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classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/F26B3-092
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filingDate 2017-07-27-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 2018-03-16-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_e4f963b5a1f457d2861eb4da85d0dd4e
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publicationDate 2018-03-16-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber CN-207113428-U
titleOfInvention A kind of ammonia process of desulfurization sulphur ammonium after-treatment system
abstract The utility model provides a kind of ammonia process of desulfurization sulphur ammonium after-treatment system, and it mainly includes mother liquid tank, hydrocyclone, centrifuge, conveying worm, vibrated fluidized bed, finished product hopper, heat exchange of heat pipe, cyclone dust collectors, the wet scrubber connected by pipeline with pump/blower fan.Slurries after crystallization inside tower form moisture content in 5 8% sulphur ammonium solids after hydrocyclone, centrifuge dewatering, aqueous≤1% product is formed after vibra fluidized bed drying, dries tail gas that evaporation is formed by returning to desulfurizing tower after cyclone dust collectors, wet scrubber dedusting, cooling, humidification.The mother liquor of system recovery mainly returns to desulfurizing tower, and a portion is introduced directly into vibra fluidized bed drying.Vibrated fluidized bed dries desulfurization slurry using desulfurizing tower inlet flue gas heat.The utility model can reduce system chlorine, fluorinion concentration, meet the requirement arranged outside no waste liquid, while reduce sulphur ammonium drying system energy consumption.
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