Method for extracting valuable metal from low-matte nickel converter slag

Patent metadata

Field	Value
Publication number	US-12018346-B2
Application number	US-202218260235-A
Country	US
Kind code	B2
Filing date	Jun 6, 2022
Priority date	Jul 21, 2021
Publication date	Jun 25, 2024
Grant date	Jun 25, 2024

Abstract

Disclosed in the present invention is a method for extracting valuable metal from low-matte nickel converter slag. The method comprises: mixing low-matte nickel converter slag and quicklime then calcinating, obtaining a calcinated material; grinding and magnetically separating the calcinated material, obtaining silicate and iron-rich slag; adding a strong alkali solution to the iron-rich slag to perform leaching processing, and performing solid-liquid separation, obtaining a filtrate and a residue; mixing the residue with an acid solution, performing oxygen pressure acid leaching, and performing solid-liquid separation, obtaining a leachate and iron oxide; introducing hydrogen sulfide gas into the leachate, adjusting the pH, and performing solid-liquid separation, obtaining a copper sulfide precipitate and a nickel-cobalt-containing filtrate. In the present invention, first, removing silicon dioxide is removed by means of calcination to prepare silicate, then iron oxide is prepared by means of acid leaching, and finally metal separation is performed on the leachate, causing various components of the converter slag to be effectively utilized. The process flow of the present invention is short and effectively utilizes each component of the low-matte nickel converter slag, waste is turned into valuable material, and the loss of valuable metal elements is reduced.

First claim

What is claimed is:

1. A method for extracting a valuable metal from a low nickel matte converter slag, comprising the following steps:
S1: mixing a low nickel matte converter slag with quicklime, then roasting to obtain a roasted material; the low nickel matte converter slag contains FeSiO 3 ; a mass ratio of the quicklime and the low nickel matte converter slag is (0.1-0.3):1; a temperature of the roasting is 800° C. to 1350° C.; and a time of the roasting is 0.5 h to 2.0 h;
S2 performing a grinding and a magnetic separation to the roasted material to obtain a silicate and an iron-rich slag;
S3: adding a strong alkali solution to the iron-rich slag for a leaching treatment, and performing a solid-liquid separation to obtain a filtrate and a filter residue; the strong alkali solution has a concentration of 0.1 mol/L to 4.0 mol/L; and a time of the leaching treatment is 0.5 h to 3.0 h;
S4: mixing the filter residue with an acid solution to perform an oxidative pressure acid leaching, then performing a solid-liquid separation to obtain a leaching solution and an iron oxide red; a solid-to-liquid ratio of the filter residue and the acid solution is 1 g: (0.5-5) mL; the oxidative pressure acid leaching has an oxygen partial pressure of 350 kPa to 700 kPa, a temperature of 160° C. to 225° C., and a pH of 2.0 to 3.0;
S5: introducing a hydrogen sulfide gas into the leaching solution, adjusting pH, then performing a solid-liquid separation to obtain a copper sulfide precipitate and a nickel-cobalt-containing filtrate;
wherein a mass content of nickel in the low nickel matte converter slag is 0.93 wt % to 1.38 wt %.

2. The method according to claim 1 , wherein in step S2, the roasted material after grinding has a particle size of ≤100 μm; a magnetic field intensity of the magnetic separation is 500 GS to 1500 GS.

3. The method according to claim 1 , wherein in step S5, the pH is 0 to 2.0.

4. The method according to claim 1 , wherein in step S5, an adjusting agent for adjusting pH is one or more of sulfuric acid, nickel hydroxide, nickel carbonate, cobalt hydroxide or cobalt carbonate.

5. The method according to claim 1 , wherein in step S5, further comprising an extraction process and a back-extraction process to the nickel-cobalt-containing filtrate: adding an extractant to the nickel-cobalt-containing filtrate, then separating to obtain an extracted nickel-containing organic phase and a cobalt-containing raffinate, and then back-extracting nickel from the extracted nickel-containing organic phase with a sulfuric acid solution to obtain a nickel sulfate solution.

Assignees

• Guangdong Brunp Recycling Technology Co Ltd
• Hunan Brunp Recycling Tech Co Ltd
• Hunan Brunp Ev Recycling Co Ltd

Inventors

• Yu Haijun
• Xie Yinghao
• Li Aixia
• Zhang Xuemei
• Li Changdong

Classifications

• Y02P10/20

  Recycling · CPC title

• C22B3/20

  Treatment or purification of solutions, e.g. obtained by leaching (C22B3/18 takes precedence) · CPC title

• C22B1/02 Primary

  Roasting processes (C22B1/16 takes precedence) · CPC title

• C22B23/00

  Obtaining nickel or cobalt · CPC title

• C22B15/0063

  Hydrometallurgy · CPC title