IP Library Granted Patent US 9,359,657
Granted Patent B2
US 9,359,657 · App. 14/357,150 · Granted Jun 7, 2016

Method for leaching a sulphidic metal concentrate

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Quick Facts
Patent No.
US 9,359,657
App. No.
14/357,150
Granted
Jun 7, 2016
Kind
B2
Abstract

A method for leaching a sulfidic metal concentrate in hydrometallurgical production of metal in a leaching process from which hot water vapor containing off-gas is conducted out and to which an acid solution warmed up to an elevated temperature is conducted. The acid solution is warmed up to an elevated temperature by bringing off-gas of the leaching step into direct contact with the acid solution.

Claims (11)

1. A method for leaching a sulfidic metal concentrate in hydrometallurgical production of metal using a leaching process, from which process water vapor containing off-gas is conducted out and to which process an acid solution warmed to an elevated temperature is conducted, characterized in that the acid solution is warmed by bringing off-gas of the leaching process into direct contact with the acid solution.

2. The method according to claim 1 , characterized in that the acid solution is warmed by providing it as droplets in the off-gas, the off-gas being present as a continuous phase.

3. The method according to claim 2 , characterized in that the acid solution is sprayed in the off-gas through a nozzle forming droplets in a device where the off-gas and the acid solution move against a flow.

4. The method according to claim 2 , characterized in that the off-gas and the acid solution are brought into mutual contact by an ejector/venturi technique.

5. The method according to claim 1 , characterized in that the acid solution is warmed by dispersing the off-gas in the acid solution, the acid solution being present as a continuous phase.

6. The method according to claim 5 , characterized in that the off-gas is dispersed in a sulfuric acid solution.

7. The method according to claim 1 , characterized in that the temperature of the water vapor in the off-gas of the leaching process is approximately 100° C.

8. The method according to claim 1 , characterized in that the acid solution is warmed up to between approximately 50° C. to approximately 80° C. by means of the off-gas.

9. The method according to claim 1 , characterized in that the metal is zinc and the acid is sulfuric acid.

10. The method according to claim 1 , characterized in that the acid solution is a return acid obtained from electrolysis.

11. The method according to claim 1 , characterized in that the method comprises at least one first acid leaching step from which water vapor containing off-gas is conducted out, and thereafter at least one second acid leaching step, where before being conducted to the second acid leaching step, the acid solution is warmed by bringing off-gas of the first acid leaching step into direct contact with the acid solution to be conducted to the second acid leaching step.

Assignments (4)
CHANGE OF NAME Recorded Sep 22, 2025
From: METSO OUTOTEC FINLAND OY
To: METSO FINLAND OY
Reel/Frame 072924/0266 →
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 Jun 26, 2014
From: HAAKANA, TIMO; SAXEN, BJORN
To: OUTOTEC OYJ
Reel/Frame 033186/0703 →