Method for purifying zinc sulfate aqueous solution to remove nickel, cobalt and germanium

A zinc sulfate aqueous solution and nickel-cobalt technology are applied in the fields of purifying and removing nickel, cobalt and germanium, and in the fields of purifying and removing nickel, cobalt and germanium by hydro-smelting zinc, and can solve the problems of easy oxidation of cadmium and cobalt slag, poor adaptability of raw materials, and cobalt removal. The mechanism is unclear and other problems, so as to avoid re-dissolution, fast cobalt removal, and good cobalt removal effect.

Active Publication Date: 2020-06-09
KUNMING HANCHUANG SCI & TECH CO LTD
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  • Application Information

AI Technical Summary

Problems solved by technology

The second type is to add other metal elements to the zinc powder to improve the activity or replacement capacity of the zinc powder, but the law of cobalt removal has not been fully grasped so far, which leads to the adaptability of purification to raw materials in the production practice of zinc hydrometallurgy Poor, high consumption of zinc powder
The second-stage temperature is 75°C, but the cadmium-cobalt slag produced by this method is easy to oxidize. The characteristic of this method is that cobalt can be removed without adding copper and only a small amount of antimony, but the cadmium concentration required for cobalt removal is relatively high, making a large amount of Cadmium is cycled in the process
[0026] In 2000, Russian patent 2186131C2 proposed the use of zinc alloy zinc powder containing 0.6-0.9% lead and 0.003-0.5% iron to remove cobalt and nickel, and achieved the effect of reducing zinc powder, but obviously the iron in the solution will increase
The inventor believes that when antimony oxide and antimony potassium tartrate are added in a large amount, antimony may exceed the antimony content control standard of the electrolytic purification solution
[0035] 2. Antimony salts use different compounds, mainly antimony potassium tartrate and antimony oxide, but no patents have been found to compare the two. Most of the antimony compounds used in patents are antimony oxide, and the rest are antimony potassium tartrate. There is only one article The patent (Canadian patent 1122229) proposes the use of pentavalent antimony salts to remove cobalt
However, it is obvious that since this first-stage purification slag contains almost all impurity elements, the treatment process is relatively difficult, especially the need for secondary cobalt removal
[0042] 6. In terms of equipment, reactors with special structures are used to improve the efficiency of cobalt removal and reduce the consumption of zinc powder. However, these special tank types are inconvenient to use and most of them hav...

Method used

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  • Method for purifying zinc sulfate aqueous solution to remove nickel, cobalt and germanium
  • Method for purifying zinc sulfate aqueous solution to remove nickel, cobalt and germanium
  • Method for purifying zinc sulfate aqueous solution to remove nickel, cobalt and germanium

Examples

Experimental program
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Effect test

Embodiment 1

[0140] This embodiment adopts antimony potassium tartrate, Sb respectively 2 o 3 , Sb 4 o 5 Cl 2 Contrast experiment with cobalt and bile alum as activator for purification and removal of cobalt. The test temperature is 80°C, the test solution volume is 1 liter, and the test numbers are 1a, 1b, 1c, 1d, 1e.

[0141] The experimental equipment is a constant temperature water bath with a heating and temperature control device. The experiment is carried out in a beaker with an effective volume of 2 liters, and the stirring adopts a polytetrafluoro mechanical stirring paddle.

[0142] The experimental procedure is as follows: first heat a section of copper and cadmium removal solution to a certain temperature, add an appropriate amount of sulfuric acid, and at the same time add zinc powder, bile vitriol and antimony compound in solid form, maintain this temperature, and carry out cobalt removal experiment under stirring. After reacting for 60 minutes, start sampling to measure...

Embodiment 2

[0162] This example is an experiment on the influence of the amount of acid added to different types of zinc powder on the removal of cobalt. The experimental temperature is 80° C., and the amount of the experimental solution is 1 liter. The experimental equipment is the same as in Example 1.

[0163] a. Experiment on the amount of acid added to zinc powder in electric furnace

[0164] The main purpose of this experiment is to investigate the effect of the amount of acid added to the cobalt removal process of the electric furnace zinc powder on the removal of cobalt. The experiment numbers are 2a, 2b, 2c, and 2d. The experimental equipment and experimental procedures are the same as in Example 1. The difference is that sampling is only done at 90 minutes and 120 minutes, and no slag detection is performed. The zinc powder adopts the electric furnace zinc powder listed in Table 1, the zinc powder addition amount is 2g / l, and the activator adopts Sb 4 o 5 Cl 2 + bile vitrio...

Embodiment 3

[0177] This embodiment is an experiment of adding ways of bile vitriol and different antimony compounds and zinc powder. In the disclosed patents and some research papers, the addition method of the activator has not been paid attention to basically. The more addition method is to dissolve the activator into a solution first, then add it to the solution, and then add zinc powder. This addition method is conducive to precise control of the amount of reagent added. Surprisingly, the inventors found that different addition methods of the activator lead to significant differences in the experimental results. The experiment adopts two adding methods, the first one is to add the activator and dissolve it in the solution heated to the experimental temperature for 3 minutes, and then add zinc powder to remove cobalt; the second adding method is to use solid The activator and zinc powder are simultaneously added to the solution which has been heated to the experimental temperature. T...

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Abstract

The invention relates to a method for purifying a zinc sulfate aqueous solution. In a supernatant, a zinc powder is used to remove copper and cadmium. At a temperature of 80 to 95 DEG C, the zinc powder and a copper antimony activator are added to purify to remove cobalt, nickel and germanium. According to the cobalt concentration of the solution, the copper antimony activator, the zinc powder anda small amount of sulfuric acid or electrolytic waste liquid are added. For a section of waste solution after copper and cadmium removal, containing 2-120 mg/l of cobalt, 0.02-0.3 mg/l of germanium,0.02-4 mg/l of nickel, and 5-120 mg/l of cadmium, the purifying effect of the waste solution containing 0.1 mg/l of cobalt, 0.02 mg/l of germanium, and 0.1 mg/l of nickel can be realized after 90-150minutes. Various zinc powders are used to realize deep purification of the solution. The method is suitable for a purification system of an electrolytic zinc plant.

Description

technical field [0001] The invention belongs to the field of metallurgy of non-ferrous metals, and mainly relates to a method for purifying and removing nickel, cobalt and germanium by hydrometallurgy, in particular to a method for purifying and removing nickel, cobalt and germanium after a section of copper and cadmium removal The method, aiming at the deficiency of traditional purification and removal of cobalt, has been improved. Background technique [0002] The classic wet electrolytic production of zinc metal consists of the following process: a first step of leaching, in which the oxides of zinc containing impurities are leached with sulfuric acid recovered from electrolysis. [0003] The end point of the leaching solution is around pH 5.4, so that an appropriate amount of Fe 3+ Co-precipitate with arsenic, iron, germanium and some other elements, and by such a method, a neutral zinc sulfate leaching solution containing impurities is obtained. [0004] However, the ...

Claims

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Application Information

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IPC IPC(8): C22B19/20C22B3/44C25C1/16C25C7/06
CPCC22B19/26C22B3/44C25C1/16C25C7/06Y02P10/20
Inventor 张旭耿惠段志勇张云彭沈庆峰崔鹏
Owner KUNMING HANCHUANG SCI & TECH CO LTD
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