Dezincification plant, method for operating dezincification plant, and hydrometallurgical method for nickel oxide ore

Patent metadata

Field	Value
Publication number	US-9945007-B2
Application number	US-201314382632-A
Country	US
Kind code	B2
Filing date	Mar 1, 2013
Priority date	Mar 6, 2012
Publication date	Apr 17, 2018
Grant date	Apr 17, 2018

Abstract

The present invention provides a hydrometallurgical method for nickel oxide ore, wherein the plant can be smoothly started up without imposing a load onto a filter cloth for a separation treatment of zinc sulfide, and the amount of residual zinc in a mother liquor for nickel recovery can be reduced to 1 mg/L. In the plant start-up after the completion of a periodic inspection, a post-neutralization solution is controlled to return to a neutralization reaction tank via circulation piping by adjustment of a switching valve in flow piping without sulfurizing post-neutralization solution. When the flow rate and/or the temperature of the post-neutralization solution circulated reaches a predetermined value, a sulfurization treatment is applied to the post-neutralization solution in the dezincification reaction tank to form zinc-sulfide-containing mother liquor for nickel recovery and adjust the switching valve. Zinc-sulfide-containing mother liquor for nickel recovery is transferred to a filter apparatus via transfer piping.

First claim

The invention claimed is:

1. A dezincification plant, adapted for use in a hydrometallurgical method for nickel oxide ore, in which a dezincification step is carried out in said plant, the method comprising applying a sulfurization treatment to a post-neutralization solution obtained through a neutralization step of neutralizing a leachate of said nickel oxide ore thereby to form zinc sulfide, and said zinc sulfide is separated to obtain a mother liquor containing nickel and cobalt for nickel recovery, the dezincification plant comprising:
a dezincification reaction tank configured to form zinc sulfide by applying a sulfurization treatment to the post-neutralization solution and form a mother liquor containing said zinc sulfide;
a filter apparatus configured to separate the zinc sulfide and the mother liquor; and
a holding tank A configured to hold the zinc-sulfide-containing mother liquor,
flow piping A connected to the holding tank A for transferring said zinc-sulfide-containing mother liquor to the filter apparatus, the flow piping A being both coupled to transfer piping A connected to said filter apparatus, and coupled to circulation piping A for circulating the zinc-sulfide-containing mother liquor back to the dezincification reaction tank, at a branch point A, and a switching valve A is installed at said branch point A for switching flow through the flow piping A to the transfer piping A or to the circulation piping A,
and a measurement portion to measure a flow rate and/or a temperature of a solution flowing through flow piping A provided therein,
wherein the dezincification plant is periodically shut down and inspected, and in start-up of the dezincification plant after completion of the periodic inspection, at a time of starting the start-up, before applying a sulfurization treatment to the post-neutralization solution, said post-neutralization solution is controlled by adjustment of the switching valve A so as to be circulated to the dezincification reaction tank via the circulation piping A, and, when a flow rate and/or a temperature of the post-neutralization solution circulated reach a predetermined value or more, a sulfurization treatment is applied to the post-neutralization solution in the dezincification reaction tank thereby to form the zinc-sulfide-containing mother liquor, and said zinc-sulfide-containing mother liquor is transferred to the filter apparatus via the transfer piping A by adjustment of the switching valve A.

