Method for preparing refractory material for cement kiln from calcium-magnesium phosphate rock tailings
A technology of phosphate rock tailings and refractory materials, applied in the field of refractory materials, can solve the problems of less than 10% comprehensive utilization rate of phosphate tailings, environmental and human health hazards, etc., and achieve the optimization and improvement of hydration resistance and spalling resistance The effect of added value
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Embodiment 1
[0019] The magnesium-calcium phosphate ore tailings are washed, separated, de-medicated, deslimed and then dried, and then the calcium-magnesium components with a certain purity are obtained through the magnesium flotation process of one coarse, one fine and one sweep.
[0020] Table 1 XRF analysis results of calcium-magnesium phosphate mine tailings
[0021]
[0022] In the process of magnesium flotation with one coarse, one fine and one sweep, magnesium roughing agent system: sulfuric acid 6000g / t, collector TG 1500g / t; magnesium selection agent system: collector TG 500g / t; magnesium sweeping agent system : Sulfuric acid 1000g / t, collector TG 500g / t. Phosphorus rough sorting agent system: sodium carbonate 8000g / t, collector TP 2000g / t; phosphorus sweeping agent system: sodium carbonate 1000g / t. The yield of calcium and magnesium components was 72%, the grade of MgO was 19%, and the grade of CaO was 35%.
[0023] Table 2 Chemical multi-element analysis of calcium and mag...
Embodiment 2
[0033] The magnesium-calcium phosphate ore tailings (physical and chemical properties are the same as in Example 1) are dried after washing, separation, drug removal, desliming, etc.; Calcium and magnesium components.
[0034] Among them, magnesium roughing agent system: sulfuric acid 7000g / t, collector TG 2000g / t; magnesium selection agent system: collector TG 800g / t; magnesium sweeping agent system: sulfuric acid 800g / t, collector TG 600g / t. Phosphorus rough sorting agent system: sodium carbonate 10000g / t, collector TP 2500g / t; phosphorus sweeping agent system: sodium carbonate 1000g / t. The yield of calcium and magnesium components was 60%, the grade of MgO was 22.3%, and the grade of CaO was 36.61%.
[0035] Table 5 Chemical multi-element analysis of calcium and magnesium components after flotation treatment
[0036]
[0037] The calcium and magnesium components obtained above are calcined at 900 ° C for 1 h, and the heating rate is 25 ° C / min, and further purificati...
Embodiment 3
[0043]The magnesium-calcium phosphate ore tailings (physical and chemical properties are the same as in Example 1) are dried after washing, separation, drug removal, desliming, etc.; Calcium and magnesium components.
[0044] Among them, magnesium roughing agent system: sulfuric acid 7500g / t, collector TG 2200g / t; magnesium selection agent system: collector TG1000 g / t; magnesium sweeping agent system: sulfuric acid 900g / t, collector TG 500g / t. Phosphorus rough sorting agent system: sodium carbonate 12000g / t, collector TP 2800g / t; phosphorus sweeping agent system: sodium carbonate 800g / t. The yield of calcium and magnesium components was 63%, the grade of MgO was 23.76%, and the grade of CaO was 37.07%.
[0045] Table 7 Chemical multi-element analysis of calcium and magnesium components after flotation treatment
[0046]
[0047] The calcium and magnesium components obtained above are calcined at 950° C. for 1 h, and the heating rate is 20° C. / min, and further purificati...
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