Granted Patent B2

US 12,374,703 · App. 16/695,280 · Granted Jul 29, 2025

Inventors: Timothy C. Geary (Stamford, CT); Timothy A. Barckholtz (Whitehouse Station, NJ); Jonathan Rosen (Morristown, NJ); Sandipan K. Das (Spring, TX); Carl A. Willman (Newtown, CT); Abdelkader Hilmi (Bethel, CT); Chao-Yi Yuh (New Milford, CT)

Assignees: ExxonMobil Technology and Engineering Company; FUELCELL ENERGY, INC.

H01M8/026H01M8/145H01M2008/147

Abstract

Claims (16)

1. A method for producing electricity in a molten carbonate fuel cell, the method comprising:

introducing an anode input stream comprising H 2 , a reformable fuel, or a combination thereof into an anode gas collection volume, the anode gas collection volume being defined by an anode surface, a first separator plate, and an anode collector providing support between the anode surface and the first separator plate;

introducing a cathode input stream comprising O 2 and CO 2 into a cathode gas collection volume, the cathode gas collection volume being defined by a cathode surface, a second separator plate, and a cathode collector providing support between the cathode surface and the second separator plate; and

operating the molten carbonate fuel cell at a transference of 0.97 or less and an average current density of 60 mA/cm 2 or more to generate electricity, an anode exhaust comprising H 2 , CO, and CO 2 , and a cathode exhaust comprising 2.0 vol % or less CO 2 , 1.0 vol % or more O 2 , and 1.0 vol % or more H 2 O, wherein transference is a fraction equal to carbonate ions transported across a molten carbonate electrolyte over total ions transported across the molten carbonate electrolyte,

wherein the cathode gas collection volume is further defined by one or more baffles in contact with the second separator plate, the one or more baffles reducing an unblocked flow cross-section of the cathode gas collection volume by 10% or more.

2. The method of claim 1 , wherein the transference is 0.95 or less.

3. The method of claim 1 , wherein the one or more baffles reduce the unblocked flow cross-section by 25% to 80%.

4. The method of claim 1 , wherein the one or more baffles are aligned substantially perpendicular to a direction of flow in the cathode gas volume.

5. The method of claim 1 , wherein an open area of the cathode surface is 50% or less.

6. The method of claim 1 , wherein an open area of the cathode surface is 45% or more.

7. The method of claim 1 , wherein the cathode collector comprises the one or more baffles.

8. The method of claim 1 , wherein the one or more baffles are attached to the second separator plate.

9. The method of claim 1 , wherein the cathode input stream comprises 5.0 vol % or less of CO 2 , or wherein the cathode exhaust comprises 1.0 vol % or less of CO 2 , or a combination thereof.

10. The method of claim 1 , wherein a voltage drop across the cathode is 0.4 V or less, or wherein the electricity is generated at a voltage of 0.55 V or more, or a combination thereof.

11. The method of claim 1 , wherein a fuel utilization in the anode is 60% or more, or wherein a fuel utilization in the anode is 55% or less.

12. The method of claim 1 , wherein a H 2 concentration in the anode exhaust is 5.0 vol % or more, or wherein a combined concentration of H 2 and CO in the anode exhaust is 6.0 vol % or more, or a combination thereof.

Assignments (2)

Continuity (2)

References Cited (400)