Ammonia synthesis methods and systems
US-2019202707-A1 · Jul 4, 2019 · US
US12546018B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12546018-B2 |
| Application number | US-202117466618-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 3, 2021 |
| Priority date | Dec 17, 2019 |
| Publication date | Feb 10, 2026 |
| Grant date | Feb 10, 2026 |
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An ammonia manufacturing apparatus includes: an electrochemical reaction unit including a first electrolytic bath for accommodating a first electrolytic solution, an oxidation electrode disposed in the first electrolytic bath, a second electrolytic bath for accommodating a second electrolytic solution containing nitrogen, an ammonia producing catalyst, and a reducing agent, a reduction electrode disposed in the second electrolytic bath, and a diaphragm, and configured to reduce nitrogen by the ammonia producing catalyst and the reducing agent in the second electrolytic bath to produce ammonia, and reduce the reducing agent oxidized due to the production of ammonia, at the reduction electrode by connecting the oxidation electrode and the reduction electrode to a power supply; a nitrogen supply unit including a nitrogen supply part for dissolving nitrogen in the second electrolytic solution; and an ammonia separation unit including a separation part configured to separate ammonia from the second electrolytic solution.
Opening claim text (preview).
What is claimed is: 1 . An ammonia manufacturing method comprising: supplying a first electrolytic solution into a first electrolytic bath of an electrochemical reaction unit and supplying a second electrolytic solution containing nitrogen, an ammonia producing catalyst, and a reducing agent into a second electrolytic bath of the electrochemical reaction unit, the electrochemical reaction unit comprising the first electrolytic bath, an oxidation electrode disposed in the first electrolytic bath, the second electrolytic bath, a reduction electrode disposed in the second electrolytic bath, and a diaphragm provided between the first electrolytic bath and the second electrolytic bath; reducing the nitrogen by the ammonia producing catalyst and the reducing agent in the second electrolytic bath to produce ammonia, and oxidizing the first electrolytic solution at the oxidation electrode in the first electrolytic bath and reducing the reducing agent oxidized due to the production of the ammonia in the second electrolytic bath at the reduction electrode, by supplying electric power from a power supply to the oxidation electrode and the reduction electrode; dissolving nitrogen in the second electrolytic solution so as to sustain a reduction reaction of the nitrogen in the second electrolytic bath; and separating the ammonia from the second electrolytic solution to produce the ammonia. 2 . The method according to claim 1 , wherein: the dissolving nitrogen into the second electrolytic solution is performed so as to increase a concentration of the ammonia in the second electrolytic solution; and the separating the ammonia is performed so as to separate the ammonia from the second electrolytic solution increased in the concentration of the ammonia. 3 . The method according to claim 1 , further comprising: circulating the second electrolytic solution outside the second electrolytic bath; supplying nitrogen to the second electrolytic solution in a circulation path of the second electrolytic solution including the second electrolytic bath; and taking at least part of the second electrolytic solution out of the circulation path and separating the ammonia from the second electrolytic solution, and sending the second electrolytic solution from which the ammonia has been separated into the circulation path. 4 . The method according to claim 3 , wherein nitrogen is supplied to the second electrolytic solution stored in an electrolytic solution regulation tank provided in the circulation path, and the second electrolytic solution from which the ammonia has been separated is sent to the electrolytic solution regulation tank. 5 . The method according to claim 1 , wherein the reducing agent includes a halide of a lanthanoide metal. 6 . The method according to claim 1 , wherein the ammonia producing catalyst includes a molybdenum complex.
Separation of NH3 (during purge gas treatment C01C1/0476) · CPC title
characterised by the synthesis reactor, e.g. arrangement of catalyst beds and heat exchangers in the reactor · CPC title
characterised by the catalyst · CPC title
Molybdenum · CPC title
Recycling of electrolyte to electrochemical cell · CPC title
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