Reactant management of a wet end cell in a fuel cell stack
In at least certain embodiments, the present invention relates to a fuel cell stack comprising a fuel cell assembly having opposite first and second ends, a wet end fuel cell adjacent the first end, a dry end fuel cell adjacent the second end, and a plurality of repeating fuel cells disposed between the wet end and dry end fuel cells. In at least certain embodiments, the wet end fuel cell comprises a unipolar plate and the repeating fuel cells each comprise one-half of each adjacent bipolar plate. In at least certain embodiments, the unipolar plate has a first oxidant rate, and at least one of the bipolar plates has a second oxidant rate, with the first oxidant rate being less than the second oxidant rate.
1 . A fuel cell stack comprising:
a fuel cell assembly having opposite first and second ends, a wet end fuel cell adjacent the first end, a dry end fuel cell adjacent the second end, and a plurality of repeating fuel cells disposed between the wet end and dry end fuel cells;
the wet end fuel cell comprising a unipolar plate;
the repeating fuel cells each comprising one-half of each adjacent bipolar plate; and
the unipolar plate having a first oxidant rate, and at least one of the bipolar plates having a second oxidant rate, the first oxidant rate being less than the second oxidant rate.
2 . The fuel cell stack of claim 1 wherein the unipolar plate has a first oxidant flow rate and the at least one bipolar plate has a second oxidant flow rate, the first oxidant flow rate being less than the second oxidant flow rate.
3 . The fuel cell stack of claim 2 wherein the unipolar plate has a first number of oxidant outlet openings and a second number of oxidant inlet openings, the first number being greater than the second number.
4 . The fuel cell stack of claim 2 wherein the unipolar plate has an oxidant inlet area and an oxidant outlet area, the oxidant outlet area being greater than the oxidant inlet area.
5 . The fuel cell stack of claim 4 wherein the unipolar plate has a first amount of total combined oxidant inlet openings and oxidant outlet opening, and the at least one bipolar plate has a second amount of total combined oxidant inlet openings and oxidant outlet openings, with the first amount being greater than the second amount.
6 . The fuel cell stack of claim 5 wherein the unipolar plate has a first number of oxidant outlet openings and a second number of oxidant inlet openings, the first number being greater than the second number.
7 . The fuel cell stack of claim 4 wherein the unipolar plate has a substantial number of oxidant inlet openings having a diameter that is smaller than the diameter of a substantial number of oxidant outlet openings of the unipolar plate such that the total area of the oxidant inlet openings is less than the total area of the oxidant outlet openings.
8 . The fuel cell stack of claim 1 further comprising a first oxidant system for supplying oxidant to the bipolar plates and a second oxidant system, separate from the first oxidant system, for supplying oxidant to the unipolar plate.
9 . The fuel cell stack of claim 8 wherein the first oxidant system provides a first oxidant rate to at least one of the bipolar plates and the second oxidant system provides a second oxidant rate to the unipolar plate, with the second oxidant rate being less than the first oxidant rate.
10 . The fuel cell stack of claim 4 wherein the first flow rate is less than 95% of the second flow rate.
11 . The fuel cell stack of claim 10 wherein the first flow rate is 60 to 92% of the second flow rate.
12 . A method of providing reactant to a wet end cell in a fuel cell stack, the method comprising operating a fuel cell system comprising the fuel cell stack, the fuel cell stack comprising a wet end fuel cell comprising a unipolar plate, a dry end fuel cell, and a plurality of repeating fuel cells disposed between the wet end and dry end fuel cells, each of the repeating fuel cells comprising one-half of each adjacent bipolar plate;
providing oxidant to the wet end unipolar plate having a first oxidant rate; and
providing oxidant to at least one of the bipolar plates having a second oxidant rate, the second oxidant rate being greater than the first oxidant rate.
13 . The method of claim 12 wherein the unipolar plate has an oxidant inlet area and an oxidant outlet area, the oxidant outlet area being greater than the oxidant inlet area.
14 . The method of claim 12 wherein the unipolar plate has a first oxidant flow rate and the at least one bipolar plate has a second oxidant flow rate, the first oxidant flow rate being less than the second oxidant flow rate.
15 . The method of claim 12 wherein the unipolar plate has a first number of oxidant outlet openings and a second number of oxidant inlet openings, the first number being greater than the second number.
16 . The method of claim 14 wherein the unipolar plate has a substantial number of oxidant outlet openings having a diameter that is greater than the diameter of a substantial number of oxidant inlet openings of the unipolar plate such that the total area of the oxidant output openings is greater than the total area of the oxidant inlet openings.
17 . The method of claim 14 wherein the first flow rate is less than 95% of the second flow rate.
18 . The method of claim 17 wherein the first flow rate is 60 to 92% of the second flow rate.
19 . The method of claim 12 further comprising a first oxidant system for supplying oxidant to the bipolar plates and a second oxidant system, separate from the first oxidant system, for supplying oxidant to the unipolar plate, wherein the first oxidant system provides a first oxidant rate to at least one of the bipolar plates and the second oxidant system provides a second oxidant rate to the unipolar plate, with the second oxidant rate being less than the first oxidant rate.
20 . A fuel cell stack comprising:
a fuel cell assembly having opposite first and second ends, a wet end fuel cell adjacent the first end, a dry end fuel cell adjacent the second end, and a plurality of repeating fuel cells disposed between the wet end and dry end fuel cells;
the wet end fuel cell comprising a unipolar plate having a first oxidant flow rate;
the repeating fuel cells each comprising one-half of each adjacent bipolar plate with at least one of the bipolar plates having a second oxidant flow rate, the first oxidant flow rate being less then the second oxidant flow rate; and
the unipolar plate having a first number of oxidant inlet openings and a second number of oxidant outlet openings, with the second number being greater than the first number such that the first oxidant flow rate is less than 93% of the second oxidant flow rate.