IP Library › Granted Patent US 12,537,208
Granted Patent B2
US 12,537,208 · App. 18/169,856 · Granted Jan 27, 2026

Anode recovery system of fuel cell

Inventors: Bing Yi Wu (Hsinchu County, TW); Feng Hsiang Hsiao (Hsinchu County, TW); Jheng-Yue Dong (Hsinchu County, TW); Ming-Yao Dong (Hsinchu County, TW); Ruei-Jing Lin (Hsinchu County, TW)
Assignee: Asia Hydrogen Energy
H01M8/04201H01M8/04097H01M8/04126H01M8/04156H01M8/04164H01M8/04395H01M8/04455H01M8/0447H01M8/04582H01M8/04746H01M8/04753H01M8/04783H01M8/04843H01M2008/1095
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Quick Facts
Patent No.
US 12,537,208
App. No.
18/169,856
Granted
Jan 27, 2026
Kind
B2
Abstract

Some embodiments of the disclosures provide an anode recovery system of a fuel cell. The anode recovery system includes a gas supply unit connected to a power generation unit, a gas-liquid separator connected to the power generation unit and a first anode gas recovery control component; and a storage tank connected to the gas-liquid separator and a cathode recovery system. The gas supply unit is configured to provide anode gas to the power generation unit. A first part of unreacted anode gas from the power generation unit mixes with the anode gas and flows back to the power generation unit sequentially via the gas-liquid separator and the first anode gas recovery control component. A second part of the unreacted anode gas and generated water are discharged from the power generation unit to the storage tank and is further discharged to the cathode recovery system.

Claims (21)

1 . An anode recovery system of a fuel cell, comprising:

a gas supply unit connected to a power generation unit, the gas supply unit being configured to provide anode gas to the power generation unit;

a gas-liquid separator connected to the power generation unit and a first anode gas recovery control component; and

a storage tank connected to the gas-liquid separator and a cathode recovery system;

wherein:

a first part of unreacted anode gas from the power generation unit mixes with the anode gas and flows back to the power generation unit sequentially via the gas-liquid separator and the first anode gas recovery control component;

a second part of the unreacted anode gas and generated water are discharged from the power generation unit to the storage tank and is further discharged to the cathode recovery system; and

the unreacted anode gas recycles only inside the anode recovery system, the cathode recovery system, and the power generation unit.

2 . The anode recovery system of claim 1 , wherein a buffer tank is set between the gas-liquid separator and the storage tank.

3 . The anode recovery system of claim 2 , wherein a second anode gas recovery control component is set between the gas-liquid separator and the buffer tank.

4 . The anode recovery system of claim 3 , wherein the second anode gas recovery control component is a positive flow controlling component or a passive flow controlling component.

5 . The anode recovery system of claim 3 , wherein the second anode gas recovery control component comprises at least one item selected from the group consisting of flow meter, gas pump, circulation pump, and restrictor valve.

6 . The anode recovery system of claim 3 , wherein, as the second anode gas recovery control component is activated, actuation of the first anode gas recovery control component is increased to stabilize anode operation pressure.

7 . The anode recovery system of claim 2 , wherein the buffer tank is pressure-adjustable such that an inner pressure of the buffer tank is between vacuum and 10 psia before the second part of the unreacted anode gas and generated water are discharged to the buffer tank from the gas-liquid separator.

8 . The anode recovery system of claim 1 , wherein the storage tank is pressure-adjustable such that an inner pressure of the storage tank is between vacuum and 10 psia before the second part of the unreacted anode gas and generated water are discharged to the storage tank from the gas-liquid separator.

9 . The anode recovery system of claim 1 , wherein the first anode gas recovery control component is a positive flow-control component or a passive flow-control component.

10 . The anode recovery system of claim 1 , wherein a cathode gas recovery control component is set in the cathode recovery system.

11 . The anode recovery system of claim 1 , wherein a gas concentration sensor is set in the cathode recovery system.

12 . The anode recovery system of claim 1 , wherein:

the second part of the unreacted anode gas discharged from the gas-liquid separator is discharged to the cathode recovery system; and

a concentration of the second part of the unreacted anode gas in the cathode recovery system is not higher than 1%.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 23, 2023
From: WU, BING YI; HSIAO, FENG HSIANG; DONG, JHENG-YUE; DONG, MING-YAO; LIN, RUEI-JING
To: ASIA HYDROGEN ENERGY
Reel/Frame 064045/0681 →
Continuity (2)
Provisional Application 63310151 · Feb 15, 2022
Related Publication 20230261217A1 · Aug 17, 2023
References Cited (5)
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