This application relates to methods and systems that facilitate the separation of fuel cell gases from cooling water.
Fuel cells are known and, typically, include a cathode and anode separated by a membrane. A fuel supply supplies a fuel, such as hydrogen, across the anode. An oxygen containing gas is driven across the cathode. The oxygen containing gas may be oxygen, air, or some other gas including oxygen.
Cooling water is driven across the cathode, often separate from the cathode by a wick layer. As part of the process, the gases, such as hydrogen and oxygen, may become entrained in the cooling water.
For a number of reasons, it is not desirable to have these gases entrained in the cooling water. In many fuel cell applications, the gases are simply allowed to escape from the cooling water, such as at a cooling water accumulator. Such applications may be vehicles utilized on land.
However, there are other applications wherein the vehicle containing the fuel cell is not allowed to have any waste emissions.
A fuel cell has an anode and a cathode separated by a membrane. A source of fuel is provided for passing a fuel across the anode. A source of oxygen containing gas is provided for passing oxygen across a cathode. A cooling water circuit is associated with an accumulator and for supplying cooling water to cool the cathode, and to return the cooling water from the cathode back to the accumulator. A system removes entrained gases from the water returned to the accumulator and returns the removed gases to the cathode.
A vehicle with such a fuel cell is also disclosed.
These and other features may be best understood from the following drawings and specification.
A fuel cell 20 is shown schematically mounted within a vehicle 22, which may be an underwater vehicle, such as an unmanned underwater vehicle.
An anode 24 receives a supply of fuel 26 and an inlet 27 leads across the anode 24. An outlet 29 returns the fuel to the inlet 27. The fuel may be hydrogen in some applications. A membrane 28 separates the anode 24 from a cathode 32. The cathode 32 receives a supply 36 of an oxygen containing gas, such as from an oxygen tank 34. It should be understood the oxygen containing gas may also be air or oxygen mixed with nitrogen, or some other carrier gas. The oxygen containing gas is returned at 38 to the inlet 36. A cooling water channel 40 may cool the cathode. A water accumulator 42 supplies water through an inlet 44 to the cooling water channels 40 and a return line 46 returns the water.
As known, energy is generated by the fuel cell 20 and delivered to a use 30. This aspect may be as known in the prior art.
As the fuel cell 20 operates, fuel and oxygen may pass into the cooling water flow and be mixed within the water. This can become undesirable and may result in the pressure within the accumulator 42 increasing to undesired levels.
Thus, as shown in
Over time any entrapped oxygen or hydrogen in the water in accumulator 142 will be removed in this matter and returned across the cathode 132.
If oxygen is the gas in the tank 34, the gas passing through the recycle line 138, 154 will be largely oxygen. On the other hand, the recycle line may be charged with a carrier gas. In fact, if air is the “oxygen containing gas,” the gas at 178, 152, 154 will be largely nitrogen other than the gases removed from the water.
In either instance, it is desirable to minimize the percentage of hydrogen which may be entrained in this gas. As an example, hydrogen may be maintained at a fraction of less than 5%.
In the
It should be understood the expanding chamber device 151 could be a bladder or bulb, and would operate in the same manner. A valve 153 is positioned on a return line 255 and is shown closed in the
Generally, several embodiments have been disclosed which will remove gases from the cooling water and return them to the fuel cell for use. In this manner, no waste emission is required.
It should be understood that the fuel could be entrained as part of the removed gases, and in that sense, the gases are not “returned” to the cathode, but instead sent to the cathode. Still, the oxygen removed would be returned to the cathode. While the disclosure shows sending the removed gases to the cathode, it should be understood that in certain applications, the removed gases can be sent to the anode.
Although an embodiment of this invention has been disclosed, a worker of ordinary skill in this art would recognize that certain modifications would come within the scope of this invention. For that reason, the following claims should be studied to determine the true scope and content of this invention.