http://rdf.ncbi.nlm.nih.gov/pubchem/patent/RU-2296624-C2

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assignee http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_7c7cc420fe6d3b96a0562bb195eae0f0
classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B03B7-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B03B9-04
filingDate 2000-06-19-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 2007-04-10-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_5c528d78cb4b3eae072e0b280a4a1705
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_4f4a3c9c78cbc641f2c591d3aaa3230d
publicationDate 2007-04-10-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber RU-2296624-C2
titleOfInvention Heat-and-power station ash-and-slack waste processing method
abstract FIELD: heat-and-power engineering. n SUBSTANCE: processing consists in separation of glass microspheres from total waste mass by agitating slurry for 10-12 min while maintaining liquid-to-solids ratio between 3:1 and 5:1 followed by settling and removal of microspheres from the slurry surface. Separation of non-burned organic residues is performed after they are reduced to fragments (90% of class 0.044 mm) in flotation process, which is carried out at initial pH 7 and flotation pH 9 employing kerosene in amounts 45-70 kg/t in main flotation and 25-40 kg/t in control flotation. Flotation is followed by step-by-step magnetic separation, first in week magnetic field at 50-150 mTl and then in magnetic fields of gradually increased intensity: from 500 to 1700 mTl with steps of 200 mTl. n EFFECT: increased integrated recovery of all valuable constituents of ash-and-slack waste. n 4 cl
isCitedBy http://rdf.ncbi.nlm.nih.gov/pubchem/patent/RU-2632081-C1
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priorityDate 2000-06-19-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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Total number of triples: 27.