Method for shortening operation shutdown time of high pressure acid leach equipment in a hydrometallurgical process

Patent metadata

Field	Value
Publication number	US-9719153-B2
Application number	US-201314063403-A
Country	US
Kind code	B2
Filing date	Oct 25, 2013
Priority date	Jul 31, 2008
Publication date	Aug 1, 2017
Grant date	Aug 1, 2017

Abstract

This invention provides a method for shortening operation shutdown time of high pressure acid leach equipment in a hydrometallurgical process, wherein the high pressure acid leach equipment comprises (i) means to transfer an ore slurry into the high pressure acid leach equipment;(ii) means to increase temperature and pressure of an ore slurry before leaching; (iii) means to add sulfuric acid into the high pressure acid leach equipment and to leach the ore slurry to obtain a leached slurry at high temperature under high pressure; (iv) means to adjust the pressure of the leached slurry; and (v) means to discharge the leached from the high pressure acid leach equipment; wherein, upon operation shutdown of the high pressure acid leach equipment, the leached slurry is subjected to self-circulation inside the high pressure acid leach equipment.

First claim

What is claimed is:

1. A method for shortening operation shutdown time of high pressure acid leach equipment in a hydrometallurgical process, wherein the high pressure acid leach equipment comprises
(i) a first piping, wherein the first piping is used to transfer an ore slurry into the high pressure acid leach equipment;
(ii) a multistage heater, wherein the multistage heater is used stepwise to increase temperature and pressure of the ore slurry before leaching or a leached slurry;
(iii) an autoclave, wherein the autoclave is used to add sulfuric acid to the ore slurry with temperature and pressure increased by the multistage heater (ii) and to leach the ore slurry to obtain a leached slurry at high temperature under high pressure;
(iv) a multistage flash tank to adjust the pressure of the leached slurry;
(v) a second piping, wherein the second piping is used to discharge the leached slurry from the high pressure acid leach equipment; and
(vi) a piping for self-circulation, wherein the piping for self-circulation is used to discharge the leached slurry from the multistage flash tank (iv) to transfer the leached slurry to the multistage heater (ii);
wherein, in case of operation shutdown of the high pressure acid leach equipment, the leached slurry is subjected to self-circulation inside the high pressure acid leach equipment by transferring the leached slurry from the autoclave (iii) through the multistage flash tank (iv) and the piping for self-circulation (vi) to the multistage heater (ii), so that the high temperature and high pressure atmosphere of the autoclave (iii) is held.

2. The method according to claim 1 , wherein the self-circulation of the leach slurry is achieved by:
shutdown of the transfer of the ore slurry through the first piping (i),
shutdown of the addition of sulfuric acid autoclave (iii), and
shutdown of the discharge of the leached slurry in the second piping (v); and
discharging the leached slurry from the multistage flash tank (iv) to transfer the leached slurry through the piping for self-circulation (vi) to the multistage heater (ii).

3. The method according to claim 1 , wherein the pH of the leached slurry inside the high pressure acid leach equipment is adjusted at 3.0 to 5.0.

4. The method according to claim 1 , wherein the temperature of the autoclave (iii) is 200 to 260° C.

5. The method according to claim 1 , wherein the operation shutdown time is within 12 hours.

6. The method according to claim 2 , wherein the pH of the leached slurry inside the high pressure acid leach equipment is adjusted at 3.0 to 5.0.

7. The method according to claim 2 , wherein the operation shutdown time is within 12 hours.

Assignees

• Sumitomo Metal Mining Co

Inventors

• Shibayama Keisuke
• Nakai Osamu
• Ozaki Yoshitomo

Classifications

• Y02P10/236

  Cross-Sectional Technologies · mapped topic

• C22B23/043 Primary

  Sulfurated acids or salts thereof · CPC title

• C22B23/0453

  Treatment or purification of solutions, e.g. obtained by leaching (C22B23/0407 takes precedence) · CPC title

• C22B23/0407

  Leaching processes · CPC title

• C22B15/0093

  by gases, e.g. hydrogen or hydrogen sulfide · CPC title