IP Library Granted Patent US 12,435,686
Granted Patent B2
US 12,435,686 · App. 18/766,604 · Granted Oct 7, 2025

Systems and methods for the on-board production of hydrogen from ammonia for fueling an internal combustion engine that requires no fossil fuel promotor

Inventor: James L. Wall, II (Concord, NC)
Assignee: First Ammonia Motors, Inc.
F02M21/0227C01B3/047F02M21/0206F02M21/06F02M27/02C01B2203/0277C01B2203/0811C01B2203/085C01B2203/1035C01B2203/142
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Quick Facts
Patent No.
US 12,435,686
App. No.
18/766,604
Granted
Oct 7, 2025
Kind
B2
Abstract

The present invention relates, in general, to systems and methods for generating hydrogen from ammonia on-board vehicles, where the produced hydrogen is used as fuel source for an internal combustion engine. The present invention utilizes an electric catalyst unit operating in series with a plate-type heat exchange catalyst unit. The electric catalyst unit is used to initiate an ammonia cracking process on-board during a cold start or low load operating condition of the internal combustion engine, where the ammonia cracking process occurs in the heat exchange catalyst unit once exhaust gas from the internal combustion engine has been heated to a threshold temperature suitable to perform the ammonia cracking process.

Claims (56)

1. An on-board ammonia cracking system for a vehicle having an internal combustion engine, the on-board ammonia cracking system comprising:

an ammonia tank containing liquid ammonia;

a pressure regulator receiving liquid ammonia from the ammonia tank, the pressure regulator outputting gaseous ammonia and residual liquid ammonia;

a heat exchange catalyst unit coupled to the ammonia tank, the heat exchange catalyst unit having an exhaust inlet, an exhaust outlet, an ammonia inlet, and a gas outlet, the exhaust inlet receiving exhaust from the internal combustion engine, and the ammonia inlet receiving gaseous ammonia from the pressure regulator via a first supply path;

an electric catalyst unit coupled in series to the heat exchange catalyst unit via only the gas outlet;

an injection system coupled to the internal combustion engine, the injection system receiving residual liquid ammonia from the pressure regulator via a second supply path; and

a heat exchange unit positioned between the electric catalyst unit and the injection system,

wherein the ammonia undergoes a cracking process in the heat exchange catalyst unit if the exhaust gas has a temperature sufficient to perform ammonia cracking,

wherein the ammonia exits the heat exchange catalyst unit and flows to the electric catalyst unit and undergoes the cracking process in the electric catalyst unit if the exhaust does not have a temperature sufficient to perform ammonia cracking,

wherein hydrogen resulting from ammonia cracking flows from the electric catalyst unit to the heat exchange unit,

wherein heat is transferred from the hydrogen to ammonia within the heat exchange unit, resulting in cooled hydrogen, and

wherein the injection system utilizes the cooled hydrogen as a co-fuel along with the residual liquid ammonia to power the internal combustion engine.

2. The on-board ammonia cracking system of claim 1 , wherein the heat exchange unit utilizes ammonia as a heat exchange medium.

3. The on-board ammonia cracking system of claim 1 , wherein the heat exchange unit utilizes gaseous ammonia as a heat exchange medium.

4. The on-board ammonia cracking system of claim 1 , wherein channels are formed between a plurality of plates in the heat exchange catalyst unit, and wherein discrete catalyst media is deposited in the channels.

5. The on-board ammonia cracking system of claim 4 , where surfaces of the plurality of plates are coated with a catalyst.

6. The on-board ammonia cracking system of claim 1 , wherein the electric catalyst unit includes an electric heater.

7. The on-board ammonia cracking system of claim 1 , wherein the heat exchange catalyst unit includes an exhaust channel and an ammonia channel, wherein the exhaust gas channel and the ammonia channel are oriented in a perpendicular fashion to one another.

8. An on-board ammonia cracking system for a vehicle having an internal combustion engine, the on-board ammonia cracking system comprising:

an ammonia tank containing liquid ammonia;

a pressure regulator receiving liquid ammonia from the ammonia tank, the pressure regulator outputting gaseous ammonia and residual liquid ammonia;

a heat exchange catalyst unit coupled to the ammonia tank, the heat exchange catalyst unit receiving exhaust from the internal combustion engine and receiving gaseous ammonia from the pressure regulator via a first supply path;

an electric catalyst unit coupled in series via a single fluid path with the heat exchange catalyst unit, the electric catalyst unit including an electric heater;

an injection system coupled to the internal combustion engine, the injection system receiving residual liquid ammonia from the pressure regulator via a second supply path; and

a heat exchange unit positioned between the electric catalyst unit and the injection system, the heat exchange unit utilizing gaseous ammonia as a heat exchange medium,

wherein the ammonia undergoes a cracking process in the heat exchange catalyst unit if the exhaust has a temperature sufficient to perform ammonia cracking,

wherein the ammonia exits the heat exchange catalyst unit and flows to the electric catalyst unit and undergoes the cracking process in the electric catalyst unit if the exhaust does not have a temperature sufficient to perform ammonia cracking,

wherein hydrogen resulting from ammonia cracking flows from the electric catalyst unit to the heat exchange unit,

wherein heat is transferred from the hydrogen to the gaseous ammonia within the heat exchange unit, resulting in cooled hydrogen, and

wherein the injection system utilizes the cooled hydrogen as a co-fuel along with the residual liquid ammonia to power the internal combustion engine.

