Fuel cell system and method

Patent metadata

Field	Value
Publication number	US-2021313607-A1
Application number	US-202117212161-A
Country	US
Kind code	A1
Filing date	Mar 25, 2021
Priority date	Apr 7, 2020
Publication date	Oct 7, 2021
Grant date	—

Abstract

A system for generating electrical power includes an electrochemical cell including a cathode and an anode separated by an electrolyte, a cathode fluid flow path in operative fluid communication with the cathode including a cathode-side inlet and a cathode-side outlet, and an anode fluid flow path in operative fluid communication with the anode including an anode-side inlet and an anode-side outlet. The system also includes: a reactant source in operative fluid communication with the anode-side inlet; an oxygen generator in operative fluid communication with the cathode-side inlet, including a combustible composition comprising a fuel and a salt that thermally decomposes to release oxygen; and an electrical connection between the electrochemical cell and a power sink.

First claim

What is claimed is:

1 . A system for generating electrical power, comprising:
an electrochemical cell including a cathode and an anode separated by an electrolyte, a cathode fluid flow path in operative fluid communication with the cathode including a cathode-side inlet and a cathode-side outlet, and an anode fluid flow path in operative fluid communication with the anode including an anode-side inlet and an anode-side outlet; a reactant source in operative fluid communication with the anode-side inlet; an oxygen generator in operative fluid communication with the cathode-side inlet, including a combustible composition comprising a fuel and a salt that thermally decomposes to release oxygen; and an electrical connection between the electrochemical cell and a power sink.

2 . The system of claim 1 , wherein said salt comprises an alkali metal chlorate, an alkali metal perchlorate, an alkaline earth metal chlorate, or an alkaline earth metal perchlorate.

3 . The system of claim 1 , wherein said fuel comprises a metal or non-metal reducing agent.

4 . The system of claim 1 , wherein the fuel comprises aluminum, iron, magnesium, manganese, titanium, carbon, silicon, or boron.

5 . The system of claim 1 , wherein the electrochemical cell is configured as a proton transfer fuel cell reactor including a proton transfer medium as said electrolyte.

6 . The system of claim 5 , further comprising a heater or heat exchanger arranged to heat or cool oxygen from the oxygen generator.

7 . The system of claim 1 , wherein the electrochemical cell is configured as an oxygen ion transfer fuel cell reactor including an oxygen ion transfer medium as said electrolyte.

8 . The system of claim 1 , further comprising a pressure regulator disposed on an oxygen flow path in fluid communication with the oxygen generator and the cathode.

9 . The system of claim 1 , further comprising an inert gas flow path from the cathode-side outlet in operable fluid communication with a protected space.

10 . The system of claim 9 , further comprising:
an electrical connection between the electrochemical cell and a power source; and a controller configured to alternatively operate the system in alternate modes of operation selected from a plurality of modes including:
a first mode in which electric power is directed from the power source to the electrochemical cell to provide a voltage difference between the anode and the cathode, and an inerting gas is directed from the cathode-side outlet to the protected space; and
a second mode in which reactant from the reactant source is directed to the anode, electric power is directed from the electrochemical cell to the power sink, and the inerting gas is directed from the cathode-side outlet to the protected space.

11 . A method of generating electrical power, comprising:
reacting a composition comprising a fuel and a salt that thermally decomposes to release oxygen to produce released oxygen; directing the released oxygen to a cathode of an electrochemical cell including a cathode and an anode separated by an electrolyte; directing a reactant to the anode, and reacting the reactant with the released oxygen; and directing electrical power from the electrochemical cell to a power sink.

12 . The method of claim 11 , wherein said salt comprises an alkali metal chlorate, an alkali metal perchlorate, an alkaline earth metal chlorate, or an alkaline earth metal perchlorate.

13 . The method of claim 11 , wherein said fuel comprises a metal or non-metal reducing agent.

14 . The method of claim 11 , wherein the fuel comprises aluminum, iron, magnesium, manganese, titanium, carbon, silicon, or boron.

15 . The method of claim 11 , wherein the electrochemical cell is configured as a proton transfer fuel cell reactor including a proton transfer medium as said electrolyte, and the method includes transferring protons from the anode across the proton transfer medium to the cathode, and reacting the protons with the released oxygen at the cathode.

16 . The method of claim 15 , further comprising heating or cooling the released oxygen to form heated or cooled released oxygen, and directing the heated or cooled released oxygen to the cathode.

17 . The method of claim 11 , wherein the electrochemical cell is configured as an oxygen ion transfer fuel cell reactor including an oxygen ion transfer medium as said electrolyte, and the method includes ionizing oxygen at the cathode, transferring the ionized oxygen across the oxygen ion transfer medium, and reacting the ionized oxygen with the reactant at the anode.

18 . The method of claim 11 , further comprising regulating a pressure of the released oxygen.

19 . The method of claim 11 , further comprising directing an inert gas from the cathode to a protected space.

20 . The method of claim 19 , further comprising:
alternatively operating the system in alternate modes of operation selected from a plurality of modes including:
a first mode in which electric power is directed from a power source to the electrochemical cell to provide a voltage difference between the anode and the cathode, and an inerting gas is directed from the cathode to the protected space; and
a second mode in which reactant from the reactant source is directed to the anode-side inlet, electric power is directed from the electrochemical cell to the power sink, and the inerting gas is directed from the cathode-side outlet to the protected space.

Assignees

• Hamilton Sundstrand Corp

Inventors

• Rheaume Jonathan
• Pess Matthew

Classifications

• Y02T90/40

  Application of hydrogen technology to transportation, e.g. using fuel cells · CPC title

• Y02E60/36

  Hydrogen production from non-carbon containing sources, e.g. by water electrolysis · CPC title

• Y02E60/50

  Fuel cells · CPC title

• C25B15/087

  Recycling of electrolyte to electrochemical cell · CPC title

• C25B15/021

  of heating or cooling · CPC title