http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-106051810-B
Outgoing Links
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classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-56 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-504 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F23L7-007 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F23L15-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F23N1-025 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F23J15-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F23J15-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-78 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/F23N5-02 |
classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F23N1-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-78 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F23L15-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F23J15-06 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F23J15-04 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F23L7-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-50 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F23N5-02 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01D53-56 |
filingDate | 2016-05-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
grantDate | 2018-10-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationDate | 2018-10-09-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
publicationNumber | CN-106051810-B |
titleOfInvention | The desulphurization denitration dedusting complete set of equipments of liquefied gas used for combustion |
abstract | A kind of desulphurization denitration dedusting complete set of equipments of liquefied gas used for combustion is mainly made of burner, denitrification device, heat exchanger, devulcanizer, intelligent bubble column, ammonium hydroxide dilution tuner, liquid oxygen tank, refrigerating chamber, liquid gas storage tank;The oxygen of liquid oxygen tank first passes through refrigerating chamber, using heat exchanger, finally enters combustion chamber and replaces air-breathing;The liquefied gas of liquid gas storage tank first passes through flow control valve one, enter back into burner combustion, burner combustion generation combustion tail gas enters denitrator and is reacted with liquefied ammonia, remove nitrogen oxides, enter by the tail gas of denitrator and exchanges heat with cryogenic oxygen, devulcanizer is entered back into react with ammonium hydroxide, remove oxysulfide, generate ammonium sulfate, enter intelligent bubble column by the tail gas of devulcanizer, ammonia of escaping in tail gas is only absorbed by the water, tail gas empties, the low concentration ammonium hydroxide that intelligent bubble column generates enters ammonium hydroxide dilution tuner and liquefied ammonia and aquatic production suitable concentration ammonium hydroxide, into entrance devulcanizer desulfurization;Advantage is:It is energy saving, desulphurization and denitration, dedusting, emission reduction, pollution-free. |
priorityDate | 2016-05-08-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 47.