Recycling and harmless treatment method for cyaniding tailing slurry
A technology for harmless treatment and cyanidation of tailings, applied in chemical instruments and methods, mining wastewater treatment, neutralized water/sewage treatment, etc. Surface water and other problems, to achieve the effect of speeding up the oxidation-reduction reaction speed, speeding up the acidification stripping speed, and speeding up the reaction rate
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Embodiment 1
[0049] Embodiment 1: small batch test:
[0050] Take 2L cyanide tailings slurry, add hydrogen peroxide 17ml / L, the pH value is below 2, the reaction time is 2.5h, add the same amount of concentrated H at a constant temperature of 40°C with different gas-liquid ratios 2 SO 4 Carry out conversion and stripping, and absorb HCN with an absorption column equipped with 3L NaOH solution. After the lime is neutralized to a pH of 7, 2.5ml / L hydrogen peroxide is added to remove cyanide. The test results are shown in Table 1:
[0051] Table 1: Small-scale test results of recycling and harmless batch treatment of cyanide tailings slurry
[0052]
Embodiment 2
[0053] Example 2: Small continuous experiment:
[0054] According to the technical conditions obtained from the batch test, determine the following continuous test conditions:
[0055] (1), the processing capacity of tailings slurry: 2L / h;
[0056] (2), gas-liquid ratio: 400:1;
[0057] (3), temperature control: 40 ℃;
[0058] (4), agent flow rate: convert and blow off hydrogen peroxide 30ml / L, H 2 SO 4 6ml / L, CaO6g / L, cyanide removal hydrogen peroxide 2.5ml / L;
[0059] (5) Absorption solution: 15% NaOH 4L.
[0060] The test results are shown in Table 2:
[0061] Table 2: Small-scale continuous test results of cyanide tailings slurry recycling and harmless treatment
[0062]
Embodiment 3
[0063] Embodiment 3: Pilot scale continuous treatment experiment:
[0064] This test adopts the 5 steps introduced by the present invention, the tailings slurry processing capacity is 50L / h, the hydrogen peroxide addition is 20mL / h, the sulfuric acid addition is 6mL / h, the slurry residence time is 1.5h, and the gas-liquid ratio is 300 : 1, the acidizing oxidation temperature is 40 ℃, carries out two experiments, each 8 hours, handles 840L of ore pulp altogether, and experimental result sees the following table 3:
[0065] Table 3: Small-scale continuous test results of cyanide tailings slurry recycling and harmless treatment
[0066]
[0067] Cumulative recovery of CN in the absorption solution - The amount is 469.8g; Theoretical SCN - Convert CN - The amount is 519.7g; the actual SCN - The conversion recovery rate was 90.14%. The experimental results are shown in Table 4:
[0068] Table 4: Results of continuous pilot test of cyanide tailings slurry recycling and harm...
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