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-105709598-B |
| titleOfInvention | Based on the redox flue gas ammonia process synchronized desulfuring and denitrifying technique of oxalic acid |
| abstract | The invention discloses one kind being based on the redox flue gas ammonia process synchronized desulfuring and denitrifying technique of oxalic acid, concentrate haptoreaction in concentration tower and tower is sent into after being pressurized including flue gas, the flue gas for going out concentration tower is sent into and passes upward through packing layer and spraying layer in the middle part of absorption tower and be discharged by exhanst gas outlet with after the reverse haptoreaction of circulating absorption solutionï¼›Concentration tower bottom of tower extension concentrate is through iron removal system except feeding ammonium sulfate crystallization system after iron, the circulating absorption solution by the ejection of absorption tower top spraying layer enters absorb the bottom of the tower after the packing layer on tower top and the reverse haptoreaction of flue gas and is pumped to after the regeneration of Photocatalytic Regeneration reaction system into recycled pulp liquid bath by recycling successively, then is transmitted back to as circulating absorption solution in the spraying layer penetrating tower on absorption tower top after filling into ammonium hydroxide, complexing agent Fe (II) EDTA, oxalic acid and ferrous sulfate in regenerating slurry tank.Present invention process is simple, operating cost is low, low energy consumption, control is easy, denitration effect is good, byproduct is high-quality. |
| priorityDate | 2016-04-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 41.