Method for circularly removing chlorine in zinc sulphate solution by copper slag

A technology of zinc sulfate solution and copper slag, applied in the direction of improving process efficiency, etc., can solve the problems of difficult to guarantee dechlorination effect, difficult process control, high production cost, etc., achieve good dechlorination effect, less reagent consumption, Less interference from external factors

Inactive Publication Date: 2010-01-27
蒙自矿冶有限责任公司
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] The specific method of Chinese patent CN101113015 copper slag dechlorination is: add copper sulfate (copper ion) and copper slag (containing elemental copper) in zinc sulfate solution, the main source of copper sulfate is to purchase or copper slag acidification roasting, water immersion To obtain copper sulfate, the former (referring to the purchase of copper sulfate) needs to increase relatively more costs, and the latter (referring to copper slag acidified roasting and water immersion to obtain copper sulfate) has relatively more production costs, and the operation is relatively complicated. When the source of copper slag changes, the process is difficult to control, and the dechlorination effect is difficult to guarantee

Method used

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  • Method for circularly removing chlorine in zinc sulphate solution by copper slag

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] Before copper slag is produced, the dechlorinated copper ions come from copper sulfate. In this example, only copper sulfate is added.

[0038] Chemical composition of zinc sulfate solution to be dechlorinated: Cl 1.36g / l, Zn 130g / l, Cu 0.2g / l, Fe 0.025g / l, Cd 0.7g / l; chemical composition of solid copper sulfate: Cu 20.1% ,; Electrolytic waste: H 2 SO 4 175g / l. The production process conditions are shown in Table 1:

[0039] Table 1: Process conditions for removing ammonia in zinc sulfate solution

[0040] Alkali washing copper slag

Intake (kg / h)

copper sulfate added

Quantity (kgh)

electrolytic waste stream

Quantity (m 3 / h)

Addition amount of zinc powder

(kg / h)

Zinc sulfate solution

Flow (m 3 / h)

temperature reflex

(℃)

0

540

0.09

28

30

40

[0041] Chlorine removal results of zinc sulfate solution:

[0042] The chemical composition of zinc sulfate so...

Embodiment 2

[0047] The chemical composition of a batch of zinc sulfate solution to be dechlorinated: Cl 1.1g / l, Zn 140g / l, Cu 0.3g / l, Fe 0.02g / l, Cd 0.8g / l; alkaline cleaning copper slag is the last operation Return, its chemical composition: Cu 33.5%, Cl 3.2%; electrolytic waste solution: H 2 SO 4 170g / l. The production process conditions are shown in Table 2:

[0048] Table 2: Process conditions for removing chlorine in zinc sulfate solution

[0049] Alkali washing copper slag

Intake (kg / h)

copper sulfate added

Quantity(kg / h)

electrolytic waste stream

Quantity (m 3 / h)

Addition amount of zinc powder

(kg / h)

Zinc sulfate solution

Flow (m 3 / h)

temperature reflex

(℃)

46

0

0.1

4

40

65

[0050] The result of chlorine removal by zinc sulfate solution is:

[0051] The chemical composition of zinc sulfate solution after chlorine removal: Cl 0.22g / l, Zn 138g / l, Cu 2.1g / l, Fe0.0...

Embodiment 3

[0055] When the copper ions in the returned copper slag are insufficient, additional copper sulfate is properly supplemented. This is the case in this case.

[0056] The chemical composition of the zinc sulfate solution to be dechlorinated is: Cl 1.15g / l, Zn 130g / l, Cu 0.3g / l, Fe 0.2g / l, Cd 1.2g / l; the chemical composition of the alkaline cleaning copper slag: Cu 35.3%, Cl 3.4%; copper sulfate liquid Cu 40g / l. The production process conditions are shown in Table 3:

[0057] Table 3: Process conditions for removing chlorine in zinc sulfate solution

[0058] Alkali washing copper slag

Intake (kg / h)

copper sulfate added

Quantity (kgh)

electrolytic waste stream

Quantity (m 3 / h)

Addition amount of zinc powder

(kg / h)

Zinc sulfate solution

Flow (m 3 / h)

temperature reflex

(℃)

45

1

0.15

1.5

20

90

[0059] Chlorine removal results of zinc sulfate solution:

[0060] T...

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Abstract

The invention relates to a method for circularly removing chlorine in a zinc sulphate solution by copper slag. The method comprises the following steps: copper ions, zinc powders and a zinc sulphate solution are added into a continuous reaction groove and react in a stirring state to obtain the zinc sulphate solution containing Cl<-> equal to or less than0.3g/l, and a CuCl precipitate generated in the reaction enters slag; a mixture of the zinc sulphate solution and the slag are treated by liquid-solid separation to obtain a dechlorinated zinc sulphate solution and copper slag; the separated copper slag is washed with alkali to remove chlorine ions; the copper slag after being washed with the alkali is returned to the continuous reaction groove for carrying out a circular reaction; and when the copper ions are deficient, a certain copper sulfate is added at proper time for replenishment. The invention utilizes the zinc powders as a reducer for reacting with the copper ions in the zinc sulphate solution to generate a CuCl copper slag precipitate, Cl<-> is eluted with the alkali, Cu2O is also obtained and is returned to react with the Cl<-> in the solution for circular dechlorination, copper sulfate does not need to be added or a little copper sulfate is only added in the dechlorination process, the consumption of raw materials is little, and the cost is low; compared with a method that the copper slag which can be changed is added continuously, the interference of external factors to a dechlorination technique is little, the process is easy to control, and the dechlorination effect is stable and reliable.

Description

technical field [0001] The invention relates to a method for circularly removing chlorine in zinc sulfate solution by copper slag. Background technique [0002] In the process of zinc hydrometallurgy, chlorine is a harmful impurity element, mainly derived from chlorides in zinc concentrate and zinc fume. The concentration of chlorine in the electrolytic circulating solution is high (Cl - >0.3g / l), the corrosion speed of electrolytic cathode and anode plates is greatly accelerated, which increases energy consumption and reduces the quality of electrolytic zinc. Therefore, before the zinc sulfate solution is sent to electrolysis, most of the chlorine in the solution must be removed. At present, some factories usually use the pre-fire method (such as multi-hearth furnace) roasting to remove the chlorine in the zinc fume, so that most of the chlorine does not enter the wet system, and when the chlorine in the zinc sulfate solution in the wet system reaches a certain concent...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B3/46C22B19/00
CPCY02P10/20
Inventor 黎东明黎雨黎维中黄昌元陈业建吴国钦周忠跃康大平冯继平李自兴陈春发韦乃团潘云鹏曾繁顺
Owner 蒙自矿冶有限责任公司
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