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Method of recovering manganese, lead and silver from zinc electrolyzed anode mud by utilizing acid-making tail gas

A technology for making acid tail gas and anode slime, which is applied in the fields of silver, manganese and lead recovery, which can solve the problems of difficulty in recycling, lack of recycling, high cost of electrolytic zinc, etc., and achieve the effect of simple process

Inactive Publication Date: 2011-04-06
ZHUZHOU SMELTER GRP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] The electrolysis process of zinc hydrometallurgy is to purify ZnSO 4 The solution is sent to the electrolytic cell for electrolysis, Zn 2+ Zinc is precipitated on the cathode of the aluminum plate, and the anode is an insoluble anode made of a lead plate containing a small amount of silver. During the electrolysis process, anode slime containing manganese, lead, and silver will be produced on the anode plate (because the zinc electrolyte also contains Mn 2+ , its role is to protect the anode), the traditional method is to return the anode slime produced by electrolysis directly to the leaching process, and its disadvantages are: manganese enters the leaching slag and rarely enters the leaching solution and cannot be recycled, and a large amount of manganese powder is still required for leaching (MnO 2 or MnCO 3 ), leading to high cost of electrolytic zinc; the lead and silver in the anode slime are also difficult to recover after entering the leaching residue (lead can be recovered partly through the volatilization kiln); the sulfuric acid section contains SO 2 Acid production tail gas (or containing SO 2 The leakage of industrial waste gas) is also a difficult problem in pollution control

Method used

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  • Method of recovering manganese, lead and silver from zinc electrolyzed anode mud by utilizing acid-making tail gas
  • Method of recovering manganese, lead and silver from zinc electrolyzed anode mud by utilizing acid-making tail gas

Examples

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example 1

[0024] Composition of zinc electrolysis anode sludge: manganese 52%, lead 17%, silver 1100 g / ton, slurry volume 5 liters, water: anode sludge = 4: 1 (i.e. liquid-solid ratio = 4: 1), tail gas concentration: Contains SO 2 3%, SO 2 Air flow 1m 3 / min, temperature: room temperature, through SO 2 Time: 4 hours, concentration of manganese-containing solution: manganese ion 106 g / liter, composition of lead and silver slag: manganese 2.8%, lead 49.6%, silver 2300 g / ton.

example 2

[0026] Exhaust gas concentration: containing SO 2 0.5%, SO 2 Airflow 1.1m 3 / min, temperature: room temperature, through SO 2 Time: 5 hours, concentration of manganese-containing solution: 105 g / liter of manganese ion, composition of lead and silver slag: 2.1% of manganese, 49.8% of lead, 2380 g / ton of silver, all the other are the same as example 1.

example 3

[0028] Exhaust gas concentration: containing SO 2 0.05%, SO 2 Airflow 1.6m 3 / min, temperature: room temperature, through SO 2 Time: 10 hours, concentration of manganese-containing solution: 105 g / liter of manganese ion, composition of lead and silver slag: 2.1% of manganese, 48.6% of lead, 2370 g / ton of silver, all the other are the same as example 1.

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Abstract

The invention discloses a method of recovering manganese, lead and silver from zinc electrolyzed anode mud by utilizing acid-making tail gas, aiming at recovering valuable metals such as manganese, lead and silver from zinc electrolyzed anode mud by utilizing acid-making tail gas containing SO2 and simultaneously solving the environmental problems of SO2 tail gas and slag. The method is characterized by comprising the following steps: A, pulping: grinding zinc electrolyzed anode mud and water into anode mud pulp by a globe mill; B, leaching: introducing the acid-making tail gas containing SO2 into the anode mud pulp; C, filtering products of step B to produce a solution containing manganese ions and slag containing lead and silver; and D, recovering: returning the solution containing manganese ions produced in step C to a zinc electrolyzing procedure or for producing manganese sulfate and electrolytic manganese, and sending the produced lead and silver slag to a lead blast furnace for recovering the lead and the silver. The invention mainly used for simultaneously solving two environmental problems of slag and gas in wet-process zinc-making factories.

Description

technical field [0001] The invention relates to a method for recovering manganese, lead and silver, in particular to a method for recovering manganese, lead and silver from zinc electrolysis anode slime by using acid production tail gas. Background technique [0002] The electrolysis process of zinc hydrometallurgy is to purify ZnSO 4 The solution is sent to the electrolytic cell for electrolysis, Zn 2+ Zinc is precipitated on the cathode of the aluminum plate, and the anode is an insoluble anode made of a lead plate containing a small amount of silver. During the electrolysis process, anode slime containing manganese, lead, and silver will be produced on the anode plate (because the zinc electrolyte also contains Mn 2+ , its role is to protect the anode), the traditional method is to return the anode slime produced by electrolysis directly to the leaching process, and its disadvantages are: manganese enters the leaching slag and rarely enters the leaching solution and cann...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B3/08C22B7/00C22B11/00C22B13/00C22B47/00
Inventor 龙诗明
Owner ZHUZHOU SMELTER GRP
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