IP Library Granted Patent US 12,546,018
Granted Patent B2
US 12,546,018 · App. 17/466,618 · Granted Feb 10, 2026

Ammonia manufacturing apparatus and ammonia manufacturing method

Inventors: Jun Tamura (Tokyo, JP); Satoshi Mikoshiba (Yamato Kanagawa, JP); Ryota Kitagawa (Tokyo, JP); Yoshitsune Sugano (Kawasaki Kanagawa, JP); Koji Mizuguchi (Kawasaki Kanagawa, JP)
Assignee: Kabushiki Kaisha Toshiba
C25B1/27B01J23/28C01C1/0411C01C1/0417C01C1/0458C25B9/77C25B15/083C25B15/087
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Quick Facts
Patent No.
US 12,546,018
App. No.
17/466,618
Granted
Feb 10, 2026
Kind
B2
Abstract

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.

Claims (18)

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.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 19, 2021
From: TAMURA, JUN; MIKOSHIBA, SATOSHI; KITAGAWA, RYOTA; SUGANO, YOSHITSUNE; MIZUGUCHI, KOJI
To: KABUSHIKI KAISHA TOSHIBA
Reel/Frame 057837/0522 →
Priority Claims (1)
JP 2019-227271 · Dec 17, 2019 · national
Continuity (2)
Continuation PCTJP2020033321 · Sep 2, 2020
Related Publication 20210395902A1 · Dec 23, 2021
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