Ultrafine lead oxide prepared by using waste lead plaster and preparation method thereof
A technology of waste lead paste and lead oxide, applied in the direction of lead oxide, recycling technology, regeneration of useful parts, etc., can solve the problems of inconvenient treatment by fire method and wet method, and achieve good resource recovery effect and low lead-free volatilization , the effect of convenient recycling
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Embodiment 1
[0045] (1) The pretreatment before desulfurization is as follows: the lead paste pretreatment before desulfurization is to take out the lead paste of the waste lead-acid battery, wash it to neutral drying, and grind it into waste lead paste powder with a particle size of more than 100 meshes, wherein sulfuric acid The lead content is 64.5%.
[0046] (2) Preparation of the ultrafine lead oxide (PbO / Pb)
[0047] 2.1 Desulfurization conversion
[0048] Add 100g of waste lead plaster to a total of 55g of sodium carbonate and sodium bicarbonate in a composite desulfurization solution in which the molar ratio of sodium carbonate to sodium bicarbonate is 1:2 (wherein the molar ratio of S in the waste lead plaster:Na in the desulfurizer is 1:4) , the solid-to-liquid ratio of the desulfurization solution is 1:10, and the mixed solution is obtained by reacting at 35°C for 2 hours; the desulfurization rate of waste lead plaster is above 98.5%. Obtain desulfurization lead paste, the XRD...
Embodiment 2
[0061] Difference with embodiment 1 is: sodium carbonate and sodium bicarbonate mol ratio are 1: 3, and desulfurization time is 3h, finally obtains light yellow lead powder (PbO / Pb) product, raw material utilization rate 98.3%, the lead citrate Yield 97.5%. Others are the same as in Example 1, and the main process parameters are shown in Table 1.
Embodiment 3
[0063] The difference from Example 1 is that the molar ratio of lead in the desulfurized lead paste to citric acid in the citric acid leaching step is 1:3, the utilization rate of raw materials is 98.5%, and the yield of lead citrate is 97.8%. Others are the same as in Example 1, and the main process parameters are shown in Table 1.
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