http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-217016043-U
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_6817d52da0db77cc14dd0fecd69ea22a |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-86 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F23G7-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-83 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-80 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-76 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D46-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-56 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-40 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-06 |
| filingDate | 2022-04-01-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2022-07-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a11f29928544d132b3a19b35dee81d74 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_6c5083aed79238476079fedba1e44abc http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_eff2a7ca507a63de66554387be10a1f2 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_34ccff70c2e0ad43b37e9e20f64f1b77 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_50faf0661bd9c5ffecdf9f155d4f1f72 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_eeef9c8e0556075a5721e4fbef204e1a http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_cff1a7ad752dcb0e973016fab4a0cca4 |
| publicationDate | 2022-07-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | CN-217016043-U |
| titleOfInvention | Flue gas treatment system |
| abstract | The utility model provides a flue gas treatment system, comprising an SNCR system, an incinerator, a waste heat boiler, an SCR reactor, an economizer, an induced draft system and a chimney which are connected in sequence, wherein the SNCR system is the flue gas generated in the incinerator. Excessive reducing agent is input to the gas, the SCR reactor is used for denitration reaction of flue gas, and the incinerator can decompose the reducing agent into ammonia gas. With this scheme, the ammonia gas required for the catalytic reduction reaction is completely based on the SNCR system spraying excess reducing agent and using the high temperature of the incinerator to decompose the reducing agent into ammonia gas, and through the action of the inner wall of the equipment, the flue gas and ammonia gas are mixed evenly, Full response. In this way, the system does not need to be provided with a reducing agent evaporation or pyrolysis system, nor is it necessary to provide an ammonia injection grille or a flue gas rectifier, thereby optimizing the structure of the flue gas treatment system in the prior art, reducing system failure points, and improving smoke The air treatment effect can meet the emission requirements. |
| priorityDate | 2022-04-01-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 45.