A kind of method of lead sulfate slag wet cleaning treatment
A clean treatment and lead sulfate technology, which is applied to the improvement of process efficiency, instruments, electrolytic components, etc., can solve the problems of difficulty in maintaining the heat balance of the lead smelting system, the high cost of smelting flue gas treatment, and the high energy consumption of lead sulfate slag. The effect of high recovery rate of valence elements, strong adaptability of raw materials and high cost
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Embodiment 1
[0073] The lead sulfate slag provided by a company in Hunan was analyzed as PbSO 4 The lead content in the physical phase is 26.8% (mass percentage).
[0074] Get this lead sulfate slag 200g, with CaCl 2 with NH 4 The mixed solution of Cl is used as the coordination leaching agent to carry out the chlorination coordination leaching reaction on the lead sulfate slag. Among them, CaCl 2 The amount added is 1.5 times the theoretical amount required to form all the sulfate radicals in the lead sulfate slag into calcium sulfate, and the NH 4 Cl and CaCl 2 The molar ratio is 1.5:1. The chlorination coordination leaching temperature is 85°C, the solid (g) to liquid (ml) ratio is 1:4, and the leaching time is 90 minutes; immediately after the chlorination coordination leaching is completed, the leaching system is filtered and separated while it is hot, and lead-containing chloride is obtained. Coordinate the leaching solution and leaching slag, analyze the lead content in the le...
Embodiment 2
[0076] The lead sulfate slag provided by a company in Guangxi was analyzed as PbSO 4 The lead content in the physical phase is 23.9% (mass percentage).
[0077] Get this lead sulfate slag 2000g, with BaCl 2 The mixed solution with NaCl is used as a coordination leaching agent to carry out chlorination coordination leaching reaction on the lead sulfate slag. Among them, BaCl 2 The amount added is 3 times of the theoretical amount needed to form all the sulfate radicals in the lead sulfate slag into barium sulfate, and NaCl and BaCl 2 The molar ratio is 4:1. The chlorination coordination leaching temperature is 45°C, the solid (g) to liquid (ml) ratio is 1:8, and the leaching time is 160 minutes; immediately after the chlorination coordination leaching is completed, the leaching system is filtered and separated while it is hot, and lead-containing chloride is obtained. Coordinating the leaching solution and leaching slag, analyzing the lead content in the leaching slag, and ...
Embodiment 3
[0079] Lead sulfate slag provided by a company in Henan, after analysis, PbSO 4 The lead content in the physical phase is 20.2% (mass percentage).
[0080] Get above-mentioned lead sulfate slag 450g as raw material for subsequent use, the liquid after the crystallization of output in embodiment 1 and embodiment 2 is merged, obtains NaCl, NH containing 4 Cl and a small amount of CaCl 2 and BaCl 2 The mixed solution is 16.58L. Take out 2L from this mixed solution and carry out chlorination coordination leaching with above-mentioned 450g lead sulfate slag, add CaCl during leaching 2 , CaCl 2 The add-on of this is that the sulfate group in this 450g lead sulfate slag is all formed into 1.5 times of the required theoretical amount of calcium sulfate. The leaching temperature is 90°C and the leaching time is 150min. After the leaching is completed, the liquid and solid are separated while it is hot, and the leaching residue is dried and analyzed for PbSO 4content, the calcula...
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