Oolitic hematite dressing method
A technology of oolitic hematite and ore beneficiation methods, applied in chemical instruments and methods, wet separation, solid separation, etc., can solve problems such as difficult engineering, prolonged production cycle, increased energy consumption, etc., and achieve improved dispersion effect , Dispersion efficiency improvement, and the effect of inhibiting particle agglomeration
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Embodiment 1
[0026] 1. The source of raw ore: an acidic high-phosphorus oolitic hematite ore in Hubei, with a TFe content of 40.18wt%, a P content of 1.17wt%, and a SiO 2 The content is 24.25wt%;
[0027] 2. Weigh 500g of raw ore and grind it to -0.074mm (that is, the particle size is less than 0.074mm) to account for 88wt% of the total weight of the raw ore. During the grinding process, add the slime dispersant hexabias at the ratio of 60g dispersant / ton of raw ore Sodium phosphate is co-milled with raw ore; at this time, the dispersion efficiency of mineral particles is 90%;
[0028] 3. Take the material obtained from the grinding, add water to adjust the slurry, the mass fraction of the slurry is 30%, and stir for 5 minutes after the slurry; then carry out gravity separation and desliming in the spiral chute to obtain mud-grade products and non-sludge-grade products; mud-grade products are dry Accounting for 20% of the total weight of raw ore;
[0029] 4. Using SLON-500 vertical ring ...
Embodiment 2
[0035] Ore source: an oolitic hematite ore in Ningxiang, Hunan Province, the original ore TFe content is 42.74wt%, P content is 1.50wt%, SiO 2 The content is 20.38wt%;
[0036] 9. The operation procedure of this embodiment is the same as that of Example 1, the difference is that the mineral weight of the ore ground to a particle size of -0.074mm accounts for 82% of the weight of the raw ore, and the amount of dispersant added during ore grinding is 100g / ton of raw ore. Post-pulling, at this time, the dispersion efficiency of mineral particles is 92%, the mass fraction of the obtained pulp is 25%, and the dry weight of the mud-grade product obtained after desliming accounts for 22% of the total weight of the original ore; the iron-containing mineral inhibitor is dextrin, and the deslimed The collector for phosphorus dephosphorization is oxidized paraffin soap, and the collector for desiliconization is dodecyltrimethylammonium bromide; In the reverse flotation desiliconization ...
Embodiment 3
[0038] Ore source: an oolitic hematite ore in the north, the original ore TFe content is 46.35wt%, P content is 1.10wt%, SiO 2 The content is 19.25wt%.
[0039] The operation procedure of this embodiment is the same as that of Example 1, the difference is that the mineral weight of the ore ground to a particle size of -0.074mm accounts for 87% of the total raw ore weight, and the amount of dispersant added during ore grinding is 150g / ton of raw ore. Slurry; at this time, the dispersion efficiency of mineral particles is 95%, the mass fraction of the obtained pulp is 15%, and the dry weight of the mud grade product obtained after desliming accounts for 19% of the total weight of the original ore; the iron-containing mineral inhibitor is sulfonated lignin, The dephosphorization collector is sodium oleate, and the desiliconization collector is a compound composed of hexadecylamine and dodecyl dimethyl benzyl ammonium chloride in a weight ratio of 1:1; reverse flotation dephosphor...
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