Anionic collector for normal temperature flotation of hematite and preparation method thereof
A technology of anion collector and hematite, which is applied in the field of anion collector and its preparation of hematite flotation at room temperature, can solve the problem of high energy consumption and failure to reach the iron grade of 66-68% in ironworks, etc. problems, to achieve the effect of reducing energy consumption, significant economic benefits, and huge social benefits
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Embodiment 1
[0023] Raw material components:
[0024] Waste oil fatty acid 70.0 kilograms, naphthenic acid 12.5 kilograms, cocoyl ether sulfosuccinate disodium salt 15.5 kilograms, N-lauroyl ethylenediamine triacetate sodium 2.0 kilograms, sodium hydroxide 16.5 kilograms.
[0025] Preparation:
[0026] First, add waste oil fatty acid and naphthenic acid into the saponification kettle, add sodium hydroxide, and stir for 40-45 minutes at a temperature of 85-95° C. to carry out high-temperature saponification,
[0027] Secondly, after the temperature drops to 30-40°C, saponify for 5-10 minutes, add N-lauroyl ethylenediamine triacetate sodium and disodium cocoyl ether sulfosuccinate, stir for 5-10 minutes to ripen, namely have to.
[0028] See Table 1 for comparison with the flotation operation index of the RA-715 collector currently used in the concentrator.
[0029] Table 1
[0030]
[0031] Flotation feed - 200 grain content, %
Embodiment 2
[0033] Raw material components:
[0034] 32.5 kilograms of waste oil fatty acid, 50.0 kilograms of naphthenic acid, 10.0 kilograms of cocoyl ether sulfosuccinate disodium salt, 7.5 kilograms of sodium N-lauroyl ethylenediamine triacetate, and 16.5 kilograms of sodium hydroxide.
[0035] The preparation method is the same as in Example 1.
[0036] The flotation operation index comparison of embodiment 2 and the RA-715 collector currently used in the concentrator is shown in Table 2:
[0037] Table 2
[0038]
Embodiment 3
[0040] Raw material components:
[0041] Waste oil fatty acid 67.0 kilograms, naphthenic acid 8.0 kilograms, cocoyl ether sulfosuccinate disodium salt 22.5 kilograms, N-lauroyl ethylenediamine triacetate sodium 2.5 kilograms, sodium hydroxide 15.0 kilograms.
[0042] The preparation method is the same as in Example 1.
[0043] Under the condition of pulp temperature of 23-25 ℃, the flotation feeding ore with a separation grade of 48.24% and a -200 mesh size content of 84.2%, the indicators are: flotation concentrate grade 68.35%, flotation tailings grade 13.75%, flotation The job recovery rate is 89.50%.
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