http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-205659563-U

Outgoing Links

Predicate Object
assignee http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_92ca6faae2cc4a5cf2ce3c4ed0019ce8
classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-56
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-86
filingDate 2016-06-07-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 2016-10-26-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_152e864c1df286e40586c00eff93f1b2
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_b5f83b8756b4c6d0521dd57c85f27862
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_40bac26efcdd9424c8cf1339b60858e8
publicationDate 2016-10-26-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber CN-205659563-U
titleOfInvention Utilize SCR flue gas denitration system of steam air stripping gasification aqueous ammonia
abstract The utility model provides an utilize SCR flue gas denitration system of steam air stripping gasification aqueous ammonia, belongs to the environmental protection equipment field. The empty blender of ammonia, ammonia injection grid, ammonia cigarette blender, SCR reactor, draught fan and the chimney that include ammonia storing tank, heat exchanger, wastewater tank, strip tower and concatenate in proper order, dilutent fan is connected simultaneously to the input of ammonia cigarette blender, the ammonia import of ammonia storing tank, heat exchanger and strip tower concatenates in proper order, and the ammonia steam mix gas exit linkage ammonia of strip tower empties and mixes the ware, the high -temperature steam import of strip tower is used for connecting the high -temperature steam source, and the high -temperature wastewater export of strip tower, the heat medium import of heat exchanger, heat medium export and wastewater tank concatenate in proper order. After the aqueous ammonia in the strip tower passed through steam heating, the insolubilizing of ammonia was volatilized more easily, and partial water only need be evaporated in the pneumatolytic while of ammonia to this technology, so the steam consumption is less, the running cost is lower.
isCitedBy http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-107289324-A
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-107555721-A
priorityDate 2016-06-07-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

Incoming Links

Predicate Subject
isDiscussedBy http://rdf.ncbi.nlm.nih.gov/pubchem/compound/CID222
http://rdf.ncbi.nlm.nih.gov/pubchem/compound/CID962
http://rdf.ncbi.nlm.nih.gov/pubchem/substance/SID419550829
http://rdf.ncbi.nlm.nih.gov/pubchem/substance/SID419512635
http://rdf.ncbi.nlm.nih.gov/pubchem/compound/CID281
http://rdf.ncbi.nlm.nih.gov/pubchem/substance/SID458427267
http://rdf.ncbi.nlm.nih.gov/pubchem/substance/SID453327643
http://rdf.ncbi.nlm.nih.gov/pubchem/compound/CID14923

Total number of triples: 24.