Electro-thermochemical Li Cycling for NH3 Synthesis from N2 and H2O

Patent metadata

Field	Value
Publication number	US-2018029895-A1
Application number	US-201715664240-A
Country	US
Kind code	A1
Filing date	Jul 31, 2017
Priority date	Aug 1, 2016
Publication date	Feb 1, 2018
Grant date	—

Abstract

An electro-thermochemical cycling system for producing ammonia is provided that includes a reaction chamber having a metal compound input port, an anode suitable for oxidation in contact with the metal compound and configured for oxidation of hydroxide ions to water and oxygen, a cathode suitable for plating in contact with the metal compound and configured to electrolyze the metal compound to metal, a voltage source connecting the cathode and anode, a nitrogen port to the reaction chamber that combines nitrogen with the electrolyzed metal on the cathode to form a metal-nitrogen compound proximal to the nitrogen input, an atomic hydrogen port to the reaction chamber that combines with the metal-nitrogen compound to form ammonia, and an ammonia output port from the reaction chamber, where a metal compound input port inputs the metal compound to the reaction chamber according to a depletion rate of the metal compound in the reaction chamber.

First claim

What is claimed:

1 ) An electro-thermochemical cycling system for producing ammonia, comprising:
a) a reaction chamber comprising a metal compound input port, wherein a metal compound is input to said reaction chamber through said metal compound input port; b) an anode suitable for oxidation, wherein said anode is in contact with said metal compound, wherein said anode is configured for oxidation of anions; c) a cathode that is suitable for plating, wherein said cathode is configured to electrolyze said metal compound to metal; d) a voltage source, wherein said voltage source connects said cathode to said anode; e) a nitrogen port to said reaction chamber containing said electrolyzed metal, wherein nitrogen from said nitrogen port combines with said electrolyzed metal to form a metal-nitrogen compound proximal to said nitrogen input; f) an atomic hydrogen port to said reaction chamber containing said metal-nitrogen compound, wherein atomic hydrogen from said atomic hydrogen port combines with said metal-nitrogen compound to form ammonia; and g) an ammonia output port from said reaction chamber containing said ammonia, wherein said metal compound input port is configured to input said metal compound to said reaction chamber according to a depletion rate of said metal compound in said reaction chamber.

2 ) The electro-thermochemical cycling system for production of ammonia according to claim 1 , wherein said metal compound comprises a metal selected from the group consisting of Li, Be, Mg, Na, Mo, Al, Zn, Ca, Sr, and Ba.

3 ) The electro-thermochemical cycling system for production of ammonia according to claim 2 , wherein said anode or said cathode is equipped with solid or porous alumina, magnesia, or steel structures, wherein said alumina, magnesia, or steel structures are configured to hold produced molten Li, wherein said solid or porous alumina or steel structures are configured to separate and direct H 2 O and O 2 produced gas.

4 ) The electro-thermochemical cycling system for production of ammonia according to claim 1 , wherein said reaction chamber is divided into separate said reaction chambers comprising said reaction chamber containing said electrolyzed metal, said reaction chamber containing said metal-nitrogen compound, and said reaction chamber containing said ammonia.

5 ) The electro-thermochemical cycling system for production of ammonia according to claim 1 , wherein said cathode comprises a material selected from the group consisting of steel, Ni, Cu, Ti, Mo, and graphite.

6 ) The electro-thermochemical cycling system for production of ammonia according to claim 1 , wherein said anode comprises a material selected from the group consisting of steel, Ni, Pt, W, metal alloys, metal oxides, and graphite.

7 ) The electro-thermochemical cycling system for production of ammonia to according to claim 1 , wherein said metal compound comprises a molten metal compound and an additive for reducing the melting point of said molten metal compound mixture, reducing the melting point of said molten metal compound and dissolving said metal compound, or dissolving said metal compound contained in said reaction chamber.

8 ) The electro-thermochemical cycling system for production of ammonia according to claim 7 , wherein said additive comprises LiCl, KCl, CsCl, RbCl, LiI or alkali earth metal compounds for decreased melting point and removing hydrogen, oxygen, or hydroxide sources from said cathode, or removing hydrogen, oxygen, or hydroxide sources from said cathode.

9 ) The electro-thermochemical cycling system for production of ammonia according to claim 1 , wherein said atomic hydrogen is selected from the group consisting of water, ethanol, hydrogen, and HCl.

10 ) The electro-thermochemical cycling system for production of ammonia according to claim 1 , wherein anode oxidation source is selected from the group consisting of OH, Cl, Br, I, and F.

11 ) The electro-thermochemical cycling system for production of ammonia to according to claim 1 , wherein said reaction chamber further comprises a diffusion barrier disposed between said anode and said cathode.

12 ) The electro-thermochemical cycling system for production of ammonia according to claim 1 , wherein said reaction chamber comprises a cylindrical reaction chamber that is divided into three sub-chambers, wherein said anode and said cathode are separated by said diffusion barrier, wherein said three sub-chambers rotate about a central axis of said cylindrical reaction chamber, wherein said ammonia output port is positioned on a sidewall of said cylindrical reaction chamber.

Assignees

• Univ Leland Stanford Junior

Inventors

• Mcenaney Joshua M
• Schwalbe John
• Singh Aayush Ranjan
• Lin John
• Kibsgaard Jakob
• Jaramillo Thomas F
• Cargnello Matteo
• Nørskov Jens K

Classifications

• B01J19/24

  Stationary reactors without moving elements inside (B01J19/08, B01J19/26 take precedence; with stationary particles B01J8/02) · CPC title

• C25C7/06

  Operating or servicing · CPC title

• C25C7/005

  of cells for the electrolysis of melts (C25C7/02 - C25C7/06 take precedence) · CPC title

• B01J2219/24

  Stationary reactors without moving elements inside · CPC title

• C25C3/02

  of alkali or alkaline earth metals · CPC title