Method for recovering rhenium from arsenic sulfide pressurization leach liquor
A pressure leaching and arsenic sulfide technology, applied in the field of hydrometallurgy, can solve the problems of low regeneration times, limited resin exchange capacity, and restrictions on large-scale industrial application, and achieve the effect of convenient storage and transportation and high rhenium recovery rate
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[0015] Example 1
[0016] The rhenium-arsenic filter cake treated in this example comes from a domestic copper smelting enterprise, and its main chemical components are (%): As12.14-13.45, Sb 0.065-0.078, Bi 1.23-1.54, Au 2.98-3.21 (g / t), Ag 43.16~45.18(g / t), Cu8.77~9.37, Pb 3.99~4.03, Zn 0.67~0.84, S 5.13~6.43, Re 0.09~0.11, Se 0.34~0.41, Te0.0032~0.0034 , In 0.0078~0.0089, Fe 0.19~0.25, Sn 0.29~0.35, the rest are impurities.
[0017] Put 200g of rhenium-containing arsenic filter cake into a GAS type 2L vertical autoclave, add additives, acid, water, etc. and mix them in a certain proportion into the axe, seal, stir, and heat up. When the temperature rises to the set value (100°C), the oxygen partial pressure was adjusted to the set value (0.4Mpa) by oxygen, and the timing was started. After 3 hours of reaction, the cooling water was passed to cool down, the valve was opened to reduce pressure, the material was separated from solid and liquid, and the leaching residue was ...
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[0019] Example 2
[0020] The rhenium-arsenic filter cake treated in this example comes from a domestic copper smelting enterprise, and its main chemical components are (%): As12.14-13.45, Sb 0.065-0.078, Bi 1.23-1.54, Au 2.98-3.21 (g / t), Ag 43.16~45.18(g / t), Cu8.77~9.37, Pb 3.99~4.03, Zn 0.67~0.84, S 5.13~6.43, Re 0.09~0.11, Se 0.34~0.41, Te0.0032~0.0034 , In 0.0078~0.0089, Fe 0.19~0.25, Sn 0.29~0.35, the rest are impurities.
[0021] Put 100g of rhenium-containing arsenic filter cake into a GAS type 2L vertical autoclave, add additives, acid, water, etc. and mix them in a certain proportion into the axe, seal, stir, and heat up. When the temperature rises to the set value (60°C), the oxygen partial pressure was adjusted to the set value (0.8Mpa) by oxygen, and the timing was started. After 2 hours of reaction, the cooling water was passed through to cool down, and the valve was opened to reduce pressure. After the material was separated from solid and liquid, the leaching...
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