Unlock instant, AI-driven research and patent intelligence for your innovation.

Deep nickel and cobalt purification method for zinc leachate

A deep purification and leaching solution technology, which is applied in the field of zinc metallurgy, can solve complex problems and achieve the effects of low temperature, high quality new solution and wide practicability

Inactive Publication Date: 2014-08-06
BEIJING GENERAL RES INST OF MINING & METALLURGY
View PDF6 Cites 16 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The Vallefield Zinc Plant adopts three stages of purification, the first stage does not add zinc powder, but adds the copper cadmium slag with high zinc content produced in the second and third stages, thereby reducing the consumption of zinc powder, but the obtained It is a complex Cu-Cd-Co slag

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

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Deep nickel and cobalt purification method for zinc leachate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] Take 2L zinc sulfate immersion solution (Cu0.69g / L, Cd0.74g / L, Co0.052g / L, Ni0.0087g / L, Zn141.00g / L, Mn30.23g / L, Fe<0.010g / L , Sb<0.00010g / L), the pH of the infusion solution is about 4.75, and the density is 1.41g / L. The experiment adopts a two-stage purification method to purify and remove impurities.

[0036] One-stage low-temperature purification: temperature 55°C, zinc powder addition 7.314g, lead sulfate 0.3g, time 60min;

[0037] After the first stage of purification, Cu0.063mg / L and Cd1.61mg / L in the solution; Cu12.9% and Cd14.4% of the first stage of purification residue;

[0038] Second-stage high-temperature purification: Take 1L of purified liquid in the first stage, temperature 80°C, add 3.634g of zinc powder, 0.0363g of lead sulfate, 0.0044g of antimony potassium tartrate, 0.172g of copper sulfate pentahydrate, and 180min;

[0039] After the second-stage purification, Cu0.05mg / L, Cd0.03mg / L, Co0.05mg / L, Ni0.019mg / L in the solution; the second-stage purif...

Embodiment 2

[0041] Take 2L zinc sulfate immersion solution (Cu0.69g / L, Cd0.74g / L, Co0.052g / L, Ni0.0087g / L, Zn141g / L, Mn30.23g / L, Fe<0.01g / L, Sb <0.0001g / L), the pH in the leachate is about 4.75, and the density is 1.41g / L. The experiment adopts a two-stage purification method to purify and remove impurities.

[0042] One-stage low-temperature purification: temperature 50°C, zinc powder addition 4.876g, lead sulfate 0.2g, time 30min;

[0043] After the first stage of purification, Cu0.24mg / L and Cd1.79mg / L in the solution; Cu17.8% and Cd17.7% of the first stage of purification residue;

[0044] Second-stage high-temperature purification: Take 1L of purified liquid in the first stage, temperature 90°C, add 4.990g of zinc powder, 0.0499g of lead sulfate, 0.0044g of antimony potassium tartrate, 0.172g of copper sulfate pentahydrate, and 120min;

[0045] After the second-stage purification, Cu0.05mg / L in the solution, Cd does not exist, Co0.03mg / L, Ni0.021mg / L; the second-stage purification ...

Embodiment 3

[0047] Get leaching solution (Cu0.69g / L, Cd0.74g / L, Co0.052g / L, Ni0.0087g / L, Zn141g / L, Mn30.23g / L, Fe<0.01g / L, Sb< 0.0001g / L), the pH of the infusion solution is about 4.75, and the density is 1.41g / L. The experiment adopts a two-stage purification method to purify and remove impurities.

[0048] One-stage low-temperature purification: temperature 55°C, zinc powder addition 8.5313g, lead sulfate 0.3498g, time 90min;

[0049] Second-stage high-temperature purification: Take 1L of purified liquid in the first stage, temperature 95°C, add 9.98g of zinc powder, 0.0998g of lead sulfate, 0.0088g of antimony potassium tartrate, 0.26g of copper sulfate pentahydrate, and 60 minutes;

[0050] After the second-stage purification, Cu0.05mg / L, Cd0.039mg / L, Co0.043mg / L, Ni0.021mg / L in the solution; the second-stage purification residue Zn79.6%, Cu0.70%, Co0.72%, Ni0.06%, Cd<0.05%.

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
particle diameteraaaaaaaaaa
particle diameteraaaaaaaaaa
Login to View More

Abstract

The invention relates to a deep nickel and cobalt purification method for zinc leachate. According to the method, a counterflow purification process is divided into two stages, namely first-stage low-temperature-purification copper (Cu) and cadmium (Cd) removal and second-stage high-temperature-purification nickel (Ni) and cobalt (Co) removal; by adopting a staged zinc leachate purification method, the removal of four elements, namely Cu, Cd, Ni and Co, from a zinc sulfate leachate can be realized, the content of each of Cu and Cd in purified zinc liquid obtained through the first-stage low-temperature-purification Cu and Cd removal is lower than 0.1mg / L, and the content of each of Ni and Co in purified zinc liquid obtained through the second-stage high-temperature-purification Ni and Co removal is lower than 0.1mg / L. Through the two-stage counterflow purification process, the concentration of cobalt ions (about 50mg / L) and Cu, Cd and Ni in a high-concentrations zinc containing solution can be lowered below 0.1mg / L, and thus, a qualified electrolytic zinc solution is obtained.

Description

technical field [0001] The invention belongs to the technical field of zinc metallurgy, and relates to a method for removing copper, cadmium, nickel and cobalt from a zinc leaching solution, in particular to a method for deeply purifying nickel and cobalt from a zinc leaching solution. Background technique [0002] Purification of zinc sulfate solution is one of the key processes of zinc hydrometallurgy. The quality of solution purification directly affects the current efficiency of zinc electrowinning and the quality of electrolytic zinc. The purpose of purifying the zinc hydrometallurgy solution is to remove impurities such as Cu, Cd, Ni, Co, etc., and to provide qualified new solution for the subsequent zinc electrowinning process. Among them, nickel and cobalt are the most difficult impurities to remove in the zinc sulfate solution, and zinc electrowinning has very strict requirements on the content of impurities in the electrowinning solution. If the impurity content in...

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): C22B3/46C22B3/44
CPCY02P10/20
Inventor 蒋开喜王海北刘三平邹小平张邦胜王玉芳赵磊蒋伟魏帮蒋应平汪胜东冯亚平
Owner BEIJING GENERAL RES INST OF MINING & METALLURGY