PHOSPHATE RARE-EARTH CONCENTRATE PROCESSING METHOD

FIELD: chemistry. ^ SUBSTANCE: invention can be used in chemistry and metallurgy. Phosphate rare-earth concentrate processed with nitric acid is heated with oxalic acid in plenty. Rare-earth elements (REE) oxalate deposition is separated from mother liquor containing residual quantity of oxalic acid...

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Hauptverfasser: LOKSHIN EHFROIM PINKHUSOVICH, LEBEDEV VALERIJ NIKOLAEVICH, MASLOBOEV VLADIMIR ALEKSEEVICH
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creator LOKSHIN EHFROIM PINKHUSOVICH
LEBEDEV VALERIJ NIKOLAEVICH
MASLOBOEV VLADIMIR ALEKSEEVICH
description FIELD: chemistry. ^ SUBSTANCE: invention can be used in chemistry and metallurgy. Phosphate rare-earth concentrate processed with nitric acid is heated with oxalic acid in plenty. Rare-earth elements (REE) oxalate deposition is separated from mother liquor containing residual quantity of oxalic acid, washed and treated with potash alkali in plenty 5-50% surplus in stoichiometry ratio per oxalate-ions so that potassium oxalate solution and REE hydroxide depositions are formed. After REE hydroxide depositions are separated, potassium oxalate solution is delivered back to phosphate concentrate processing stage. REE hydroxide depositions are exposed to heat treatment at 100-150°C to produce collective concentrate of REE hydroxides, or at 250-500°C to oxidise cerium to cerium (IV). Then deposition is pulped in water at ":"=1:4-8 and processed with nitric acid consumed as 0.6-0.8 wt fractions of 100% HNO3 per 1 wt fraction of REE oxides with REE transfer, except for Ce (IV), to solution. Cerium-containing deposition is separated. Potassium oxalate solution is concentrated with oxalic acid in residual quantity contained in mother liquor, and treated with neutral extractant, principally with tributylphosphate or triisoamylphosphate. Oxalic acid in residual quantity is transferred to extract, re-extracted with potassium oxalate solution. Oxalic acid consumption and thermal processing power inputs are reduced. Selective cerium separation from total REE is provided. Produced cerium concentrate contains CeO2 96.5-97.8 wt %. ^ EFFECT: reduced oxalic acid consumption and thermal processing power inputs, provided selective cerium separation from total rare-earth elements. ^ 2 cl, 5 ex
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Phosphate rare-earth concentrate processed with nitric acid is heated with oxalic acid in plenty. Rare-earth elements (REE) oxalate deposition is separated from mother liquor containing residual quantity of oxalic acid, washed and treated with potash alkali in plenty 5-50% surplus in stoichiometry ratio per oxalate-ions so that potassium oxalate solution and REE hydroxide depositions are formed. After REE hydroxide depositions are separated, potassium oxalate solution is delivered back to phosphate concentrate processing stage. REE hydroxide depositions are exposed to heat treatment at 100-150°C to produce collective concentrate of REE hydroxides, or at 250-500°C to oxidise cerium to cerium (IV). Then deposition is pulped in water at ":"=1:4-8 and processed with nitric acid consumed as 0.6-0.8 wt fractions of 100% HNO3 per 1 wt fraction of REE oxides with REE transfer, except for Ce (IV), to solution. Cerium-containing deposition is separated. Potassium oxalate solution is concentrated with oxalic acid in residual quantity contained in mother liquor, and treated with neutral extractant, principally with tributylphosphate or triisoamylphosphate. Oxalic acid in residual quantity is transferred to extract, re-extracted with potassium oxalate solution. Oxalic acid consumption and thermal processing power inputs are reduced. Selective cerium separation from total REE is provided. 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Phosphate rare-earth concentrate processed with nitric acid is heated with oxalic acid in plenty. Rare-earth elements (REE) oxalate deposition is separated from mother liquor containing residual quantity of oxalic acid, washed and treated with potash alkali in plenty 5-50% surplus in stoichiometry ratio per oxalate-ions so that potassium oxalate solution and REE hydroxide depositions are formed. After REE hydroxide depositions are separated, potassium oxalate solution is delivered back to phosphate concentrate processing stage. REE hydroxide depositions are exposed to heat treatment at 100-150°C to produce collective concentrate of REE hydroxides, or at 250-500°C to oxidise cerium to cerium (IV). Then deposition is pulped in water at ":"=1:4-8 and processed with nitric acid consumed as 0.6-0.8 wt fractions of 100% HNO3 per 1 wt fraction of REE oxides with REE transfer, except for Ce (IV), to solution. Cerium-containing deposition is separated. Potassium oxalate solution is concentrated with oxalic acid in residual quantity contained in mother liquor, and treated with neutral extractant, principally with tributylphosphate or triisoamylphosphate. Oxalic acid in residual quantity is transferred to extract, re-extracted with potassium oxalate solution. Oxalic acid consumption and thermal processing power inputs are reduced. Selective cerium separation from total REE is provided. Produced cerium concentrate contains CeO2 96.5-97.8 wt %. ^ EFFECT: reduced oxalic acid consumption and thermal processing power inputs, provided selective cerium separation from total rare-earth elements. ^ 2 cl, 5 ex</abstract><oa>free_for_read</oa></addata></record>
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subjects CHEMISTRY
CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION ORPROCESSING OF GOODS
COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM,CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THERARE-EARTH METALS
FERROUS OR NON-FERROUS ALLOYS
GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS
INORGANIC CHEMISTRY
METALLURGY
PRETREATMENT OF RAW MATERIALS
PRODUCTION AND REFINING OF METALS
TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINSTCLIMATE CHANGE
TREATMENT OF ALLOYS OR NON-FERROUS METALS
title PHOSPHATE RARE-EARTH CONCENTRATE PROCESSING METHOD
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