Copper nickel sulfide ammonium persulfate-sulfuric acid oxidation leaching method for extracting valuable metals

A technology of ammonium persulfate and valuable metals, applied in the field of non-ferrous metallurgy, can solve the problems of environmental pollution, increase of recycling cost, increase of cost, etc., and achieve the effect of protecting the environment, strong applicability, and avoiding SO2 emissions

Active Publication Date: 2022-02-01
东北大学秦皇岛分校
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AI Technical Summary

Problems solved by technology

In order to increase the leaching rate of copper, Fan Xingxiang et al. studied the process of leaching chalcopyrite with silver ion catalysis and ammonium persulfate. The mineral powder with a particle size of -74+58 μm was reacted 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 generate 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

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  • Copper nickel sulfide ammonium persulfate-sulfuric acid oxidation leaching method for extracting valuable metals
  • Copper nickel sulfide ammonium persulfate-sulfuric acid oxidation leaching method for extracting valuable metals
  • Copper nickel sulfide ammonium persulfate-sulfuric acid oxidation leaching method for extracting valuable metals

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Experimental program
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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 the second method is adopted, and the ammonium persulfate is added in batches during the oxidation leaching process, and the first reaction 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. The results of the metal extraction rate were as follows: the extraction rate of Ni was 95.8...

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] Weigh 15 g of the sieved copper-nickel sulfide ore powder and pour it into a reaction vessel, and weigh the total mass of ammonium persulfate according to 3 times the mass of ammonium persulfate required for the complete reaction of all metals in the copper-nickel sulfide ore with ammonium persulfate. Then add to the reaction vessel by mass m ...

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Abstract

The copper-nickel sulfide ammonium persulfate-sulfuric acid oxidation leaching method for extracting valuable metals of the present invention comprises the following steps: sieve the low-grade copper-nickel sulfide raw material to obtain copper-nickel sulfide mineral powder, and take ammonium persulfate and sulfuric acid raw materials in proportion , ammonium persulfate adopts one of two methods (1) after mixing all of it with sulfuric acid, mix it with mineral powder in proportion; (2) mix part of ammonium persulfate with sulfuric acid, and partly make a saturated solution; The constant temperature leaching reaction is carried out under the temperature and system pH. The saturated ammonium persulfate solution is added during the leaching process, and the leaching and filtration are completed to obtain a leaching solution. The extraction rate of valuable metal Ni in the leaching solution is 90.4-97.5%, and the extraction rate of Cu is 93.4-99.9%. The Co extraction rate is 92.7‑99.6%. This method has low leaching temperature, low concentration of sulfuric acid, less dosage, simple process flow, wide application range, ore raw materials are not limited by region, ore position, grade, etc.; the extraction rate of valuable metals is high, and there is no SO 2 emission.

Description

Technical field: [0001] The invention belongs to the technical field of nonferrous metal metallurgy, and in particular relates to a method for extracting valuable metals by oxidation leaching of copper nickel sulfide ammonium persulfate-sulfuric acid. 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 mineable high-grade sulfide-type nickel ore resources are increasingly exhausted, and low-grade copper-nickel sulfide-type 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 coppe...

Claims

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Application Information

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Patent Type & Authority Patents(China)
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
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