Collophanite obverse-reverse flotation collecting agent and preparation method thereof
A technology of reverse flotation and colloidal phosphate rock, applied in flotation, solid separation and other directions, can solve the problems of poor selectivity, low recovery rate of concentrate, high MgO content in concentrate, and achieve low beneficiation cost and high recovery rate of concentrate , The effect of low MgO content in concentrate
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Embodiment 1
[0010] Embodiment 1: Get the saturated higher fatty acid of the C12 of 100kg and the unsaturated higher fatty acid of the C18 of 900kg, saponify 6h with the KOH of 250kg after mixing to obtain the higher fatty acid potassium soap with fatty acid content higher than 40%. Get this higher fatty acid potassium soap 90kg, lauryl phosphate 10kg, after mixing, obtain basic substance; Add water 2000kg and stir to obtain collector.
[0011] Using this collector at a flotation temperature of 20°C 2 o 5 15.3%, MgO 5.2% raw ore was processed to get P 2 o 5 30.6%, MgO 1.5% concentrate, recovery rate 83.7%.
Embodiment 2
[0012] Embodiment 2: get the saturated higher fatty acid of the C14 of 130kg and the unsaturated higher fatty acid of the C18 of 870kg, after mixing, obtain the higher fatty acid potassium soap with fatty acid content higher than 40% with 250KOH saponification 6h; Get this higher fatty acid potassium soap 92kg, ten 8kg of dialkyl phosphates were mixed to obtain the basic substance; 5000kg of water was added and stirred to obtain the collector.
[0013] Using this collector at a flotation temperature of 20°C 2 o 5 15.3%, MgO 5.2% raw ore was processed to get P 2 o 5 30.4%, MgO 1.6% concentrate, recovery 82.9%.
Embodiment 3
[0014] Embodiment 3: get the saturated higher fatty acid of the C16 of 160kg and the unsaturated higher fatty acid of the C18 of 840kg, after mixing, obtain the higher fatty acid potassium soap with fatty acid content higher than 40% with 250kgKOH saponification 6h; Get this higher fatty acid potassium soap 94kg, ten 6kg of dialkyl phosphates were mixed to obtain basic substances; 8000kg of water was added and stirred to obtain collectors.
[0015] Using this collector at a flotation temperature of 20°C 2 o 5 15.3%, MgO 5.2% raw ore was processed to get P 2 o 5 30.8%, MgO 1.4% concentrate, recovery 82.5%.
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