http://rdf.ncbi.nlm.nih.gov/pubchem/patent/RU-2552414-C2

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assignee http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_bf52ee91fddaa75095a47da6f658326c
classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01F7-38
filingDate 2013-09-09-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 2015-06-10-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_dfda3d2342d288390885b6647ddfea61
http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_7ee30f5ac4856456949d1c8dbb1ea584
publicationDate 2015-06-10-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber RU-2552414-C2
titleOfInvention Production of alumina
abstract FIELD: process engineering. n SUBSTANCE: invention relates to production of alumina from man-made wastes, particularly, from mineral part of brown coal combustion ash. Charge is prepared by mixing of ash-slag wastes of thermal power plants and limestone taken in exceeds of 28.0-75.0% of stoichiometric amount and, thereafter, sintered. Obtained cake is leached at mixing to get cake pulp and desilicated by calcareous milk and filtered to obtain slime and filtrate. Slime is flushed and carbonized by CO 2 -bearing gas-air mix to filter produced hydrate pulp to get aluminium hydroxide and mother soda solution recycled for cake leaching. Cake leaching is conducted by carbonate solution containing at least 52.0 g/dm 3 of Na 2 CO 3 at 75-80°C. At aluminium oxide leaching from cake, additional primary vibro-cavitation processing is performed. At desilicating of cake pulp by calcareous milk vibro-cavitation processing is reiterated. n EFFECT: higher yield and quality of aluminium oxide. n 4 tbl
priorityDate 2013-09-09-04:00^^<http://www.w3.org/2001/XMLSchema#date>
type http://data.epo.org/linked-data/def/patent/Publication

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