High power density solid oxide fuel cell steam reforming system and process for electrical generation
A system comprising: a solid oxide fuel cell having an anode and a cathode; an anode recycle loop; and an adiabatic steam reformer positioned in the anode recycle loop.
1. A system comprising:
a solid oxide fuel cell having an anode gas inlet, an anode gas outlet, a cathode gas inlet, and a cathode gas outlet;
an adiabatic steam reformer fluidly coupled to the anode gas outlet, the anode gas inlet, and to a fuel supply, the adiabatic steam reformer being directly coupled from the anode gas outlet;
a heat recuperator fluidly coupled to the cathode gas outlet;
a combustor fluidly coupled to the cathode gas outlet of the heat recuperator;
a first conduit fluidly coupled from the anode gas outlet to the adiabatic steam reformer thereby forming an anode recycle loop; and
a second conduit directly leading from the first conduit to the combustor such that the combustor is also fluidly coupled to the anode gas outlet,
wherein the adiabatic steam reformer does not include means for introducing steam into the reformer except via the anode recycle loop, the anode recycle loop does not include any separation means for removing water or CO 2 , and the adiabatic steam reformer is not fluidly coupled to the cathode gas outlet; and
wherein the system does not include another combustor separate from the combustor fluidly coupled to the cathode gas outlet of the heat recuperator.
2. The system of claim 1 , wherein a combusted gas outlet of the combustor is fluidly coupled to an expander, the expander is coupled to a compressor, and the compressor has an air inlet and a compressed air outlet fluidly coupled to the cathode gas inlet.
3. The system of claim 2 , wherein the heat recuperator has a first flow path in fluid communication between the cathode gas outlet and the combustor, and a second flow path in fluid communication between the compressed air outlet and the cathode gas inlet.
4. The system of claim 1 , wherein the combustor is configured for combusting anode exhaust gas and cathode exhaust gas.
5. The system of claim 1 , wherein the system is configured such that 80% to 95% of the gas exiting the anode gas outlet is introduced into the adiabatic steam reformer via the anode recycle loop.
6. The system of claim 1 , wherein the system is configured such at least 90% of the gas exiting the anode gas outlet is introduced into the adiabatic steam reformer via the anode recycle loop.
7. An electrical generation system comprising the system of claim 1 .
8. The system of claim 7 , wherein the system is an on-board electrical generation system for an aircraft.
9. The system of claim 7 , wherein the system includes:
a plurality of solid oxide fuel cells arranged in a plurality of solid oxide fuel cell stacks along an axial direction;
and a plurality of adiabatic steam reformers arranged in the same axial direction,
wherein each individual adiabatic steam reformer is positioned adjacent to the solid oxide fuel cell stacks along the axial direction.
10. The system of claim 9 , wherein each individual adiabatic steam reformer is positioned to form a line parallel to the line formed by the individual fuel cell stacks arranged in a row along the axial direction.
11. The system of claim 9 , wherein the fuel cell stacks and the adiabatic steam reformers are housed within an insulated pressure vessel.