http://rdf.ncbi.nlm.nih.gov/pubchem/patent/JP-H05285338-A

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filingDate 1992-04-10-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_d1a7b362314cd8ba969e0bfbfde21196
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publicationDate 1993-11-02-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber JP-H05285338-A
titleOfInvention Wet flue gas desulfurization equipment
abstract (57) [Summary] [Purpose] A wet flue gas desulfurization system that achieves a high desulfurization rate with a compact desulfurization tower structure and low operating costs. [Structure] A ball 11 is provided on the surface of the tank 6 that holds the absorbing liquid. Float, and collide the absorbing liquid falling from the upper part of the desulfurization tower. The slurry-like absorbing liquid, which has absorbed SO 2 and has a lowered pH, collides with the balls 11 to perform mixing / redispersion and surface renewal of absorbing droplets. In addition, in the gap between the balls 11, there is a residue of the air supplied to the tank 6 that was used for the oxidation of CaSO 3 , and the O 2 concentration there becomes high, and SO 2 Absorbing liquid containing a large amount of CaSO 3 by absorbing the balls 11 When it collides with, the oxidation of CaSO 3 is promoted. Also, Since the oxygen concentration in the gas near the surface of the absorbing liquid in the tank 6 is high, the dissolved O 2 concentration in the absorbing liquid in the tank 6 is also high, and the oxidation of CaSO 3 in the tank 6 is promoted. Therefore, a high desulfurization rate can be obtained and the volume of the tank 6 can be reduced.
isCitedBy http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-114849459-A
priorityDate 1992-04-10-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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