Dense solid-liquid separation method in wet zinc smelting solution capable of improving clarification effect
A technology of hydrometallurgy and solid separation, applied in the direction of improving process efficiency, etc., can solve problems such as difficulty in production control, deterioration of supernatant liquid quality, and small production capacity of supernatant liquid, so as to reduce soluble silicon and iron content, increase the effect of dense clarification, and the effect of clear supernatant
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Embodiment 1
[0016] A method for providing a clarification effect in dense liquid-solid separation in a zinc hydrometallurgy solution, comprising the steps of:
[0017] Step 1: Quality control of zinc calcine: control the particle size of zinc calcine to be -160 to -200 mesh during the roasting process, accounting for 70% of the total mass of zinc calcine, and the particle size of zinc calcine to be -140 to -160 mesh to account for zinc calcine 20% of the total mass; the particle size of the zinc calcine is +100~-120 meshes, accounting for 10% of the total mass of the zinc calcine; controlling Si in the zinc calcine 可溶 The mass percentage of Fe is less than 2.5%, and the mass percentage of Fe is less than 6%;
[0018] Step 2: Intermediate leaching process control: control the acidity of the intermediate leaching mother liquor to 50g / l, the flow rate of the intermediate leaching oxidation solution to 180m? / h, and the flow rate of the intermediate leaching calcine to 15t / h when adding zinc...
Embodiment 2
[0023] A method for providing a clarification effect in dense liquid-solid separation in a zinc hydrometallurgy solution, comprising the steps of:
[0024] Step 1: Quality control of zinc calcine: control the particle size of zinc calcine to be -160 to -200 mesh during the roasting process, accounting for 70% of the total mass of zinc calcine, and the particle size of zinc calcine to be -140 to -160 mesh to account for zinc calcine 20% of the total mass; the particle size of the zinc calcine is +100~-120 meshes, accounting for 10% of the total mass of the zinc calcine; controlling Si in the zinc calcine 可溶 The mass percentage of Fe is less than 2.5%, and the mass percentage of Fe is less than 6%;
[0025] Step 2: Intermediate leaching process control: control the acidity of the intermediate leaching mother liquor to 50g / l, the flow rate of the intermediate leaching oxidation solution to 180m? / h, and the flow rate of the intermediate leaching calcine to 15t / h when adding zinc ...
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