US2003203264A1PendingUtilityA1
Maximizing PEM fuel cell power plant system efficiency at optimum system pressure
Priority: Apr 24, 2002Filed: Apr 24, 2002Published: Oct 30, 2003
Est. expiryApr 24, 2022(expired)· nominal 20-yr term from priority
H01M 8/04291H01M 8/1007H01M 8/04097H01M 8/04089H01M 8/10H01M 8/04Y02E60/50
39
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Abstract
A PEM fuel cell power plant system ( 10 ) has a process air pump ( 26 ), which may be a fan, a blower or a compressor, with an adiabatic efficiency of between 40% and 70%. The process air at the inlet 27 of the cathode reactant gas flow field 16 is between 1.07 atmospheres and 1.85 atmospheres, and may be at an optimal pressure for maximum overall system efficiency P={ 0.45+2.6 E− 1.8 E 2 }atms± 0.2 atms where P is the air inlet pressure and E is the adiabatic efficiency of the process air pump.
Claims
exact text as granted — not AI-modifiedWe claim:
1 . A fuel cell power plant comprising:
a plurality of fuel cells, each including a proton exchange membrane having a cathode catalyst on a first surface and an anode catalyst on a second surface opposite to said first surface; a cathode flow field plate adjacent to said cathode catalyst and having an oxidant reactant gas flow field; an anode flow field plate adjacent to said anode catalyst and having a fuel reactant gas flow field; a source for providing hydrogen-containing gas to said fuel reactant gas flow field; and an air pump for pumping air from the earth's atmosphere to said oxidant reactant gas flow field; characterized by the improvement comprising:
said pump having an adiabatic efficiency, E, of between 0.3 and 0.70 and providing air to said oxidant reactant gas flow field at a pressure, P, substantially equal to:
P={ 0.45+2.6 E− 1.8 E 2 }atms± 0.2 atms
2 . A fuel cell power plant comprising:
a plurality of fuel cells, each including a proton exchange membrane having a cathode catalyst on a first surface and an anode catalyst on a second surface opposite to said first surface; a cathode flow field plate adjacent to said cathode catalyst and having an oxidant reactant gas flow field; an anode flow field plate adjacent to said anode catalyst and having a fuel reactant gas flow field; a source for providing hydrogen-containing gas to said fuel reactant gas flow field; and an air pump for pumping air from the earth's atmosphere to said oxidant reactant gas flow field; characterized by the improvement comprising:
said pump having an adiabatic efficiency, E, of between 0.40 and 0.70 and providing air to said oxidant reactant gas flow field at a pressure between 1.07 atmospheres and 1.85 atmospheres.
3 . A fuel cell power plant according to claim 2 wherein:
said pump has an adiabatic efficiency between about 0.40 and about 0.50, and air is provided to said oxidant reactant gas flow field at a pressure between 1.10 atmospheres and 1.50 atmospheres.
4 . A fuel cell power plant according to claim 2 wherein:
said pump has an adiabatic efficiency between about 0.50 and about 0.70, and air is provided to said oxidant reactant gas flow field at a pressure between 1.20 atmospheres and 1.70 atmospheres.Cited by (0)
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