2. A method for operating a dezincification plant,
the dezincification plant comprising:
a dezincification reaction tank configured to form zinc sulfide by applying a sulfurization treatment to the post-neutralization solution and form a mother liquor containing said zinc sulfide;
a filter apparatus configured to separate the zinc sulfide and the mother liquor; and
a holding tank A configured to hold the zinc-sulfide-containing mother liquor,
flow piping A connected to the holding tank A for transferring said zinc-sulfide-containing mother liquor to the filter apparatus, the flow piping A being both coupled to transfer piping A connected to said filter apparatus, and coupled to circulation piping A for circulating the zinc-sulfide-containing mother liquor back to the dezincification reaction tank, at a branch point A, and a switching valve A is installed at said branch point A for switching flow through the flow piping A to the transfer piping A or to the circulation piping A,
and a measurement portion to measure a flow rate and/or a temperature of a solution flowing through flow piping A provided therein,
the dezincification plant being adapted for use in a dezincification step in a hydrometallurgical method for nickel oxide ore, in which a dezincification step is carried out in said plant, the method comprising applying a sulfurization treatment to a post-neutralization solution obtained through a neutralization step of neutralizing a leachate of said nickel oxide ore thereby to form zinc sulfide, and said zinc sulfide is separated thereby to obtain a mother liquor containing nickel and cobalt for nickel recovery,
wherein, as part of said method, the dezincification plant is periodically shut down and inspected, and in start-up of the dezincification plant after completion of the periodic inspection, at a time of starting the start-up, before applying a sulfurization treatment to the post-neutralization solution, said post-neutralization solution is controlled by adjustment of the switching valve A so as to be circulated to the dezincification reaction tank via the circulation piping A, and, when a flow rate and/or a temperature of the post-neutralization solution circulated reach a predetermined value or more, a sulfurization treatment is applied to the post-neutralization solution in the dezincification reaction tank thereby to form the zinc-sulfide-containing mother liquor, and said zinc-sulfide-containing mother liquor is transferred to the filter apparatus via the transfer piping A by adjustment of the switching valve A.

3. A hydrometallurgical method for nickel oxide ore, the hydrometallurgical method comprising:
a neutralization step of neutralizing a leachate obtained by leaching nickel oxide ore to obtain a neutralized precipitate containing an impurity and a post-neutralization solution containing zinc as well as nickel and cobalt; and
a dezincification step of applying a sulfurization treatment to said post-neutralization solution to form zinc sulfide and separating said zinc sulfide to obtain a mother liquor for nickel recovery, the mother liquor containing nickel and cobalt and carried out by the method for operating a dezincification plant according to claim 2 .

4. The hydrometallurgical method for nickel oxide ore according to claim 3 ,
wherein a neutralization plant configured to perform a neutralization treatment in the neutralization step comprises:
a neutralization reaction tank configured to perform a neutralization reaction of the leachate;
a separation treatment tank configured to add a flocculant to a slurry obtained after the neutralization reaction to separate into a neutralized precipitate and a post-neutralization solution; and
a holding tank B configured to hold the post-neutralization solution transferred from the separation treatment tank,
wherein flow piping B is connected to said holding tank B, the flow piping B being branched at a predetermined point B provided with a switching valve B, and, at said branched point B, the flow piping B being coupled to transfer piping B configured to transfer the post-neutralization solution to the dezincification reaction tank in the dezincification step and circulation piping B configured to return said post-neutralization solution to the neutralization reaction tank to circulate the post-neutralization solution,
wherein, in the neutralization plant in the neutralization step, in start-up of the dezincification plant after completion of the periodic inspection thereof, at a time of starting the start-up, the post-neutralization solution is controlled to be returned to the neutralization reaction tank by adjustment of the switching valve B, and, when a flow rate and/or a temperature thereof measured in the measurement portion installed in the dezincification plant reaches a predetermined value or more, the post-neutralization solution is transferred to the dezincification reaction tank via the transfer piping B by adjustment of the switching valve B.

5. The hydrometallurgical method for nickel oxide ore according to claim 3 , the hydrometallurgical method comprising:
a leaching step of adding sulfuric acid to a slurry of the nickel oxide ore to perform leaching under high temperature and high pressure;
a solid-liquid separation step of separating a residue by multistage washing of a leached slurry

Assignees

• Sumitomo Metal Mining Co

Inventors

• Mitsui Hiroyuki
• Nakai Osamu
• Matsubara Satoshi

Classifications

• C22B23/0461

  by chemical methods · CPC title

• C22B3/04 Primary

  by leaching (C22B3/18 takes precedence) · CPC title

• C22B23/0469

  by chemical substitution, e.g. by cementation · CPC title

• Y02P10/234

  Cross-Sectional Technologies · mapped topic

• C22B23/043 Primary

  Sulfurated acids or salts thereof · CPC title