Nickel recovery process

Patent metadata

Field	Value
Publication number	US-10344354-B2
Application number	US-201515503430-A
Country	US
Kind code	B2
Filing date	Jul 23, 2015
Priority date	Aug 13, 2014
Publication date	Jul 9, 2019
Grant date	Jul 9, 2019

Abstract

A nickel recovery process capable of decreasing nickel remaining in a byproduct by recovering nickel from the byproduct of electrolytic nickel manufacturing process by chlorine-leaching, and also, capable of simplifying a cementation step simultaneously, is provided. In a nickel recovery step S60, a nickel recovery step S70 and a nickel recovery step S80, nickel is recovered in each step from S0 slurry, residue flaker and chlorine-leached residue, which are byproducts of electrolytic nickel manufacturing process by chlorine-leaching, by using an aqueous solution containing 80 g/L to 390 g/L of chlorine and 30 g/L to 70 g/L of copper.

First claim

The invention claimed is:

1. A nickel recovery process for recovering nickel from a byproduct of an electrolytic nickel manufacturing process, comprising:
a chlorine-leaching step including oxidizing and leaching nickel sulfide to obtain a chlorine leachate and a chlorine-leached residue;
a cementation step including fixing copper in the chlorine leachate to remove copper from the chlorine leachate;
a sulfur recovery step including making the chlorine-leached residue into a first slurry in a melting tank, followed by performing a solid-liquid separation to obtain a sulfur-containing solution and a residue; and
a nickel recovery step including: (a) mixing the byproduct, which contains 5 wt % to 20 wt % of nickel, with an aqueous solution having: (i) a dissolved chlorine amount of 80 g/L to 390 g/L, and (ii) a copper concentration of 30 g/L to 70 g/L to obtain a second slurry, and (b) performing a solid-liquid separation to separate the second slurry into a solid phase and a liquid phase,
wherein the liquid phase is returned into a transportation path from the chlorine-leaching step to the cementation step.

2. The nickel recovery process according to claim 1 , wherein the second slurry obtained from the nickel recovery step has a solid content of from 130 g/L to 350 g/L.

3. The nickel recovery process according to claim 1 , wherein the solid phase is returned into the cementation step, and the byproduct is slurry repulped from the residue in the sulfur recovery step.

4. The nickel recovery process according to claim 1 , wherein the second slurry is returned into the cementation step without the solid-liquid separation, and the byproduct is slurry repulped from the residue in the sulfur recovery step.

5. The nickel recovery process according to claim 1 , wherein the solid phase is discharged out of a system of the electrolytic nickel manufacturing process, and the byproduct is a chlorine-leached residue: (i) obtained from the sulfur recovery step, and (ii) adhered to an inner wall of the melting tank.

6. The nickel recovery process according to claim 1 , wherein the solid phase is returned into the sulfur recovery step, and the byproduct is a part of the chlorine-leached residue obtained from the chlorine-leaching step.

7. The nickel recovery process according to claim 1 , wherein the chlorine leachate obtained from the chlorine-leaching step is used instead of the aqueous solution.

8. The nickel recovery process according to claim 1 , wherein the byproduct includes the residue obtained in the sulfur recovery step.

Assignees

• Sumitomo Metal Mining Co

Inventors

• Shoji Hirofumi
• Hayata Jiro
• Kudou Keiji
• Higaki Tatsuya

Classifications

• Y02P10/20

  Recycling · CPC title

• C22B23/0407 Primary

  Leaching processes · CPC title

• C22B23/0423

  Halogenated acids or salts thereof · CPC title

• C25C1/08

  of nickel or cobalt · CPC title

• C22B7/007

  by acid leaching · CPC title