Method for selectively recycling rhenium from high-arsenic waste acid system
A selective and systematic technology, applied in the direction of improving process efficiency, can solve the problems of poor selective extraction performance and low separation rate of rhenium and arsenic, and achieve the effect of low cost, simple process flow and good tolerance
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Embodiment 1
[0026] A method for selectively recovering rhenium from a high-arsenic waste acid system containing H + 0.38mol / L, As6.62g / L, Fe 39.08mg / L, Pb 17.22mg / L, Zn 271.75mg / L, Re 42.5ug / L, Cl - 1.97g / L, F - 0.1g / L,SO 4 2- 13.64g / L, including the following steps:
[0027] Use a mixed extractant to directly extract high-arsenic waste acid to obtain a rhenium-rich organic phase; the mixed extractant includes trioctylamine, N1923, isoamyl alcohol and sulfonated kerosene, the quality of trioctylamine, N1923, isoamyl alcohol and sulfonated kerosene The percentages are 10%, 4%, 18% and 68% respectively; during extraction, O / A=1:2, extraction time 10min, single-stage extraction, room temperature. It is determined that in this step, the extraction rate of rhenium is 99.2%, and the separation rate of rhenium and arsenic is 99.46%.
[0028] In this embodiment, the separation rate of rhenium and arsenic is (1-(the amount of arsenic in the collected rhenium material / the amount of arsenic in ...
Embodiment 2
[0030] Compared with Example 1, this example differs in that sodium hyposulfite is added to the high-arsenic waste acid before using the mixed extractant to extract the high-arsenic waste acid, and the amount of sodium hyposulfite added is 1.1 times the theoretical amount for reducing arsenic.
[0031] It is determined that in this step, the extraction rate of rhenium is 99.2%, and the separation rate of rhenium and arsenic is 99.78%.
Embodiment 3
[0033] A method for selectively recovering rhenium from a high-arsenic waste acid system containing H + 0.52mol / L, As6.25g / L, Fe 41.2mg / L, Pb 17.32mg / L, Zn 255.6mg / L, Re 287.1ug / L, Cl - 2.7g / L, F - 0.13g / L,SO 4 2- 16.64g / L, including the following steps:
[0034] Use a mixed extractant to directly extract high-arsenic waste acid to obtain a rhenium-rich organic phase; the mixed extractant includes trioctylamine, N1923, isoamyl alcohol and sulfonated kerosene, the quality of trioctylamine, N1923, isoamyl alcohol and sulfonated kerosene The percentages are 14%, 5%, 12% and 69% respectively; during extraction, O / A=1:2, extraction time 10min, three-stage extraction, normal temperature. It is determined that in this step, the extraction rate of rhenium is 99.61%, and the separation rate of rhenium and arsenic iron is 100%.
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