Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

High grade cobalt sulfonate slag and production process thereof

A high-grade technology of cobalt xanthate, applied in the direction of improving process efficiency, etc., can solve the problems of reducing the amount of sodium ethyl sulfonate, expensive oxidant, and expensive copper sulfate, so as to reduce energy consumption, high promotion value, low cost effect

Active Publication Date: 2012-09-19
巴彦淖尔紫金有色金属有限公司
View PDF6 Cites 1 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the cobalt removal process using copper sulfate as the oxidant has the disadvantages that the oxidant is expensive, and the cobalt sulfonate residue contains copper impurities, and the oxidant itself consumes sodium ethyl sulfonate. This process needs further improvement.
[0006] Chinese patent application CN1172859A and CN101440431A disclose the method that utilizes cobalt xanthate slag to reclaim cobalt respectively, yet its cobalt xanthate slag all utilizes copper sulfate to remove cobalt and obtains, and the technique for preparing cobalt xanthate slag has the following defects: (1) The traditional sodium ethyl sulfonate cobalt removal process using copper sulfate as an oxidant, copper sulfate is expensive, resulting in high cost of cobalt removal, the purpose of the present invention is to use cheap oxidant instead of copper sulfate as oxidant
[0008] (3) Traditional sodium ethyl sulfonate removes cobalt process, oxidant copper sulfate reacts with sodium ethyl sulfonate, consumes sodium ethyl sulfonate additionally, further increases the cost of removing cobalt, the purpose of the present invention is to select a kind of ethyl sulfonate Sodium sulfonate is an oxidizing agent for removing cobalt. The oxidizing agent does not react with sodium ethyl sulfonate and minimizes the amount of sodium ethyl sulfonate.
[0009] (4) The cobalt salt produced by the traditional sodium ethyl sulfonate cobalt removal process has low efficiency and low cobalt content

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
  • High grade cobalt sulfonate slag and production process thereof
  • High grade cobalt sulfonate slag and production process thereof
  • High grade cobalt sulfonate slag and production process thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0057] The specific embodiments of the present invention are as follows, those skilled in the art should understand that the zinc hydrometallurgy process is only a schematic illustration, those skilled in the art can further clearly understand through the specific embodiments of the present invention given below the present invention, but they are not limitations of the present invention.

[0058] Hydrometallurgy zinc process:

[0059] 1. Purification slag leaching

[0060] 1. Process principle

[0061] The principle of purification slag leaching is to use the zinc, cadmium, cobalt of the purification slag to react with sulfuric acid to enter the solution, while the copper element does not react with sulfuric acid and remains in the slag, so as to realize the separation of copper and other valuable metals.

[0062] main chemical reaction

[0063] Cd+H 2 SO 4 =CdSO 4 +H 2 ↑ (1)

[0064] CdO+H 2 SO 4 =CdSO 4 +H 2 O (2)

[0065] Zn+H 2 SO 4 =ZnSO 4 +H 2 ↑ (3)

...

Embodiment 2

[0116] Similar to other steps of embodiment 1, wherein for the technology of reclaiming cobalt in the hydrometallurgy process, ammonium persulfate is used as oxidant sodium ethyl sulfonate to reclaim cobalt:

[0117] The technological conditions are: temperature 35-40°C; initial pH 5.0-5.2; sodium ethylsulfonate: ammonium persulfate: cobalt = (9-12): (4-5): (0.5-2); Time 20-30 minutes; reaction time 0.5-1.5 hours,

[0118] 3. Operating procedures

[0119] 3.1 Calculate the amount of cobalt removal agent according to the total amount of cobalt in the solution, the preparation ratio of the agent: sodium ethylsulfonate: ammonium persulfate: cobalt = (9-12): (4-5): (0.5-2),

[0120] 3.2 Prepare sodium ethyl sulfonate as a 10% solution, and ammonium persulfate as a solution for later use.

[0121] 3.3 Drill 40-45m into the cobalt removal tank 3 After the second stage of cadmium removal, control the pH of the initial acid to be greater than 5.0. When the acidity is too high, add ...

Embodiment 3

[0125] Similar to other steps of embodiment 1, wherein for the technique of reclaiming cobalt in the hydrometallurgy process is: ammonium persulfate is used as oxidant sodium ethyl sulfonate to remove cobalt, and its technological condition is:

[0126] Temperature 38°C; PH (beginning) 5.1; sodium ethylsulfonate: ammonium persulfate: cobalt = 12:4.8:0.9; dosing time 29 minutes; reaction time 1.1 hours.

[0127] Operation steps include

[0128] 3.1 Calculate the amount of cobalt removal agent according to the total amount of cobalt in the solution. The preparation ratio of the agent is: sodium ethylsulfonate: ammonium persulfate: cobalt = 12:4.8:0.9.

[0129] 3.2 Prepare sodium ethylsulfonate as a 10% solution and ammonium persulfate as a solution for later use.

[0130] 3.3 Drill 40-45m into the cobalt removal tank 3 After the second stage of cadmium removal, control the pH of the initial acid to 5.1. When the acidity is too high, add sodium hydroxide to adjust the pH to the...

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

No PUM Login to View More

Abstract

The invention relates to high grade cobalt sulfonate slag produced by using ammonium sulfate instead of copper sulfate as an oxidant. The high grade cobalt sulfonate slag comprises 15 to 21 percent of cobalt. The method comprises the following steps: preparing an agent from sodium isethionate, ammonium persulfate and cobalt in a ratio of (9-12):(4-5):(0.5-2); preparing the sodium isethionate into a 10 percent solution, and preparing the ammonium persulfate into a solution for later use; introducing 40 to 45 m<3> of two-stage cadmium removing solution into a cobalt removing tank, controlling the pH of initial acid to be more than 5.0, adding sodium hydroxide to regulate the pH to the required range when the acidity is high, and controlling the temperature to be less than or equal to 45DEG C; and adding the ammonium persulfate, slowly and uniformly adding the sodium isethionate, controlling the dosing time to be 20-30 minutes, reacting for 0.5 to 1.5 hours, discharging a solution into a middle tank by opening a bottom current valve, pumping into a cobalt removing filter press by using a pump for filter pressing, unloading the cobalt slag into a cobalt slag primary rinsing bath, and conveying filtrate into a leaching workshop.

Description

technical field [0001] The present invention relates to a kind of using ammonium persulfate instead of conventional oxidant (copper sulfate) as oxidant to produce high-grade cobalt xanthate slag and its production process, more specifically to a kind of wet zinc smelting process, which utilizes the above-mentioned recycling cobalt process to remove cobalt. Background technique [0002] There are three main processes for the recovery of cobalt in the zinc hydrometallurgy process, namely antimony salt cobalt removal process, β-naphthol cobalt removal process and sodium ethyl sulfonate cobalt removal process. At present, the cobalt removal process of antimony salt is mainly used in the zinc liquid purification process of wet smelting. The cobalt in the zinc concentrate enters the purification slag to open the circuit during the liquid purification process. The recovery process of cobalt metal in the purification slag mainly includes β-naphthol cobalt removal process and Sodium...

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): C22B7/04C22B19/30C22B23/00
CPCY02P10/20
Inventor 沙涛孙明生甄勇杜敏
Owner 巴彦淖尔紫金有色金属有限公司
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products