http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-108996536-B

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classificationCPCAdditional http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01P2006-80
classificationCPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C01F17-271
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classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01F17-17
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C01F17-271
filingDate 2018-08-08-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 2020-07-21-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationDate 2020-07-21-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber CN-108996536-B
titleOfInvention A kind of extraction and separation method of co-producing pure praseodymium and pure gadolinium
abstract The invention provides an extraction and separation method for co-producing pure praseodymium and pure gadolinium, wherein P507 is used as the extractant, 2N-3N grade gadolinium chloride is used as the first feed liquid, and 2N~3N grade praseodymium chloride is used as the second feed liquid; It consists of fractional extraction and separation of SmEuGd/GdTbDyHoY, fractional extraction and extraction of Pr/NdSm, fractional extraction and extraction of SmEu/Gd and fractional extraction and extraction of Gd/TbDyHoY. Two pure products, 4N-grade praseodymium chloride aqueous solution and 4N-grade gadolinium chloride aqueous solution, are obtained simultaneously in an extraction and separation process. The invention has the characteristics of low acid-base consumption, high stability, high product qualification rate, high green degree, short technological process, low production cost and the like.
priorityDate 2018-08-08-04:00^^<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: 34.