Removal method of manganese from waste water

Patent metadata

Field	Value
Publication number	US-9657370-B2
Application number	US-99901710-A
Country	US
Kind code	B2
Filing date	Feb 23, 2010
Priority date	Mar 9, 2009
Publication date	May 23, 2017
Grant date	May 23, 2017

Abstract

A removal method of manganese in which manganese is removed by precipitating manganese selectively from sulfuric acid waste water containing aluminum, magnesium and manganese with inhibiting the precipitation of magnesium.
The removal method of manganese from waste water in which manganese is removed by precipitating manganese selectively from the sulfuric acid waste water containing aluminum, magnesium and manganese with inhibiting the precipitation of magnesium, characterized in that said waste water is subjected to the following steps (1) and (2).
(1) First, aluminum in said waste water is removed. (2) Subsequently, neutralizing agent is added into the wastewater after removing aluminum, then pH of the waste water is adjusted at 8.0 to 9.0, and oxygen gas is blown.

First claim

What is claimed is:

1. A method of removing manganese from a sulfuric acid waste water in which manganese is removed by precipitating manganese selectively from the sulfuric acid waste water containing aluminum, magnesium and manganese, comprising:
(1) First, removing aluminum from said sulfuric acid waste water so that a concentration of aluminum is 0.1 g/L or less;
(2) Subsequently, adding neutralizing agent into the sulfuric acid waste water after removing aluminum and adjusting a pH value of the sulfuric acid waste water to no less than 8.0 and less than 9.0; and
(3) adding oxygen gas with a purity of 98 volume % or more into the sulfuric acid waste water,
wherein manganese is precipitated in steps (2) and (3), and
wherein in step (2), the pH value of the sulfuric acid waste water is adjusted to reach an equilibrium by adding neutralizing agent, prior to step (3) of adding the oxygen gas into the sulfuric acid waste water under a pressure load of 0.10 MPa to 0.20 MPa.

2. The method of removing manganese from the sulfuric acid waste water according to claim 1 , wherein in step (1) a pH value of the sulfuric acid waste water is adjusted to 4.0 to 6.0 by adding calcium carbonate or calcium hydroxide as a neutralizing agent.

3. The method of removing manganese from the sulfuric acid waste water according to claim 1 , wherein a pressurized vessel is used when adding oxygen gas into the sulfuric acid waste water in step (3).

4. The method of removing manganese from the sulfuric acid waste water according to claim 1 ,
wherein said sulfuric acid waste water is obtained from a sulfide precipitation step;
wherein the sulfide precipitation step is a step in a hydrometallurgical process in which nickel and cobalt are recovered from nickel oxide ore by High Pressure Acid Leach, comprising a leaching step in which a leach solution is obtained by leaching nickel oxide ore with sulfuric acid; and the sulfide precipitation step in which sulfides of nickel and cobalt are separated and recovered by adding hydrogen sulfide gas into a mother liquid obtained by neutralizing the leach solution.

5. The method of removing manganese from the sulfuric acid waste water according to claim 4 , wherein in step (1) a pH value of the sulfuric acid waste water is adjusted to 4.0 to 6.0 by adding calcium carbonate or calcium hydroxide as a neutralizing agent.

6. The method of removing manganese from the sulfuric acid waste water according to claim 4 , wherein in step (2), the pH value of the sulfuric acid waste water is adjusted to a range of 8.0 to 9.0 by adding neutralizing agent, prior to step (3) of adding oxygen gas into the sulfuric acid waste water.

7. The method of removing manganese from the sulfuric acid waste water according to claim 4 , wherein a pressurized vessel is used when adding oxygen gas into the sulfuric acid waste water in step (3).

8. The method of removing manganese from the sulfuric acid waste water according to claim 1 , wherein in step (2), the pH value of the sulfuric acid waste water is adjusted to a range of 8.0 to 9.0 by adding neutralizing agent, prior to step (3) of adding oxygen gas into the sulfuric acid waste water.

Assignees

• Kobayashi Hiroshi
• Toki Norihisa
• Shoji Hirofumi
• Kudo Keiji
• Higaki Tatsuya
• Sumitomo Metal Mining Co

Inventors

• Kobayashi Hiroshi
• Toki Norihisa
• Shoji Hirofumi
• Kudo Keiji
• Higaki Tatsuya

Classifications

• C22B3/44

  by chemical processes (treatment or purification of solutions by liquid-liquid extraction C22B3/26, by ion-exchange extraction C22B3/42) · CPC title

• C22B47/00

  Obtaining manganese · CPC title

• C02F2209/06

  pH · CPC title

• Y02P10/234

  Cross-Sectional Technologies · mapped topic

• C22B23/0461

  by chemical methods · CPC title