Method for extraction and separation of tungsten and molybdenum from tungsten and molybdenum mixed solution
A mixed solution, tungsten and molybdenum technology, applied in the field of chemical extraction, can solve the problems of large loss of tungsten co-extraction, large amount of tungsten co-extraction, large water solubility, etc., to achieve less loss of organic phase, small loss of tungsten co-extraction, and environmental pollution small effect
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Embodiment 1
[0022] Organic phase composition (volume percentage): 3%TRPO+60%TBP+37%sulfonated kerosene, among which TRPO is a mixed trialkylphosphine oxide of Cynex923 provided by Cytec Corporation of Canada.
[0023] Aqueous phase material liquid: prepared molybdenum-containing sodium tungstate solution, pH 10.3, adjusted to pH 3.5 with nitric acid, added 30% H 2 o 2 aqueous solution, H 2 o 2 The amount of addition is 1.0 times of the total amount of moles of tungsten and molybdenum, and then the pH value is adjusted to 1.5 with nitric acid solution to obtain the extraction material liquid, wherein WO 3 140.5g / L, Mo 16.3g / L, Mo / WO 3 =0.116.
[0024] Extraction and separation: the above-mentioned organic phase and aqueous phase feed liquid are subjected to 8-stage countercurrent extraction under the condition of ratio 2 / 1, and the loaded organic phase is subjected to single-stage back extraction under the condition of ratio 1 / 1 with 0.1mol / L NaOH aqueous solution , after stripping, ...
Embodiment 2
[0027] Organic phase composition (volume percentage): 1%TRPO+40%TBP+59% aviation kerosene, wherein TRPO is a mixed trialkylphosphine oxide Cynex923 provided by Cytec Company.
[0028] Aqueous phase material liquid: an industrial actual molybdenum-containing ammonium tungstate solution produced by a company using an ion exchange process, the pH value is 9.5, the pH value is adjusted to 3.5 with hydrochloric acid, and 30% H is added to it 2 o 2 ,H 2 o 2 The addition amount is 1.5 times of the sum of the moles of tungsten and molybdenum, mix evenly, and then adjust the pH value to 2.5 with ammonia solution to obtain the extraction water phase complexing material liquid, wherein WO 3 180.2g / L, Mo 3.60g / L, Mo / WO 3 =0.020.
[0029] Extraction and separation: the organic phase and the aqueous phase feed liquid are subjected to 3-stage countercurrent extraction under the condition of a ratio of 4 / 3, and the loaded organic phase is subjected to single-stage stripping under the con...
Embodiment 3
[0032] Organic phase composition (volume percentage): 5%TRPO+80%TBP+15%sulfonated kerosene, wherein TRPO is a mixed trialkylphosphine oxide Cynex923 provided by Cytec Company.
[0033] Aqueous phase material liquid: an industrial actual molybdenum-containing ammonium tungstate solution produced by a company using a quaternary ammonium salt alkaline medium extraction process, with a pH value of 9.5, adjusted to pH 3.0 with sulfuric acid, and adding 30% H 2 o 2 ,H 2 o 2 The addition amount is 1.8 times of the sum of moles of tungsten and molybdenum, the pH value is 1.30, and then the pH value is adjusted to 1.8 with ammonia solution to obtain the extraction material liquid, wherein WO 3 140.2g / L, Mo17.5g / L, Mo / WO 3 =0.125.
[0034] Extraction and separation: the above-mentioned organic phase and the aqueous phase feed liquid are subjected to 15-stage countercurrent extraction under the condition of a ratio of 3 / 2, and the loaded organic phase is subjected to a 3-stage under...
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