Beneficiation method for collophanite
A beneficiation method and a technology for colloidal phosphate rock, which are used in flotation, solid separation, energy and wastewater treatment, etc., and can solve the problem that it is difficult to meet the index requirements of high-quality phosphorus concentrates, cannot effectively reduce the content of sesquioxide, and is difficult to achieve high-quality phosphate concentrates. Chemical utilization and other issues to achieve the effect of improving quality
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Embodiment 1
[0086] Preparation of medicament A: Mix butylammonium black, ether alcohol and kerosene in a mass ratio of 2:1:1, add water, and stir at 3000 r / min for 30 minutes to obtain an aqueous solution with a mass concentration of 2%, namely medicament A.
[0087] Preparation of sulfuric acid solution: mix H 2 SO 4 Mix with water at 2:8, stir evenly to get H 2 SO 4 A sulfuric acid solution with a mass concentration of 20%.
[0088] Preparation of agent B: mix oxidized paraffin soap with H 2 SO 4 , prepared into a solution with a mass concentration of 20%, heated to 100°C, stirred at a high speed of 3000r / min for 30min, concentrated and evaporated to dryness to obtain a paste. Water is added to the obtained paste to prepare an aqueous solution with a mass concentration of 5%, namely agent B.
Embodiment 2
[0090] 1.1 Colloidal raw ore
[0091] The chemical composition of collophosite raw ore samples includes: P 2 o 5 19.53%, MgO 5.64%, SiO 2 13.20%, CaO36.63%, Fe 2 o 3 1.46%, K 2 O 0.34%, Na 2 O 0.04%, F 1.42%, Al 2 o 3 0.90%, Loss 7.37%, CO 2 7.02%; sample particle size is -2mm.
[0092] The ore belongs to silicon-magnesia phosphate rock, with severe mudification and darker color. Among them, magnesium mainly exists in the form of dolomite, silicon mainly exists in the form of quartz, and sesquioxide mainly exists in the form of iron with a relatively high content. Under the microscope, iron mainly exists in the form of pyrite.
[0093] 1.2 Mineral dressing process
[0094] according to figure 1 The beneficiation process shown is carried out, figure 1 It is the flow chart of the ore dressing process in Example 2 of the present invention; wherein, 2' refers to stirring for 2 minutes after adding the corresponding agent, similarly, 5' refers to stirring for 5 min...
Embodiment 3
[0110] 1.1 Colloid ore: Same as Example 2.
[0111] 1.2 Mineral dressing process
[0112] Carry out according to the beneficiation flow process of embodiment 2, difference is, the dosage of agent of individual link is adjusted to some extent, and concrete process is as follows:
[0113] S1, with embodiment 2.
[0114] S2. Rough selection 1: Carry out according to Example 2, the difference is that the dosage of agent A is adjusted to 120g / t raw ore.
[0115] S3, rough selection two: carry out according to embodiment 2, the difference is that H 2 SO 4 The dosage is adjusted to 24Kg / t raw ore, and the dosage of agent B is adjusted to 500g / t raw ore.
[0116] S4, selection one: carry out according to embodiment 2, the difference is that H 2 SO 4 The dosage is adjusted to 2Kg / t raw ore, and the dosage of agent B is adjusted to 150g / t raw ore.
[0117] S5. Selection 2: Carry out according to Example 2, the difference is that the dosage of agent B is adjusted to 300g / t raw ore...
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