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Zinc concentrate carbon-adding oxidizing roasting and leaching method

A zinc concentrate and carbon oxidation technology, applied in chemical instruments and methods, magnetic separation, solid separation, etc., can solve the problems of large area occupation, complicated process, high energy consumption, etc., achieve low energy consumption, simple process, and reduce production volume effect

Pending Publication Date: 2022-07-15
GUILIN UNIVERSITY OF TECHNOLOGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] It can be seen that the traditional zinc extraction methods require complicated processes, high energy consumption, and occupy a lot of land.

Method used

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  • Zinc concentrate carbon-adding oxidizing roasting and leaching method
  • Zinc concentrate carbon-adding oxidizing roasting and leaching method
  • Zinc concentrate carbon-adding oxidizing roasting and leaching method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] (1) The zinc concentrate is crushed, collected and bagged after passing through a 200-mesh sieve, and 20g of zinc concentrate I and 3.0% of the dust-removing ash relative to the mass of the zinc concentrate are weighed by an electronic balance and evenly placed in the corundum ark. , the tube furnace is heated to 900 degrees Celsius, and then the mixture of zinc concentrate with carbonaceous reducing agent is placed in the tube furnace for heating, stirring once every 10 minutes to make it fully react, and after 1 hour of roasting, the The ark was cooled naturally at room temperature, and the calcine was cooled and then ground in a mortar.

[0037] (2) Weighing 10g of calcine, according to the mass ratio of zinc calcine to dilute acid solution I 1:15, weigh 150g of dilute sulfuric acid with a concentration of 30g / L for neutral leaching. The leaching time was 2 hours, and the pH value of the leaching end point was 5.0. The mixed solution is filtered to obtain intermedia...

Embodiment 2

[0040](1) The zinc concentrate is crushed, collected and bagged after passing through a 200-mesh sieve, and 20g of zinc concentrate I and 3% of the coke relative to the mass of the zinc concentrate are weighed by an electronic balance and evenly placed in the corundum ark. The tube furnace was heated to 750 degrees Celsius, and then the mixture of zinc concentrate with carbonaceous reducing agent was placed in the tube furnace for heating, and stirred every 10 minutes to make it fully react. After 1 hour of roasting, the ark was heated. Cool naturally at room temperature, and place the calcine in a mortar for grinding after cooling.

[0041] (2) Weighing 10g of calcine, according to the mass ratio of zinc calcine to dilute acid solution I 1:15, weigh 150g of dilute sulfuric acid solution with a concentration of 30g / L for neutral leaching. The leaching time was 2 hours, and the pH value of the leaching end point was 5.0. The mixed solution is filtered to obtain intermediate le...

Embodiment 3

[0044] (1) The zinc concentrate is crushed, collected and bagged after passing through a 200-mesh sieve, and 20g of zinc concentrate I and 3% of the coke relative to the mass of the zinc concentrate are weighed by an electronic balance and evenly placed in the corundum ark. The tube furnace is heated to 900 degrees Celsius, and then the mixture of zinc concentrate containing carbonaceous reducing agent is placed in the tube furnace for heating, stirring once every 10 minutes to make it fully react, and after 1 hour of roasting, the ark is heated. Cool naturally at room temperature, and place the calcine in a mortar for grinding after cooling.

[0045] (2) Weighing 10g of calcine, according to the mass ratio of zinc calcine to dilute acid solution I 1:15, weigh 150g of dilute sulfuric acid solution with a concentration of 30g / L for neutral leaching. The leaching time was 2 hours, and the pH value of the leaching end point was 5.0. The mixed solution is filtered to obtain inter...

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Abstract

The invention discloses a zinc concentrate carbon-adding oxidizing roasting and leaching method which comprises the following steps: (1) mixing: crushing zinc concentrate, and uniformly mixing the crushed zinc concentrate with a carbonaceous reducing agent to obtain a mixture; (2) roasting: roasting the mixture to obtain zinc calcine; (3) neutral leaching: mixing the zinc calcine with a dilute acid solution I, and carrying out neutral leaching; (4) acid leaching: mixing neutral leaching residues with a dilute acid solution II, and carrying out acid leaching; and (5) collecting: collecting the neutral leaching solution and the acid leaching solution. The carbonaceous reducing agent is added into the zinc concentrate, and under the action of the carbonaceous reducing agent, a weak oxidizing atmosphere is formed, so that iron in the zinc concentrate mainly generates Fe3O4 and an anoxic oxide Fe2O3-x (0lt; xlt; the method has the advantages that 1) the generation amount of zinc ferrite is reduced, and the content of ZnO which is easily dissolved in acid is increased, so that the purpose of efficiently leaching zinc is achieved; the leaching rate of zinc in the dilute sulphuric acid solution of the zinc calcine subjected to carbon oxidation roasting reaches 79.98% or above, and the leaching rate of iron is extremely low and is only about 1%.

Description

technical field [0001] The invention belongs to the field of zinc metallurgy, and in particular relates to a method for oxidative roasting and leaching of zinc concentrate by adding carbon. Background technique [0002] Zinc concentrate usually refers to a general term for a type of zinc sulfide concentrate with iron content of not more than 18wt%, zinc content of more than 40wt%, sulfur content of generally 25 to 35wt%, and associated with a certain content of copper and lead metals. For the treatment of this type of iron-containing zinc sulfide concentrate, the traditional technological process is oxidative roasting of zinc concentrate—neutral leaching—acid leaching—electrodeposition. When this method is used to treat iron-containing zinc concentrates, the zinc oxide produced in the oxidative roasting process reacts with the impurity ferric oxide to form zinc ferrite (ZnFe) which is insoluble in weak acid. 2 O 4 ), resulting in a low zinc leaching rate (≤80%). The high ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B19/20C22B1/02C22B19/02B03C1/015
CPCC22B19/22C22B1/02C22B19/02B03C1/015
Inventor 蔡井泉陈进中郭佳文邹家俊马皓皓武威王志云覃媚
Owner GUILIN UNIVERSITY OF TECHNOLOGY