http://rdf.ncbi.nlm.nih.gov/pubchem/patent/DE-2548741-A1

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classificationCPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01D53-34
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http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01F5-42
filingDate 1975-10-31-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_03914d677d7c8eb1215eb3d0da9c4242
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_dddc2b504c4cc56f5591190391733dc9
publicationDate 1976-06-10-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber DE-2548741-A1
titleOfInvention PROCESS AND EQUIPMENT FOR THE RECOVERY OF SULFUR AND MAGNESIUM FROM EXHAUST GASES
abstract The recovery of the S and Mg in the form of technically pure Mg(HSO3)2 from the waste gases bearing MgO dust from a liquor combustion plant in a multistage washing process, in which the waste gas is washed with MgSO3 suspension in >=1 stage, comprises producing a water-insol. MgSO3 cpd. in a suspension at least in a second washing stage and sepg. from the suspension, then passing the suspension freed from coarse MgSO3 into a clarifier, in which the water-soluble impurities are drained from the water-insol. constituents and the remaining fine grained suspension is recycled to the second washing stage, whilst the coarse MgSO3 is passed to the first stage in the form of a suspension and converted to Mg(HSO3)2 by the SO2-rich waste gas stream. The prodt. is obtd. in very pure form.
priorityDate 1974-11-29-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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