Zinc-based electrolyte compositions, and related electrochemical processes and articles
View Patent ↗An aqueous electrolyte composition is described, including a zinc salt based on zinc acetate or zinc glocolate. The saturation concentration of zinc in the electrolyte composition is in the range of about 2.5M to about 3.5M. The composition also contains at least one salt of a monovalent cation. The molar ratio of zinc to the monovalent cation is about 1:2. An aqueous zinc electroplating bath, containing the aqueous electrolyte composition, is also disclosed, along with a method for the electrochemical deposition of zinc onto a substrate surface, using the electroplating bath. Related flow batteries are also described, including a catholyte, as well as an anolyte based on the aqueous electrolyte composition, with a membrane between the catholyte and the anolyte.
1. A flow battery, comprising:
(a) a first chamber (catholyte) comprising an aqueous solution of at least one salt of a halogen oxoacid;
(b) a second chamber (anolyte) comprising an aqueous solution of an electrochemically active material that is capable of participating in a reduction-oxidation (redox) reaction with the salt of component (a);
(c) at least one membrane separating the first chamber from the second chamber; and
(d) means for flowing the aqueous solutions through the battery;
wherein the second chamber (anolyte) contains an electro-deposited zinc anode; and the aqueous solution of the electrochemically active material has a pH between 4.5 and 7; and comprises
i) a zinc salt selected from zinc acetate, zinc glycolate, and combinations thereof, wherein the saturation concentration of zinc in the electrolyte composition is in the range of 2.5M to about 3.5M; and
ii) at least one salt of a monovalent cation selected from sodium, potassium, lithium, and ammonium; wherein the molar ratio of zinc to the monovalent cation is about 1:2.
2. The flow battery of claim 1 , configured to promote the reversible redox(oxidation-reduction) reaction that converts any of (ClO 3 − ) to Cl − , (BrO 3 − ) to Br − or (IO 3 − ) to I − .
3. The flow battery of claim 1 , wherein the salt is a chlorate salt and the oxoacid acid is chloric acid, HClO 3 .
4. The flow battery of claim 3 , wherein the chlorate salt is sodium chlorate, lithium chlorate, or combinations thereof.
5. The flow battery of claim 1 , including a bipolar cell stack that comprises a series of electrically-conductive electrodes and alternating positive plates and negative plates, each separated by one of the membranes.
6. The flow battery of claim 5 , wherein a material providing the electrically-conductive characteristic of the plates is a metal, a conductive form of carbon, or a conductive metal oxide or combinations thereof.
7. The flow battery of claim 1 , wherein the membrane separating the first chamber from the second chamber is a bipolar membrane.
8. An electric vehicle or an electric grid system that includes at least one flow battery according to claim 1 .
9. The flow battery of claim 1 , wherein the aqueous solution of the electrochemically active material further comprises acetic acid.
10. The flow battery of claim 1 , wherein the zinc salt is zinc glycolate.
11. The flow battery of claim 1 , wherein the monovalent cation is sodium.
12. The flow battery of claim 1 , wherein the monovalent cation is potassium.
13. The flow battery of claim 1 , wherein the monovalent cation is lithium.
14. The flow battery of claim 1 , wherein the monovalent cation is ammonium.