Granted Patent B2

US 12,240,755 · App. 17/367,905 · Granted Mar 4, 2025

Inventors: Sai P. Katikaneni (Dhahran, SA); Kunho Lee (Dhahran, SA); Joongmyeon Bae (Daejeon, KR); WooChul Jung (Daejeon, KR)

Assignees: Saudi Arabian Oil Company; Korea Advanced Institute of Science and Technology

C01B3/047C25B1/02C25B9/17C25B11/061C25B11/0773

Abstract

Claims (20)

1. A method of converting ammonia to hydrogen gas (H 2 ) in a fuel cell comprising:

passing the ammonia under pressure to a pressurized anode of the fuel cell utilizing a booster pump, wherein the fuel cell comprises the pressurized anode having an ammonia decomposition catalyst, a pressurized cathode, and a proton-conducting electrolyte disposed between the pressurized anode and the pressurized cathode,

decomposing the ammonia into nitrogen gas (N 2 ), electrons (e−), and protons (H+);

purging the nitrogen gas (N 2 ) from the pressurized anode utilizing an exhaust line comprising a back pressure regulator;

passing the protons (H+) through the proton conducting electrolyte and into the pressurized cathode;

passing the electrons (e−) from the pressurized anode to the pressurized cathode, wherein the protons (H+) accept the electrons (e−) to yield the hydrogen (H 2 ) under pressure; and

passing the hydrogen under pressure from the pressurized cathode through a relief valve, wherein the combination of the booster pump, the back pressure regulator in the exhaust line, and the relief valve pressurize the pressurized anode and the pressurized cathode.

2. The method according to claim 1 , wherein the proton-conducting electrolyte comprises a solid oxide electrolyte.

3. The method according to claim 1 , wherein the proton-conducting electrolyte comprises doped barium cerate or barium zirconate.

4. The method according to claim 1 , wherein the ammonia decomposition catalyst comprises a metal-based decomposition catalyst.

5. The method according to claim 4 , wherein the metal-based decomposition catalyst comprises one or more metals selected from the group consisting of nickel, cobalt, iron, ruthenium, and combinations thereof.

6. The method according to claim 1 , wherein the pressurized anode comprises a composite of nickel and electrolyte.

7. The method according to claim 6 , wherein the electrolyte of the composite comprises doped barium cerate, doped barium zirconate, SrCeO 3 , BaZrO 3 , or combinations thereof.

8. The method according to claim 1 , wherein the pressurized cathode comprises a perovskite.

9. The method according to claim 1 , further comprising:

purging excess ammonia along with the nitrogen gas utilizing the exhaust line;

exposing the nitrogen gas and the excess ammonia to a chiller, thereby forming chilled nitrogen gas and chilled ammonia; and

separating the chilled ammonia from the chilled nitrogen gas.

10. The method according to claim 9 , further comprising recycling the chilled ammonia along with the ammonia to the pressurized anode to form additional nitrogen gas (N 2 ) and protons (H+).

11. The method according to claim 1 , wherein the relief valve is connected to a hydrogen tank, such that passing the hydrogen under pressure from the pressurized cathode through the relief valve passing the hydrogen under pressure to the hydrogen tank.

Assignments (2)

Continuity (2)

References Cited (65)