Electrolyte and method for electrolyzing and refining crude lead

An electrolytic refining and electrolyte technology, applied in the field of hydrometallurgy, can solve problems such as poor working environment, unpleasant smell, and low comprehensive recovery rate, and achieve the effects of avoiding toxic and harmful gases, significant energy saving effects, and high product quality

Inactive Publication Date: 2015-07-01
KUNMING UNIV OF SCI & TECH
View PDF4 Cites 22 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There are many pyro-refining processes, which produce a large amount of lead-containing smoke and waste residue, serious environmental pollution, poor working environment, and low lead yield and comprehensive recovery rate of valuable elements such as precious metals. Therefore, the electrolytic refining of crude lead is widely used in Canada and the United States. , Japan and China are widely used
[0003] At present, the electrolytic refining of crude lead uses a solution system composed of fluorosilicic acid and lead fluorosilicic acid as the electrolyte for electrolysis. The main disadvantages of electrolysis in this system are: (1) fluorosilicic acid is volatile and decomposes into toxic HF and SiF 4 Gas, a large amount of acid mist is formed at the work site, which has an unpleasant smell and is very harmful to the human body and the environment; (2) In the widely used 105~200A / m 2 Under the current density, the corresponding cell voltage is as high as 0.36~0.7V, and the DC power consumption per ton of lead is 110~190kw h, which is high energy consumption; (3) The current efficiency is low, only about 90%

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] The electrolytic refining crude lead methanesulfonic acid solution system electrolyte is composed of lead methanesulfonate and free methanesulfonic acid, wherein Pb 2+ The concentration is 50g / L, and the concentration of free methanesulfonic acid is 100g / L.

[0019] Adopt the electrolysis method of electrolytic refining rough lead of this electrolyte, concrete steps comprise as follows: will contain Pb 2+ The electrolyte with a concentration of 50g / L and a concentration of free methanesulfonic acid of 100g / L, the crude lead anode plate to be refined, and the cathode plate are placed in the electrolytic cell, and then direct current is applied, and the cathode current density is controlled to 500A / m 2 , The distance between the rough lead anode plate and the cathode plate is 65mm, the circulation rate of the electrolyte is 30L / min, the temperature of the electrolyte is 20°C, and the mixture of animal glue and lignosulfonate with a mass ratio of 1:1 is added to the electr...

Embodiment 2

[0022] The electrolytic refining crude lead methanesulfonic acid solution system electrolyte is composed of lead methanesulfonate and free methanesulfonic acid, wherein Pb 2+ The concentration is 200g / L, and the concentration of free methanesulfonic acid is 160g / L.

[0023] Adopt the electrolysis method of electrolytic refining rough lead of this electrolyte, concrete steps comprise as follows: will contain Pb 2+ The concentration is 200g / L, the concentration of free methanesulfonic acid is 160g / L electrolyte, the crude lead anode plate and cathode plate to be refined are put into the electrolytic cell, and then direct current is passed through, and the cathode current density is controlled to 80A / m 2 , The distance between the crude lead anode plate and the cathode plate is 45mm, the circulation rate of the electrolyte is 15L / min, the temperature of the electrolyte is 40°C, and animal glue, lignosulfonate and β-naphthalene are added to the electrolyte with a mass ratio of 1:1...

Embodiment 3

[0026] The electrolytic refining crude lead methanesulfonic acid solution system electrolyte is composed of lead methanesulfonate and free methanesulfonic acid, wherein Pb 2+ The concentration is 120g / L, and the concentration of free methanesulfonic acid is 50g / L.

[0027] Adopt the electrolysis method of electrolytic refining rough lead of this electrolyte, concrete steps comprise as follows: will contain Pb 2+ The electrolyte with a concentration of 120g / L and a concentration of free methanesulfonic acid of 50g / L, the crude lead anode plate to be refined, and the cathode plate are placed in the electrolytic cell, and then direct current is applied, and the cathode current density is controlled to 300A / m 2 , The distance between the anode plate and the cathode plate of crude lead is 35mm, the circulation rate of the electrolyte is 20L / min, the temperature of the electrolyte is 50°C, and the mass ratio of adding animal glue, lignin sulfonate and aloin in the electrolyte is 1:1...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

PropertyMeasurementUnit
current efficiencyaaaaaaaaaa
current efficiencyaaaaaaaaaa
Login to view more

Abstract

The invention relates to electrolyte and a method for electrolyzing and refining crude lead, and belongs to the technical field of wet-process metallurgy. The electrolyte electrolyzing and refining crude lead is of a methylsulphonic acid solution system comprising methyl lead sulfonate and free methyl sulfonic acid, wherein the concentration of Pb<2+> is 50-200g / L, and the concentration of the free methyl sulfonic acid is 50-160g / L. The method comprises the following steps: placing a solution system electrolyte comprising the methyl lead sulfonate and free methyl sulfonic acid, a to-be-refined crude lead anode plate and a cathode plate into an electrolytic cell, then, applying direct-current power, adding an additive comprising one or a mixture of animal glue, lignosulfonate, aloin and beta-naphthol into the electrolyte to electrolyze for 2-7 days so as to generate cathode lead and anode mud, obtaining national-standard 1# lead ingot after melting and casting cathode lead, performing washing and filter pressing on the anode mud, and then feeding the anode mud to a noble metal extracting process. According to the method, a brand-new methanesulfonic acid solution system is adopted as an electrolyte for electrolysis, so that the method has the characteristic of being remarkable in environment-friendly advantage.

Description

technical field [0001] The invention relates to an electrolytic solution and an electrolysis method for electrolytically refining crude lead, and belongs to the technical field of hydrometallurgy. Background technique [0002] Crude lead produced by various methods contains a certain amount of impurities. In order to remove harmful impurities and recover valuable elements such as precious metals, it must be refined. The refining methods are divided into two types: fire refining and electrolytic refining. There are many pyro-refining processes, which produce a large amount of lead-containing smoke and waste residue, serious environmental pollution, poor working environment, and low lead yield and comprehensive recovery rate of valuable elements such as precious metals. Therefore, the electrolytic refining of crude lead is widely used in Canada and the United States. , Japan and China are widely used. [0003] At present, the electrolytic refining of crude lead uses a solutio...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Applications(China)
IPC IPC(8): C25C1/18
CPCC25C1/18
Inventor 金炳界张玉慧
Owner KUNMING UNIV OF SCI & TECH
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products