Divided Electrochemical Cell and Low Cost High Purity Hydride Gas Production Process
US-2015345037-A1 · Dec 3, 2015 · US
US2020002180A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2020002180-A1 |
| Application number | US-201916448692-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jun 21, 2019 |
| Priority date | Jun 29, 2018 |
| Publication date | Jan 2, 2020 |
| Grant date | — |
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It is an object of the present invention to provide an electrochemical system for producing ammonia from nitrogen oxides which can perform the reaction at room temperature under normal pressure with high ammonia selectivity, and a preparation method thereof. To achieve the object above, the present invention provides an electrochemical system for producing ammonia from nitrogen oxides characteristically comprising a cathode electrode where the reduction reaction of a complex of nitrogen oxide and a metal complex compound occurs, an anode electrode, a reference electrode, an electrolyte including a metal complex compound, and a nitrogen oxide supply unit. The present invention also provides a method for producing ammonia from nitrogen oxides, which characteristically comprises the steps of introducing nitrogen oxide in the electrochemical system; forming a complex from the introduced nitrogen oxide and the metal complex compound included in the electrolyte; and performing an electrical reduction reaction of the formed complex. According to the present invention, ammonia can be produced from nitrogen oxides via electrochemical method under normal atmospheric pressure and at room temperature with a high selectivity.
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What is claimed is: 1 . An electrochemical system for producing ammonia from nitrogen oxides characteristically comprising a cathode electrode where the reduction reaction of a complex of nitrogen oxide and a metal complex compound occurs, an anode electrode, a reference electrode, an electrolyte including a metal complex compound, and a nitrogen oxide supply unit. 2 . The electrochemical system according to claim 1 , wherein the nitrogen oxide is nitrogen monoxide. 3 . The electrochemical system according to claim 1 , wherein the metal of the metal complex compound is iron or magnesium. 4 . The electrochemical system according to claim 1 , wherein the complex compound is a salt selected from the group consisting of ethylenediamine tetraacetic acid (EDTA), 1,2-cyclohexanediamine tetraacetic acid (CyDTA), and nitrilo disodium triacetate (NTA). 5 . The electrochemical system according to claim 1 , wherein the material forming the cathode electrode or the anode electrode is one or more substances selected from the group consisting of iron, glassy carbon (GC), aluminum, copper, silver, nickel, platinum, oxides thereof, and alloys thereof. 6 . The electrochemical system according to claim 1 , wherein when the material forming the cathode electrode is silver or copper, the applied potential difference is in the range of 0.2 to −0.4 Volt by the reference hydrogen electrode; when the material is glassy carbon, the applied potential difference is in the range of −0.3 to −0.4 Volt; and when the material is platinum, the applied potential difference is in the range of 0.4 to −0.4 Volt. 7 . The electrochemical system according to claim 1 , wherein the pH of the electrolyte is maintained in the range of 6˜8. 8 . A method for producing ammonia from nitrogen oxides comprising the following steps: introducing nitrogen oxide in the electrochemical system; forming a complex from the introduced nitrogen oxide and the metal complex compound included in the electrolyte; and performing an electrical reduction reaction of the formed complex. 9 . The method for producing ammonia from nitrogen oxides according to claim 8 , wherein the nitrogen oxide is nitrogen monoxide. 10 . The method for producing ammonia from nitrogen oxides according to claim 8 , wherein the concentration of the metal complex compound is 10 mM-500 mM. 11 . The method for producing ammonia from nitrogen oxides according to claim 8 , wherein when the material forming the cathode electrode is silver or copper, the applied potential difference is in the range of 0.2 to −0.4 Volt by the reference hydrogen electrode; when the material is glassy carbon, the applied potential difference is in the range of −0.3 to −0.4 Volt; and when the material is platinum, the applied potential difference is in the range of 0.4 to −0.4 Volt. 12 . The method for producing ammonia from nitrogen oxides according to claim 8 , wherein the pH of the electrolyte included in the electrochemical system for the electrical reduction reaction is maintained in the range of 6˜8.
Preparation, {purification} or separation of ammonia · CPC title
Electrolytic production of inorganic compounds or non-metals · CPC title
characterised by the material · CPC title
Preparation of ammonia from inorganic compounds · CPC title
Preparation of ammonia by synthesis (preparation or purification of gas mixtures for ammonia synthesis C01B3/025) · CPC title
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