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

Active Publication Date: 2019-08-23
CENT SOUTH UNIV
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Therefore, when it is mixed into the furnace and smelted with PbS concentrate, its matching amount is limited, otherwise it will be difficult to maintain the heat balance of the lead smelting system
In addition, the pyrometallurgical process to treat lead sulfate slag not only consumes a lot of energy, but also easily produces SO 2 , volatile lead dust and other air pollutants, the cost of smelting flue gas treatment is relatively higher; the most common treatment method for lead sulfate slag in the wet recovery process is mainly Na 2 CO 3 or NaHCO 3 As a desulfurizer, the PbSO in the lead sulfate slag was mixed under strong stirring conditions 4 Convert to PbCO 3 , and then roast it or mix it with fluorosilicic acid system and electrolyze it to get lead powder
However, practice has proved that the lead sulfate slag wet treatment process has problems such as low conversion rate, large amount of wastewater discharge, and easy release of toxic and harmful gases such as HF during electrolysis of the fluorosilicic acid system.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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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Abstract

The invention discloses a method for wet-process cleaning treatment of lead sulfate slag. The method comprises the following steps that firstly, a chloride solution is taken as a coordination leachingagent, the lead sulfate slag is subjected to chlorination coordination leaching, and a lead chlorination coordination leaching solution and leaching slag are obtained; the leaching solution is subjected to cooling crystallization after immediate hot filtration, then liquid-solid separation is carried out again, and a lead chloride crystal and a crystallized solution are obtained correspondingly;the crystallized solution is reused for the chlorination coordination leaching, and the lead chloride crystal obtained by crystallization is added into an acetate solution system for conversion and leaching; after the leaching solution is converted and leached, the leaching solution is directly used as a cathode solution without purification, and lead is extracted by adopting a diaphragm electrodeposition technology; and after the diaphragm electrodeposition is completed, the negative electrode obtains 99.9% or more of lead, a cathode dilution solution and an anode dilution solution can be returned to the system to be used, and closed loop circulation of the technological process is realized. According to the method, the lead sulfate slag can be subjected to clean and efficient treatment so that a lead product with relatively high purity can be obtained directly, and the method has the outstanding advantages of being high in raw material adaptability, simple in technological process, high in valuable element recovery rate and clean and environment-friendly.

Description

technical field [0001] The invention belongs to the field of hydrometallurgy, and in particular relates to a method for wet cleaning treatment of lead sulfate slag. Background technique [0002] In the process of zinc hydrometallurgy, a large amount of lead sulfate slag is often produced. In addition, zinc leaching slag, converter soot, iron and steel plant soot, copper smelting soot, etc., after pyro-reduction and volatilization treatment, also contains lead. After sulfuric acid leaching, most of the lead is concentrated in the leaching slag, forming lead sulfate slag. Most of the lead in these lead sulfate slags is PbSO 4 There are physical phases, and the lead content generally ranges from 10 to 50%. It is of great significance to realize its resource utilization, reduction and recycling. [0003] At present, the treatment process of lead sulfate slag can be divided into pyrometallurgy and hydrometallurgy. Pyrometallurgy is mainly to use it as raw material for lead sme...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B7/00C22B13/00C25C1/18C25C7/02C25C7/06
CPCC22B7/006C22B13/045C25C1/18C25C7/02C25C7/06Y02P10/20
Inventor 杨建广丁龙李陵晨南天翔刘山闫万鹏杨建英
Owner CENT SOUTH UNIV
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