Fuel cell reactant inlet humidification
View Patent ↗In a proton exchange membrane fuel cell power plant ( 9 ) in which each of the fuel cells ( 11 ) employ reactant gas flow field channels ( 51 ) extending inwardly from a first surface of a conductive, water permeable reactant gas flow field plate ( 50 ), for at least one of the reactants of the fuel cell, a region ( 63 ) of the reactant gas flow field channels is substantially shallower than the remaining portion ( 60 ) of the flow field channels ( 51 ) thereby decreasing resistance to gas phase mass transfer from the wetted walls of the flow field plate to the gas in the region ( 63 ), the resulting increase in thickness of the web ( 58 ) adjacent the region ( 63 ) reduces the resistance to liquid water transport from the first coolant channel ( 52 ) to the inlet edge ( 55 ) of the plate ( 50 ) so that the plate supports a higher evaporation rate into the reactant gas in the shallow region ( 63 ).
1. A proton exchange membrane fuel cell having a planform, comprising:
an active area smaller than said planform;
a conductive water permeable plate coextensive with said planform and having (a) a plurality of reactant gas flow field channels extending inwardly from a first surface of said plate, said reactant gas flow field channels having reactant gas inlets at an edge of said plate, and (b) a plurality of water channels extending inwardly from a second surface of said plate opposite to said first surface, characterized by:
the depth of portions of said reactant gas flow field channels between said active area and said inlets being less than the depth of the remaining length of said reactant gas flow field channels.
2. A fuel cell according to claim 1 further characterized in that:
the portion of said reactant gas flow field channels upstream of said active area are between 30% and 50% less deep than the depth of the remaining length of said flow field channels.
3. A fuel cell according to claim 1 further characterized in that:
the portions of said reactant gas flow field channels upstream of said active area are between 25% and 50% of the thickness of said reactant gas flow field plate.
4. A fuel cell according to claim 1 further characterized in that:
the inlets are air inlets and the portion of the reactant gas flow field channels upstream of said active area are sufficiently shallow so as to increase the relative humidity of air flow entering said active area by between 15% and 25%, compared with the relative humidity of air flow entering said active area from reactant gas flow field channels having portions upstream of said active area substantially the same depth as the depth of the remaining lengths of said reactant gas flow field channels, when air flow is maximum.
5. A fuel cell power plant characterized by a stack of fuel cells according to claim 1 .
6. A method of improving humidification of reactant gas as it enters an active area of a proton exchange membrane fuel cell having reactant gas flow field plates which are conductive and water permeable, characterized by:
configuring the depth of reactant gas flow field channels in said reactant gas flow field plates, between the active area and inlets of the reactant gas flow field channels, to be more shallow than the depth of the remaining lengths of said flow field channels.
7. A method according to claim 6 further characterized in that:
configuring the portion of said reactant gas flow field channels upstream of said active area to be between 30% and 50% less deep than the depth of the remaining length of said reactant gas flow field channels.
8. A method according to claim 6 further characterized in that:
configuring the portions of said reactant gas flow field channels upstream of said active area to be between 25% and 50% of the thickness of said reactant gas flow field plate.
9. A method according to claim 6 further characterized in that:
the inlets are air inlets and said configuring comprises configuring the portion of the reactant gas flow field channels between said active area and said inlets to be sufficiently shallow so as to increase the relative humidity of air entering said active area by between 15% and 25% compared with relative humidity of air entering channels having the portions upstream of said active area the same depth as the depth of the remaining lengths of said flow field channels.
10. A method according to claim 6 further characterized in that:
the inlets are air inlets and said configuring comprises configuring the portion of the reactant gas flow field channels between said active area and said inlets to be sufficiently shallow so as to provide relative humidity if air entering said active area to be at least 55% when air flow is maximum.