Process for treatment of wastewater

Patent metadata

Field	Value
Publication number	US-11148961-B2
Application number	US-201716490344-A
Country	US
Kind code	B2
Filing date	Mar 9, 2017
Priority date	Mar 9, 2017
Publication date	Oct 19, 2021
Grant date	Oct 19, 2021

Abstract

A process for the treatment of acidic wastewater which comprises hydrochloric acid, nitric acid as an optional component, 0.1 to 30 wt.-% of one or more dissolved metals selected from the group consisting of aluminum and heavy metals other than precious metals, and 10 to 500 wt.-ppm of at least one dissolved precious metal, wherein the process comprises the successive steps (1) to (5):(1) adjusting the pH value of the wastewater to 6 to 8 to produce a first composition comprising a first precipitate and an aqueous phase having a pH value in the range of 6 to 8,(2) adjusting the pH value of the first composition to >8 to 11 to produce a second composition comprising the first precipitate, a second precipitate and an aqueous phase having a pH value in the range of >8 to 11,(3) separating the precipitates from the aqueous phase,(4) passing the aqueous phase through a sand filter to produce an aqueous filtrate, and(5) passing the aqueous filtrate through a regenerative cation exchanger comprising an acidic cation exchanger resin with chelating groups and a downstream non-regenerative cation scavenger comprising a scavenger resin with chelating sulfur containing groups to produce an aqueous salt solution with a total content of dissolved aluminum plus dissolved precious metals plus dissolved heavy metals other than precious metals of 0.1 to 10.0 wt.-ppm.

First claim

The invention claimed is:

1. A process for the treatment of acidic wastewater which comprises hydrochloric acid, 0.1 to 30 wt.-% of one or more dissolved metals selected from the group consisting of aluminum and heavy metals other than precious metals, and 10 to 500 wt.-ppm of at least one dissolved precious metal, wherein the process comprises the successive steps (1) to (5):
(1) adjusting the pH value of the wastewater to 6 to 8 to produce a first composition comprising a first precipitate and an aqueous phase having a pH value in the range of 6 to 8,
(2) adjusting the pH value of the first composition to >8 to 11 to produce a second composition comprising the first precipitate, a second precipitate and an aqueous phase having a pH value in the range of >8 to 11,
(3) separating the precipitates from the aqueous phase,
(4) passing the aqueous phase through a sand filter to produce an aqueous filtrate, and
(5) passing the aqueous filtrate through a regenerative cation exchanger comprising an acidic cation exchanger resin with chelating groups followed by a downstream non-regenerative cation scavenger comprising a scavenger resin with chelating sulfur containing groups to produce an aqueous salt solution with a total content of dissolved aluminum plus dissolved precious metals plus dissolved heavy metals other than precious metals of 0.1 to 10.0 wt.-ppm, wherein the aqueous salt solution comprises a salt content which comprises as essential components: 1 to 15 wt.-% of alkali chloride, 0 to 5 wt.-% of calcium chloride and 0 to 5 wt.-% of alkali nitrate, wherein the wt.-% are in each case based on the aqueous salt solution.

2. The process of claim 1 , wherein the acidic wastewater has a pH value in the range of 0 to <6.

3. The process of claim 1 , wherein the wastewater is a mixture or a combination of more than one different wastewaters.

4. The process of claim 1 , wherein the wastewater originates from a precious metal extraction process and/or from a precious metal recycling process.

5. The process of claim 1 , wherein the adjustment of the pH value of step (1) is performed by mixing the acidic wastewater with one or more basic alkali compounds.

6. The process of claim 1 , wherein the adjustment of the pH value of step (2) is performed by mixing the first composition with one or more basic alkali compounds.

7. The process of claim 1 , wherein the solid-liquid separation of step (3) is supported by adding a flocculent to the second composition.

8. The process of claim 7 , wherein the flocculent comprises polyacrylamide and/or one or more derivatives thereof.

9. The process of claim 1 , wherein the separation of step (3) is performed batchwise or as a continuous process.

10. The process of claim 1 , wherein the chelating groups of the acidic cation exchanger resin comprise chelating iminodiacetate groups.

11. The process of claim 1 , wherein the chelating sulfur containing groups of the scavenger resin comprise chelating thiourea groups.

12. The process of claim 1 , further comprising a step (6) of pH adjustment of the aqueous salt solution to a pH value in the range of 6 to 10.

13. The process of claim 12 , further comprising a step (7) of drying the aqueous salt solution produced in step (5) or (6).

14. The process of claim 1 , further comprising a step (6) of drying the aqueous salt solution produced in step (5).

15. The process of claim 1 , wherein the aqueous salt solution further comprises calcium nitrate.

16. The process of claim 1 , wherein the acidic wastewater further comprises nitric acid.

17. The process of claim 10 , wherein the chelating sulfur containing groups of the scavenger resin comprise chelating thiourea groups.

Assignees

• Heraeus Deutschland Gmbh & Co Kg
• Heraeus Precious Metal Tech China Co Ltd
• Heraeus Site Operations Gmbh & Co Kg

Inventors

• Nowottny Christian
• Lehr Birger
• Janitz Hartmut
• Yu Zhenggang
• Chen Li

Classifications

• C22B3/42

  by ion-exchange extraction · CPC title

• C02F1/004

  using large scale industrial sized filters · CPC title

• C02F2101/20

  Heavy metals or heavy metal compounds · CPC title

• C02F2103/16

  from metallurgical processes, i.e. from the production, refining or treatment of metals, e.g. galvanic wastes · CPC title

• Y02P10/20

  Recycling · CPC title