Processing method for fine-grained disseminated rutile ore difficult to separate
A rutile ore and processing method technology, applied in chemical instruments and methods, wet separation, magnetic separation, etc., can solve the problem of increasing the magnetic difference between rutile and iron minerals, difficult to effectively separate, and reducing the separation effect and utilization of rutile. Value and other issues, to achieve the effect of reducing operating costs, reducing impact, and increasing added value
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Embodiment 1
[0020] SiO in the used rutile ore of the present invention 2 Content 52.46%, Fe 2 O 3 content 24.93 %, TiO 2 content 5.60 %, Al 2 o 3 Content 11.19%, V 2 o 5 The content of MgO is 0.9%, the content of MgO is 0.59%, and the content of CaO is 0.11%. The results of rock ore identification show that the minerals contained in rutile mainly include: muscovite, quartz, rutile, hematite, pyrrhotite, pyroxene, clay ore, and rutile -0.074mm is still related to quartz, hematite Wait for Liansheng. attached by figure 2 , 3 , 4. It can be seen that most rutiles are associated with other ores such as hematite, and the embedded particle size is relatively fine.
[0021] first step:
[0022] After grinding operation I, the overflow fineness of the grading equipment is -0.074mm, accounting for 65%. The overflow of the grading equipment is fed into the shaking table, and the ore in the shaking table is used as the final tailings, the shaker concentrate and the shaker slime A...
Embodiment 2
[0032]The rutile ore used is the rutile ore in Example 1.
[0033] first step:
[0034] After grinding operation I, the overflow fineness of the grading equipment is -0.074mm, accounting for 70%. The overflow of the grading equipment is fed into the shaking table, and the ore in the shaking table is used as the final tailings, the shaker concentrate and the shaker slime After the three-stage dehydration operation of concentration, filtration and drying, the dehydrated product is subjected to fluidized bed tubular roasting, and the roasted product is subjected to forced stirring and water quenching.
[0035] After the three-stage dehydration operation, the water content of the product is 0, and water gas is fed into the fluidized bed tubular roasting. The hydrogen content in the water gas is 40%, and the hydrogen content in the water gas is 40%. 3 / h, the calcination temperature is 680°C, and the calcination time is 8min.
[0036] Step two:
[0037] Classified grinding opera...
Embodiment 3
[0044] The rutile ore used is the rutile ore in Example 1.
[0045] first step:
[0046] After grinding operation I, the overflow fineness of the grading equipment is -0.074mm, accounting for 68%. The overflow of the grading equipment is fed into the shaking table, and the ore in the shaking table is used as the final tailings, the shaker concentrate and the shaker slime After the three-stage dehydration operation of concentration, filtration and drying, the dehydrated product is subjected to fluidized bed tubular roasting, and the roasted product is subjected to forced stirring and water quenching.
[0047] After the three-stage dehydration operation, the water content of the product is 1%. Water gas is fed into the fluidized bed tubular roasting. The hydrogen content in the water gas is 35%, and the hydrogen content in the water gas is 35%. 3 / h, the calcination temperature is 600°C, and the calcination time is 9min.
[0048] Step two:
[0049] Classified grinding operati...
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