Arsenic removal from lead concentrate by ozone treatment and reverse flotation

Patent metadata

Field	Value
Publication number	US-10822673-B1
Application number	US-201916716630-A
Country	US
Kind code	B1
Filing date	Dec 17, 2019
Priority date	Dec 17, 2019
Publication date	Nov 3, 2020
Grant date	Nov 3, 2020

Abstract

Method for removing arsenic mineral from a lead concentrate by reverse flotation with an ozone pre-treatment. The method comprises the steps of: receiving a slurry of the lead concentrate that has previously undergone flotation processes, bubbling ozone into the slurry of the lead concentrate to remove reagents used in previous flotation processes, adding a sulfide salt to the slurry to depress lead mineral, adding an alkali to increase the pH of the slurry, adding a collector and then a frother to the slurry for a reverse flotation processing and floating the arsenic mineral out of the lead mineral to obtain a now-purified lead concentrate.

First claim

What is claimed is:

1. A method for removing arsenic mineral from a lead concentrate by reverse flotation with an ozone pre-treatment, the method comprising the steps of:
a) receiving a slurry of the lead concentrate that has previously undergone flotation processes;
b) bubbling ozone into the slurry of the lead concentrate to remove reagents used in previous flotation processes;
c) adding a sulfide salt to the slurry to depress lead mineral;
d) adding an alkali to increase the pH of the slurry;
e) adding a collector and then a frother to the slurry for a reverse flotation processing; and
f) floating the arsenic mineral out of the lead mineral to obtain a now-purified lead concentrate.

2. The method of claim 1 , wherein the reagents used in the previous flotation processes include dithiophosphinate.

3. The method of claim 1 , wherein the sulfide salt is selected from NaSH, Na 2 S, SO 2 gas, or combination thereof.

4. The method of claim 1 , wherein the alkali is lime.

5. The method of claim 1 , wherein the redox potential of the slurry after the step b) of adding the sulfide salt is from about −500 mV to about −300 mV.

6. The method of claim 1 , wherein the pH of the slurry after the step c) of adding the alkali is between about 9.0 and about 11.5.

7. The method of claim 1 , wherein the pH of the slurry after the step c) of adding the alkali is between about 10.0 and about 11.0.

8. The method of claim 1 , wherein the collector is a short carbon-chain anionic collector.

9. The method of claim 8 , wherein the short carbon-chain anionic collector comprises 1 to 6 carbon atoms (i.e., C 1 to C 6 ).

10. The method of claim 9 , wherein the short carbon-chain anionic collector is PEX.

11. The method of claim 1 , wherein the frother is MIBC.

12. The method of claim 1 , wherein the arsenic mineral is arsenopyrite (FeAsS).

13. The method of claim 1 , wherein the lead mineral is galena (PbS) that contains silver.

14. The method of claim 1 , wherein the lead mineral is galena (PbS) that does not contain silver.

15. The method of claim 1 , further comprising the step of:
retaining the slurry for a contact time with ozone sufficient in length to maintain the slurry have no more foaming appears at the surface during the step a) of bubbling ozone gas into the slurry.

16. The method of claim 15 , wherein the contact time is about 10 to about 20 minutes.

17. The method of claim 1 , further comprising the step of adding N 2 or sulfite salts to the slurry after the step of b) to de-aerate the slurry and keep a dissolved oxygen concentration in the slurry less than about 1 mg/L.

18. The method of claim 1 , further comprising the step of
adding N 2 or sulfite salts to the slurry after the step of b) to de-aerate the slurry and keep a dissolved oxygen concentration in the slurry less than about 0.5 mg/L.

19. The method of claim 1 , wherein an arsenic content in the now-purified lead concentrate is about 0.66% or less.

20. A method of for removing arsenic mineral from a lead concentrate by reverse flotation with an ozone pre-treatment, the method comprising the steps of:
a) receiving a slurry of the lead concentrate that has previously undergone flotation processes;
b) bubbling ozone into the slurry of the lead concentrate to remove dithiophosphinate used in previous flotation processes;
c) adding NaHS to the slurry to depress lead mineral;
d) adding lime to increase the pH of the slurry;
e) adding PEX and then MIBC to the slurry for a reverse flotation processing; and
f) floating the arsenic mineral out of the lead mineral to obtain a now-purified lead concentrate.

Assignees

• Air Liquide American

Inventors

• Zuttah Sylvester

Classifications

• C22B1/11 Primary

  Removing sulfur, phosphorus or arsenic other than by roasting · CPC title

• B03D2203/025

  Precious metal ores · CPC title

• B03D2203/02

  Ores · CPC title

• B03D2201/007

  Modifying reagents for adjusting pH or conductivity · CPC title

• B03D1/085

  of the feed, e.g. conditioning, de-sliming · CPC title