Electrolytic cell for the production of ammonia
US-2016194767-A1 · Jul 7, 2016 · US
US2021238756A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2021238756-A1 |
| Application number | US-201916972160-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jun 27, 2019 |
| Priority date | Jun 28, 2018 |
| Publication date | Aug 5, 2021 |
| Grant date | — |
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The invention provides a cathode for the nitrogen reduction reaction, comprising an electrically conductive substrate and an electrocatalytic composition on the substrate, wherein the electrocatalytic composition comprises: a support material present in one or more crystalline phases; and metallic clusters dispersed on the support material, the metallic clusters comprising at least one metal selected from ruthenium, iron, rhodium, iridium and molybdenum, wherein at least 80 mass % of the support material is present in a semiconductive crystalline phase having a conduction band minimum energy below (more positive than) −0.3 V relative to the normal hydrogen electrode (NHE).
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1 . A cathode for the nitrogen reduction reaction, comprising an electrically conductive substrate and an electrocatalytic composition on the substrate, wherein the electrocatalytic composition comprises: a support material present in one or more crystalline phases; and metallic clusters dispersed on the support material, the metallic clusters comprising at least one metal selected from ruthenium, iron, rhodium, iridium and molybdenum, wherein at least 80 mass % of the support material is present in a semiconductive crystalline phase having a conduction band minimum energy below (more positive than) −0.3 V relative to the normal hydrogen electrode (NHE). 2 . (canceled) 3 . (canceled) 4 . The cathode according to claim 1 , wherein the semiconductive crystalline phase has a conduction band minimum energy below (more positive than) 0 V relative to the normal hydrogen electrode (NHE). 5 . The cathode according to claim 1 , wherein the support material comprises at least one selected from molybdenum disulphide (MoS 2 ), ferric oxide (Fe 2 O 3 ) and titanium dioxide (TiO 2 ). 6 . The cathode according to claim 1 , wherein the metallic clusters have an average cluster size of from 1 to 10 nm. 7 . The cathode according to claim 1 , wherein the semiconductive crystalline phase is a 2D-crystalline phase. 8 . The cathode according to claim 7 , wherein the metallic clusters are at least partially intercalated between layers of the 2D-crystalline phase. 9 . The cathode according to claim 7 , wherein the support material comprises molybdenum disulphide (MoS 2 ) and the 2D-crystalline phase comprises 2H—MoS 2 . 10 . (canceled) 11 . A method of reducing dinitrogen to ammonia, the method comprising: contacting an electrocatalytic composition with dinitrogen and an electrolyte comprising a source of hydrogen; and applying a potential at the electrocatalytic composition sufficient to reduce the dinitrogen and the source of hydrogen on the electrocatalytic composition to form ammonia, wherein the electrocatalytic composition comprises: a support material present in one or more crystalline phases; and metallic clusters dispersed on the support material, the metallic clusters comprising at least one metal selected from ruthenium, iron, rhodium, iridium and molybdenum, wherein at least 80 mass % of the support material is present in a semiconductive crystalline phase having a conduction band minimum energy below (more positive than) −0.3 V relative to the normal hydrogen electrode (NHE). 12 . (canceled) 13 . (canceled) 14 . The method according to claim 11 , wherein the semiconductive crystalline phase has a conduction band minimum energy below (more positive than) 0 V relative to the normal hydrogen electrode (NHE). 15 . The method according to claim 11 , wherein the support material comprises at least one selected from molybdenum disulphide (MoS 2 ), ferric oxide (Fe 2 O 3 ) and titanium dioxide (TiO 2 ). 16 . (canceled) 17 . The method according to claim 11 , wherein the semiconductive crystalline phase is a 2D-crystalline phase. 18 . The method according to claim 17 , wherein the metallic clusters are at least partially intercalated between layers of the 2D-crystalline phase. 19 . (canceled) 20 . The method according to claim 11 , wherein the potential is in the range of −50 mV to −500 mV relative to the reversible hydrogen electrode (RHE). 21 . The method according to claim 11 , further comprising providing or replenishing the source of hydrogen in the electrolyte by oxidising a hydrogen-containing species at an anode in electrochemical communication with the electrolyte. 22 . The method according to claim 11 , further comprising recovering a product stream comprising the ammonia and recycling dihydrogen (H 2 ) present in the product stream for contact with the electrocatalytic composition and/or for oxidation at an anode in electrochemical communication with the electrolyte. 23 . The method according to claim 11 , wherein the electrolyte comprises an aprotic liquid, an ionic liquid or an ionic liquid dissolved in an aprotic liquid. 24 . An electrocatalytic composition for the nitrogen reduction reaction, comprising: a support material present in one or more crystalline phases; and metallic clusters dispersed on the support material, the metallic clusters comprising at least one metal selected from ruthenium, iron, rhodium, iridium and molybdenum, wherein at least 80 mass % of the support material is present in a semiconductive 2D-crystalline phase having a conduction band minimum energy below (more positive than) −0.3 V relative to the normal hydrogen electrode (NHE). 25 . (canceled) 26 . (canceled) 27 . (canceled) 28 . The electrocatalytic composition according to claim 24 , wherein the metallic clusters have an average cluster size of from 1 to 10 nm. 29 . The electrocatalytic composition according to claim 24 , wherein the metallic clusters are at least partially intercalated between layers of the 2D-crystalline phase. 30 . The electrocatalytic composition according to claim 24 , wherein the support material comprises molybdenum disulphide (MoS 2 ) and the 2D-crystalline phase comprises 2H—MoS 2 . 31 . (canceled) 32 . (canceled) 33 . (canceled) 34 . (canceled) 35 . (canceled) 36 . (canceled) 37 . (canceled)
Ammonia · CPC title
using catalysts, e.g. selective catalysts · CPC title
Molybdenum · CPC title
the element being a noble metal · CPC title
Iridium · CPC title
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