Cathode, electrochemical cell and its use

Patent metadata

Field	Value
Publication number	US-10676378-B2
Application number	US-201414889055-A
Country	US
Kind code	B2
Filing date	May 9, 2014
Priority date	May 13, 2013
Publication date	Jun 9, 2020
Grant date	Jun 9, 2020

Abstract

An electrochemical cell containing a sacrificial electrode suitable for electrocoagulation as well as an electrocoagulation process for removing various pollutants from water or wastewater by the use of the electrochemical cell. Also, the sacrificial electrode itself. Several electrochemical cells can be coupled to an electrochemical cell assembly. Certain aspects and embodiments are especially suitable for reduction of fluoride or fluoride in combination with heavy metals such as hexavalent chromium or arsenic.

First claim

The invention claimed is:

1. A sacrificial anode containing a compacted sacrificial part and a non-sacrificial electrical conductive part, the sacrificial part having porosity between 20-60% by volume and containing iron powder, wherein, in the iron powder, the amount of particles below 45 μm is at most 20% by weight.

2. A sacrificial anode according to claim 1 , wherein the sacrificial part contains a mixture of iron powder and aluminum powder.

3. A sacrificial anode according to claim 2 , wherein the weight ratio between iron powder and aluminum powder 50:50 to 98:2.

4. A sacrificial anode according to claim 1 , wherein the iron powder contains at least 90% by weight of iron.

5. A sacrificial anode according to claim 1 , wherein the non-sacrificial electrical conductive part of the anode is made of graphite or stainless steel.

6. A sacrificial anode according to claim 5 , wherein the sacrificial part of the sacrificial anode is at least one toroid made of the compacted powders surrounding and in close electrical contact with the non-sacrificial electrical conductive part.

7. A sacrificial anode according to claim 1 , wherein the non-sacrificial electrical conductive part of the anode has a shape of a porous graphite basket or container.

8. A sacrificial anode according to claim 1 , wherein the non-sacrificial electrical conductive part of the anode has a shape of a solid rod, bar, or plate.

9. A sacrificial anode according to claim 1 , wherein the sacrificial part has porosity between 30-50% by volume.

10. A sacrificial anode according to claim 1 , wherein, in the iron powder, the amount of particles below 45 μm is at most 12% by weight.

11. A sacrificial anode according to claim 1 , wherein, in the iron powder, the amount of particles between 45 and 150 μm being 5-50% by weight, the amount of particles between 150 and 250 μm being 5-50% by weight, the amount of particles between 250 and 850 μm being 20-80% by weight.

12. A sacrificial anode according to claim 1 , wherein the iron powder has an apparent density between 0.8-3.0 g/cm 3 .

13. A sacrificial anode according to claim 1 , wherein the iron powder has an apparent density between 1.2-1.8 g/cm 3 .

14. A sacrificial anode according to claim 1 , wherein the iron powder has a specific surface area may be between 0.1 and 0.5 m 2 /g as measured according to BET.

15. A sacrificial anode according to claim 1 , wherein the compacted sacrificial part is compacted at a compaction pressure of at least 70 MPa.

16. A sacrificial anode according to claim 1 , wherein the iron powder has:
a particle size distribution between 10 μm and 1 mm,
an apparent density as measured according to ISO 3923-1:2008 between 0.8-3.0 g/cm3, and
a specific surface area between 0.1 and 0.5 m2/g as measured according to BET.

17. An electrochemical cell containing a sacrificial electrode according to claim 1 and a cathode.

18. An electrochemical cell according to claim 17 , wherein the anode and the cathode are identical in structure.

19. A method for removal of pollutants from water by electrocoagulation comprising:
providing at least one electrochemical cell containing a sacrificial electrode and a cathode, and
contacting water to be purified with the at least one electrochemical cell while supplying an electric potential difference between the cathode and the anode,
wherein the sacrificial electrode is a sacrificial anode containing a compacted sacrificial part and a non-sacrificial electrical conductive part, the sacrificial part having porosity between 20-60% by volume and containing iron powder, wherein, in the iron powder, the amount of particles below 45 μm is at most 20% by weight.

20. A method according to claim 19 , wherein the method is stopped when the sacrificial part of the sacrificial anode is at least partly consumed and optionally continued after replacement of the sacrificial part of the sacrificial anode.

21. A method according to claim 19 , for removal of pollutants from water by electrocoagulation wherein when the anode and cathode are identical in structure the method further comprises the step of:
switching polarity when the sacrificial part of the sacrificial anode at least partly is consumed.

22. A method according to claim 19 , wherein prior to, and/or during, the method, pH is adjusted to a value which prohibits dissolution of formed hydroxide flocculants.

23. A method according to claim 19 , wherein the potential difference between the anode and the cathode is sufficient to yield a current density between 15 and 300 A/m 2 .

24. A method according to claim 19 , wherein the water contains heavy metals.

25. A method according to claim 19 , wherein the water contains fluoride.

Assignees

• Hoeganaes Ab Publ

Inventors

• Tandukar Madan
• Unger Kyle
• Endler Paul

Classifications

• C02F2001/46171

  Cylindrical or tubular shaped · CPC title

• C02F2001/46161

  Porous electrodes · CPC title

• C02F2201/4613

  Inversing polarity · CPC title

• C02F1/66

  by neutralisation; pH adjustment (for degassing C02F1/20; using ion-exchange C02F1/42; for flocculation or precipitation of suspended impurities C02F1/52; for removing dissolved compounds C02F1/58) · CPC title

• C02F2101/103

  Arsenic compounds · CPC title