| Predicate |
Object |
| classificationCPCAdditional |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2259-124
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2258-0283
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D2251-206
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F23J2219-10
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F23J2215-10 |
| classificationCPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F02B35-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F23J7-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J8-0278
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F01N5-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-86
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F23J15-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-8631
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F23J15-003
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F23J15-02
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F01N3-30
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-90 |
| classificationIPCInventive |
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-94
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J4-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-56
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J7-02 |
| filingDate |
2011-06-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationDate |
2013-08-22-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber |
JP-2013533109-A |
| titleOfInvention |
Hot gas and other heated gas extraction systems for reactant evaporation |
| abstract |
Hot exhaust gas is extracted from the flue gas flue and its thermal energy is used to evaporate the aqueous solution of the reactant such as aqueous ammonia solution or to supply a mixture of heated air and process gas. The compressed air provides the driving force that creates a vacuum in the ejector venturi device that draws hot exhaust gases (“hot gases”) from the exhaust flue. In one embodiment, hot gas is drawn into the vaporizer unit. The injected reactant aqueous solution is evaporated by the heat energy in the high temperature gas. The evaporated mixture is drawn into the ejector and is entrained by the motive air. The diluted reactant vapor mixture is injected back into the flue gas flue to continue the selective catalytic reduction (SCR) process and reduce nitrogen oxides (NOx). [Selection] Figure 2 |
| isCitedBy |
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-113606020-A
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-2017129139-A
http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-113606020-B |
| priorityDate |
2010-06-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type |
http://data.epo.org/linked-data/def/patent/Publication |