IP Library Granted Patent US 9,617,621
Granted Patent B2
US 9,617,621 · App. 13/878,025 · Granted Apr 11, 2017

Method for treating a solution containing zinc sulphate

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Quick Facts
Patent No.
US 9,617,621
App. No.
13/878,025
Granted
Apr 11, 2017
Kind
B2
Abstract

The invention relates to a method for treating a solution containing zinc sulphate, so that at least one of the rare metals such as indium, gallium and germanium can be separated from it. A portion of the metals to be separated can be precipitated from zinc sulphate solution by neutralizing the acidic solution and at least a portion is cemented by means of metal powder. The solid precipitates that are formed can be combined and treated subsequently in some suitable way to leach out the desired metals.

Claims (11)

1. A method for treating an acidic solution containing zinc sulphate in order to separate at least one metal or compounds of them in solution from the acidic solution containing zinc sulphate, whereby the metal to be separated is one of the group of indium, gallium and germanium, wherein the acidic solution containing zinc sulphate is neutralised in a pre-neutralisation stage to a pH value of 2.5-3.5 and wherein a precipitate formed in the pre-neutralisation stage is separated from the acidic solution containing zinc sulphate by solids-liquid separation and a precipitate obtained from the solids-liquid separation is subjected to a precipitate scrubbing and leaching stage and at least one of the group of metals or compounds of them to be separated is separated from the acidic solution containing zinc sulphate obtained from the solids-liquid separation in a cementation stage by means of zinc powder.

2. The method according to claim 1 , wherein the precipitate formed in the pre-neutralisation stage contains a first portion of the gallium and indium of the acidic solution containing zinc sulphate.

3. The method according to claim 1 , wherein the acidic solution containing zinc sulphate also contains copper, which is cemented from the solution in the cementation stage.

4. The method according to claim 1 , wherein in the cementation stage, the germanium contained in solution is cemented from the acidic solution containing zinc sulphate.

5. The method according to claim 2 , wherein in the cementation stage, a second portion of the indium contained in solution is cemented from the acidic solution containing zinc sulphate.

6. The method according to claim 2 , wherein in the cementation stage, a second portion of the gallium contained in solution is precipitated from the acidic solution containing zinc sulphate.

7. The method according to claim 1 , wherein the metals or compounds of them that were separated from the acidic solution containing zinc sulphate in the cementation stage are separated from solution by solids-liquid separation and the metals separated are subjected to the precipitate scrubbing and leaching stage.

8. The method according to claim 6 , wherein, after cementation, the solution containing zinc sulphate containing gallium is subjected to a gallium precipitation stage, in which the solution is neutralised to a pH value of 3.2-4.0 in order to precipitate a third portion of the gallium.

9. The method according to claim 1 , wherein a precipitate formed in a gallium precipitation stage is subjected to the precipitate scrubbing and leaching stage.

10. The method according to claim 1 , wherein the precipitate formed in the pre-neutralisation stage, a precipitate formed in the cementation stage and a precipitate formed in a gallium precipitation stage are treated jointly with an acid-containing solution in the precipitate scrubbing and leaching stage in order to leach metals to be separated and to separate them from a metallic copper deposit.

11. A method for treating an acidic solution containing zinc sulphate in order to separate at least one metal or compounds of them in solution from the acidic solution containing zinc sulphate, whereby the metal to be separated is one of the group of indium, gallium and germanium, wherein the acidic solution containing zinc sulphate is neutralised in a pre-neutralisation stage to a pH value of 2.5-3.5 and wherein a precipitate formed in the pre-neutralisation stage is separated from the solution containing zinc sulphate by solids-liquid separation and the separated precipitate is subjected to a precipitate scrubbing and leaching stage and wherein a precipitate is formed in a cementation stage and the precipitate is contained in the acidic solution containing zinc sulphate and subjected to a gallium precipitation stage.

Assignments (4)
CHANGE OF NAME Recorded Sep 22, 2025
From: METSO OUTOTEC FINLAND OY
To: METSO FINLAND OY
Reel/Frame 072925/0070 →
NUNC PRO TUNC ASSIGNMENT Recorded Aug 21, 2023
From: OUTOTEC OYJ
To: OUTOTEC (FINLAND) OY
Reel/Frame 064644/0168 →
MERGER AND CHANGE OF NAME Recorded Aug 21, 2023
From: OUTOTEC (FINLAND) OY; METSO MINERALS OY
To: METSO OUTOTEC FINLAND OY
Reel/Frame 064644/0186 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 29, 2013
From: SALMINEN, JUSTIN; RIIHIMAKI, TEPPO; RUONALA, MIKKO
To: OUTOTEC OYJ
Reel/Frame 030501/0122 →