http://rdf.ncbi.nlm.nih.gov/pubchem/patent/CN-108950252-B

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classificationCPCAdditional http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/Y02P10-20
classificationCPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C22B3-3846
http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C22B59-00
classificationIPCInventive http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C22B59-00
http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C22B3-38
filingDate 2018-08-12-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 2020-07-28-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationDate 2020-07-28-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber CN-108950252-B
titleOfInvention A kind of separation method of fractional distillation extraction and co-production of pure samarium and pure terbium
abstract The present invention is a separation method for co-producing pure samarium and pure terbium by fractional distillation and extraction. P229 is used as the extractant, 2N-3N grade samarium chloride solution is the first feed liquid, and 1N grade terbium chloride solution is the second feed liquid PrNdSm/SmEuGd is separated by fractional extraction, SmEuGdTb/TbDyHoY is separated by fractional extraction, PrNd/Sm is separated by fractional extraction, Sm/EuGd is extracted by quasi-fractionation, Sm/EuGd/Tb is separated by three-outlet fractional extraction, and Tb/DyHoY is separated by fractional extraction. composition. One extraction and separation process of the present invention simultaneously obtains two pure products of 4N-level samarium chloride aqueous solution and 4N-level terbium chloride aqueous solution, and has the advantages of low acid-base consumption, good process stability, high product qualification rate, high degree of greening, and high production efficiency. Features such as low cost.
priorityDate 2018-08-12-04:00^^<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: 33.