Nonferrous metallurgy arsenic-containing impure acid harmless disposal method
A disposal method and technology of arsenic polluted acid, applied in chemical instruments and methods, water/sewage treatment, neutralized water/sewage treatment, etc., to achieve the effect of low cost of treating polluted acid
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Embodiment 1
[0021] Embodiment 1: The harmless disposal method of the non-ferrous smelting arsenic-containing sewage acid is as follows:
[0022] (1) The laterite nickel ore (composition shown in Table 1) is subjected to dry ball milling and magnetic separation (the speed of the ball mill is 740r / min, the grinding time is 11min, and the magnetic separation intensity of the magnetic separator is 700mT) to obtain iron-rich nickel ore and other impurities, and other impurities are piled up for treatment;
[0023] Table 1
[0024]
[0025] (2) According to the ratio of iron:arsenic molar ratio of 2.5:1, according to H 2 o 2 : The molar ratio of arsenic is 1:1, and the iron-rich nickel ore, polluted acid and H 2 o 2 The solution was uniformly mixed, and the arsenic precipitation reaction was carried out at 70°C and 180r / min stirring conditions for 10 hours to obtain a solid-liquid mixture A, which was separated to obtain arsenic-containing solid A and filtrate A; the dirty acid came from...
Embodiment 2
[0032] Embodiment 2: The harmless disposal method of the non-ferrous smelting arsenic-containing sewage acid is as follows:
[0033] (1) The laterite nickel ore (composition shown in Table 4) is subjected to dry ball milling and magnetic separation (the speed of the ball mill is 860r / min, the grinding time is 9min, and the magnetic separation intensity of the magnetic separator is 900mT) to obtain iron-rich nickel ore and other impurities, and other impurities are piled up for treatment;
[0034] Table 4
[0035]
[0036] (2) According to the ratio of iron:arsenic molar ratio of 3:1, according to H 2 o 2 : The molar ratio of arsenic is 1.2:1, and the iron-rich nickel ore, polluted acid and H 2 o 2 The solution was uniformly mixed, and the arsenic precipitation reaction was carried out under the condition of 80°C and 200r / min stirring for 11 hours to obtain a solid-liquid mixture A, and the solid-liquid separation obtained arsenic-containing solid A and filtrate A; the p...
Embodiment 3
[0043] Embodiment 3: The harmless disposal method of the non-ferrous smelting arsenic-containing sewage acid is as follows:
[0044] (1) Dry the laterite nickel ore (the composition is shown in Table 7) to dry ball mill magnetic separation (the speed of the ball mill is 900r / min, the grinding time is 7min, and the magnetic separation intensity of the magnetic separator is 1000mT) to obtain iron-rich nickel ore and other impurities, and other impurities are piled up for treatment;
[0045] Table 7
[0046]
[0047] (2) According to the ratio of iron:arsenic molar ratio of 3.5:1, according to H 2 o 2 : The molar ratio of arsenic is 1.6:1, and the iron-rich nickel ore, polluted acid and H 2 o 2 The solution was uniformly mixed, and the arsenic precipitation reaction was carried out under the condition of 80°C and 220r / min stirring for 12 hours to obtain a solid-liquid mixture A, and the solid-liquid separation obtained arsenic-containing solid A and filtrate A; the pollute...
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