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

Method for extracting valuable metal from copper nickel sulfide through ammonium persulfate-sulfuric acid oxidation leaching

A technology of ammonium persulfate and valuable metals, which is applied in the field of non-ferrous metallurgy, and can solve the problems of polluting the environment, increasing recycling costs, increasing costs, etc.

Active Publication Date: 2020-07-14
东北大学秦皇岛分校
View PDF4 Cites 4 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In order to improve the leaching rate of copper, Fan Xingxiang et al. studied the process of leaching chalcopyrite with silver ion catalysis and ammonium persulfate, and reacted the ore powder with a particle size of -74+58 μm at 95°C for 100 minutes, and the leaching rate of copper could reach 98%. % or more, but the addition of silver ions not only increases the cost, but also causes the decomposition of ammonium persulfate to produce N 2 and SO 2 , increase recycling costs and pollute the environment
In addition, these studies are all aimed at the study of single mineral phase minerals with extremely fine grain size, while the processing research on low-grade copper-nickel sulfide minerals with complex mineral phase composition and multi-metal coexistence has not been reported, so the oxidation of this type of minerals It is of great significance to study the efficient extraction of valuable metals by leaching

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
  • Method for extracting valuable metal from copper nickel sulfide through ammonium persulfate-sulfuric acid oxidation leaching
  • Method for extracting valuable metal from copper nickel sulfide through ammonium persulfate-sulfuric acid oxidation leaching
  • Method for extracting valuable metal from copper nickel sulfide through ammonium persulfate-sulfuric acid oxidation leaching

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1-1

[0106] A copper-nickel sulfide ammonium persulfate-sulfuric acid oxidation leaching method for extracting valuable metals, its process flow chart is as follows figure 1 shown, including the following steps:

[0107] Step 1: Crushing and screening

[0108] The copper-nickel sulfide ore is crushed, ball-milled, and passed through a 180-200-mesh sieve to obtain copper-nickel sulfide ore powder with a particle size of 75-80 μm. The main metal elements and their mass percentage contents of copper-nickel sulfide ore are shown in Table 1.

[0109] Table 1 Composition and mass percentage of main metal elements of copper-nickel sulfide ore

[0110]

[0111] Step 2: Oxidation Leaching

[0112] Weigh 15g of the sieved copper-nickel sulfide ore powder and pour it into the reaction vessel, add the mixed solution of ammonium persulfate and sulfuric acid according to the liquid-solid ratio (ml:g) 20:1, the concentration of sulfuric acid in the mixed solution is 0.3mol / L, the amount o...

Embodiment 1-2

[0119] A copper-nickel sulfide ammonium persulfate-sulfuric acid oxidation leaching method for extracting valuable metals, the steps are the same as in Example 1, the difference is that, using mode two, ammonium persulfate adopts the method of adding in batches in the oxidation leaching process, and first reacts A container with a mass of m 1 The mixed solution of ammonium persulfate and sulfuric acid, m 1 It is 30% of the total mass of ammonium persulfate, and the mixed solution is mixed evenly with copper-nickel sulfide ore powder. Then, under the condition that the mechanical stirring speed is 500r / min, the heating is turned on, and at the same time, the mass is m 2 A saturated solution of ammonium persulfate (solubility 80g / 100ml), where m 2 It is 70% of the total mass of ammonium persulfate. When the reaction temperature reached 80°C, time the reaction for 3 hours. As a result of the metal extraction rate, the extraction rate of Ni was 95.8%, the extraction rate of Cu...

Embodiment 2-1

[0121] A copper-nickel sulfide ammonium persulfate-sulfuric acid oxidation leaching method for extracting valuable metals, comprising the following steps:

[0122] Step 1: Crushing and screening

[0123]The copper-nickel sulfide ore is crushed, ball-milled, and passed through a 160-180-mesh sieve to obtain copper-nickel sulfide ore powder with a particle size of 80-96 μm. The main metal elements and their mass percentage contents of copper-nickel sulfide ore are shown in Table 2.

[0124] Table 2 Composition and mass percentage of main metal elements of copper-nickel sulfide ore

[0125]

[0126] Step 2: Oxidation Leaching

[0127] Take by weighing copper-nickel sulfide ore powder 15g after screening and pour in reaction vessel, take by weighing the total mass of ammonium persulfate according to 3 times of the required ammonium persulfate quality that all metals in copper-nickel sulfide ore react completely with ammonium persulfate. Then add to the reaction vessel by mas...

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 discloses a method for extracting valuable metal from copper nickel sulfide through ammonium persulfate-sulfuric acid oxidation leaching. The method comprises the steps of screening low-grade copper nickel sulfide raw materials to obtain copper nickel sulfide mineral powder, according to the proportion, taking ammonium persulfate and sulfuric acid raw materials, adopting one (1) of the two manners in the ammonium persulfate to be completely mixed with sulfuric acid to form a mixture, and then uniformly mixing the mixture with mineral powder according to the proportion; and secondly, enabling the ammonium persulfate to be partly mixed with the sulfuric acid, partly making a saturated solution, under the specific temperature and system pH, performing a constant-temperature leaching reaction, in the leaching process, adding a saturated ammonium persulfate solution, finishing leaching and filtering, and obtaining leaching liquid, wherein the extraction rate of valuable metalNi in the leaching liquid is 90.4 to 97.5%, the extraction rate of Cu is 93.4 to 99.9%, and the extraction rate of Co is 92.7 to 99.6%. The method is low in leaching temperature, low in sulfuric acidconcentration, small in use amount, simple in process flow, and wide in application range, ore raw materials are limited by areas, ore, grade and the like, the extraction rate of the valuable metal ishigher, and no SO2 is emitted.

Description

Technical field: [0001] The invention belongs to the technical field of non-ferrous metal metallurgy, and in particular relates to a copper-nickel sulfide ammonium persulfate-sulfuric acid oxidation leaching method for extracting valuable metals. Background technique: [0002] Nickel is an important strategic metal, mainly distributed in sulfide nickel ore and oxidized nickel ore resources. Among them, sulfide-type nickel ore is the main resource for nickel production because of its good quality and mature smelting technology. In recent years, with the increasing demand for nickel in the world, the exploitable high-grade nickel sulfide ore resources are increasingly exhausted, and low-grade copper-nickel sulfide nickel ore has become the key development target of the nickel industry. [0003] Low-grade copper-nickel sulfide ore is a thick mixed ore zone between the primary sulfide ore lean body and the upper oxidation zone, accompanied by a large amount of copper and cobalt...

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
IPC IPC(8): C22B3/08C22B3/22C22B23/00C22B15/00C22B26/22
CPCC22B3/08C22B3/22C22B23/043C22B23/0453C22B15/0071C22B15/0086C22B26/22Y02P10/20
Inventor 牟文宁田蓓金程皓罗绍华辛海霞
Owner 东北大学秦皇岛分校
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