Divided Electrochemical Cell and Low Cost High Purity Hydride Gas Production Process
US-2015345037-A1 · Dec 3, 2015 · US
US9540737B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9540737-B2 |
| Application number | US-201414778627-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 26, 2014 |
| Priority date | Mar 26, 2013 |
| Publication date | Jan 10, 2017 |
| Grant date | Jan 10, 2017 |
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A method is provided for an electrochemical synthesis of ammonia in alkaline media. The method electrolytically converts N 2 and H 2 to NH 3 in an electrochemical cell comprising an anode, a cathode, and an alkaline electrolyte. The method includes exposing an anode to a H 2 -containing fluid, wherein the anode is active toward adsorption and oxidation of H 2 ; exposing a cathode to a N 2 -containing fluid, wherein the cathode is active toward adsorption and reduction of N 2 to form NH 3 ; and applying a voltage between the anode and the cathode so as to facilitate adsorption of hydrogen onto the anode and adsorption of nitrogen onto the cathode; wherein the voltage is sufficient to simultaneously oxidize the H 2 and reduce the N 2 . The electrolytic method is performed with the H 2 and N 2 pressures from about 10 atmospheres (atm) to about 1 atm; and at temperatures from about 25° C. to about 205° C.
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What is claimed is: 1. A method for electrolytically converting molecular nitrogen (N 2 ) to ammonia (NH 3 ) in an electrochemical cell comprising an anode, a cathode, and an alkaline electrolyte, the method comprising: exposing an anode comprising a first conducting component to a molecular hydrogen (H 2 ) containing fluid at a first pressure and first temperature, wherein the first conducting component is active toward adsorption and oxidation of H 2 ; exposing a cathode comprising a second conducting component to a molecular nitrogen (N 2 ) containing fluid at a second pressure and second temperature, wherein the second conducting component is active toward adsorption and reduction of N 2 to form NH 3 ; and applying a voltage between the anode exposed to the H 2 -containing fluid and the cathode exposed to the molecular N 2 -containing fluid so as to facilitate adsorption of hydrogen onto the anode and adsorption of nitrogen onto the cathode; wherein the voltage is sufficient to simultaneously oxidize the H 2 and reduce the N 2 ; wherein the first and second pressures are independently equal to or less than about 10 atmospheres (atm) to about 1 atm; and wherein the first and second temperatures are greater than about 25° C. and less than about 205° C. 2. A method according to claim 1 , further comprising maintaining the voltage equal or more negative than a temperature dependent thermodynamics voltage for the production of ammonia. 3. The method of claim 1 , wherein the voltage is applied as a constant voltage. 4. The method of claim 1 , wherein the first conducting component of the anode comprises a metal selected from platinum, iridium, ruthenium, palladium, rhodium, nickel, iron, or a combination thereof. 5. The method of claim 4 , wherein the first conducting component of the anode comprises a combination of the metals, which are co-deposited as alloys or deposited by layers. 6. The method of claim 1 , wherein the second conducting component of the cathode comprises a metal selected from platinum, iridium, ruthenium, palladium, rhodium, nickel, iron, copper, or a combination thereof. 7. The method of claim 6 , wherein the second conducting component of the cathode comprises a combination of the metals, which are co-deposited as alloys or deposited by layers. 8. The method of claim 1 , wherein the alkaline electrolyte has a pH equal to or greater than about 8. 9. The method of claim 1 , wherein the alkaline electrolyte comprises a hydroxide salt. 10. The method of claim 1 , wherein the alkaline electrolyte comprises an alkali metal or alkaline earth metal salt of a hydroxide. 11. The method of claim 1 , wherein the alkaline electrolyte has a hydroxide concentration from 0.1 M to about 9 M. 12. The method of claim 1 , wherein the alkaline electrolyte contains potassium hydroxide in a concentration from about 0.1 M to about 9 M. 13. The method of claim 9 , wherein the alkaline electrolyte further comprises a polymeric gel. 14. The method of claim 13 , wherein the polymeric gel comprises a polyacrylic acid. 15. The method of claim 1 , wherein the electrochemical cell further comprises a separator. 16. The method of claim 15 , wherein separator comprises an anion exchange membrane.
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