9. The on-board ammonia cracking system of claim 8 , wherein the gaseous ammonia flows in a first channel within the heat exchange catalyst unit and the exhaust flows in a second channel within the heat exchange catalyst unit, wherein the first channel and second channel are oriented perpendicular to each other.

10. The on-board ammonia cracking system of claim 8 , wherein when the gaseous ammonia undergoes the cracking process in the electric catalyst unit, the gaseous ammonia has been pre-heated in the heat exchange catalyst unit before flowing to the electric catalyst unit.

11. The on-board ammonia cracking system of claim 8 , wherein the temperature sufficient to perform ammonia cracking ranges from 400° C. to 700° C.

12. The on-board ammonia cracking system of claim 8 , wherein the electric heater is selected from a group consisting of an air process heater, a cartridge heater, a tubular heater, a band heater, a strip heater, an etched foil heater, a thin-film heater, a ceramic heater, a ceramic fiber heater, and a resistance wire.

13. The on-board ammonia cracking system of claim 8 , wherein the exhaust flows in a first direction through the heat exchange catalyst unit, and the gaseous ammonia flows in a second direction, opposite the first direction, through the heat exchange catalyst unit.

14. The on-board ammonia cracking system of claim 8 , wherein the exhaust and the gaseous ammonia each flow in the same direction through the heat exchange catalyst unit.

15. An on-board ammonia cracking system for a vehicle having an internal combustion engine, the on-board ammonia cracking system comprising:

an ammonia tank containing liquid ammonia;

a pressure regulator receiving liquid ammonia from the ammonia tank, the pressure regulator outputting gaseous ammonia and residual liquid ammonia;

a heat exchange catalyst unit coupled to the ammonia tank, the heat exchange catalyst unit receiving exhaust from the internal combustion engine and receiving gaseous ammonia from the pressure regulator via a first supply path;

an electric catalyst unit coupled in series with the heat exchange catalyst unit via a single fluid path such that the exhaust gas does not flow from the heat exchange catalyst unit to the electric catalyst unit;

an injection system coupled to the internal combustion engine, the injection system receiving residual liquid ammonia from the pressure regulator via a second supply path; and

a heat exchange unit positioned between the electric catalyst unit and the injection system, the heat exchange unit utilizing gaseous ammonia as a heat exchange medium,

wherein the ammonia undergoes a cracking process in the heat exchange catalyst unit if the exhaust has a temperature sufficient to perform ammonia cracking, and

if the exhaust does not have a temperature sufficient to perform ammonia cracking:

(1) the gaseous ammonia is pre-heated in the heat exchange catalyst unit,

(2) the pre-heated gaseous ammonia exits the heat exchange catalyst unit and flows to the electric catalyst unit, and

(3) the pre-heated gaseous ammonia undergoes the cracking process in the electric catalyst unit,

wherein hydrogen resulting from ammonia cracking flows from the electric catalyst unit to the heat exchange unit,

wherein heat is transferred from the hydrogen to the gaseous ammonia within the heat exchange unit, resulting in cooled hydrogen, and

wherein the injection system utilizes the cooled hydrogen and residual liquid ammonia as co-fuels to power the internal combustion engine.

16. The on-board ammonia cracking system of claim 15 , wherein the electric catalyst unit includes an electric heater.

17. The on-board ammonia cracking system of claim 16 , wherein the electric heater is selected from a group consisting of an air process heater, a cartridge heater, a tubular heater, a band heater, a strip heater, an etched foil heater, a thin-film heater, a ceramic heater, a ceramic fiber heater, and a resistance wire.

18. The on-board ammonia cracking system of claim 15 , wherein the electric catalyst unit includes discrete catalyst media deposited within the electric catalyst unit.

19. The on-board ammonia cracking system of claim 15 , wherein the temperature sufficient to perform ammonia cracking ranges from 400° C. to 700° C.

20. The on-board ammonia cracking system of claim 15 , wherein channels are formed between a plurality of plates in the heat exchange catalyst unit, and wherein discrete catalyst media is deposited in the channels.

Continuity (4)
Continuation In Part 18241321 · Sep 1, 2023
Continuation In Part 17986265 · Nov 14, 2022
Provisional Application 63395820 · Aug 6, 2022
Related Publication 20240360804A1 · Oct 31, 2024
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