Chemistry: electrical current producing apparatus – product – and – With pressure equalizing means for liquid immersion operation
Reexamination Certificate
2000-06-12
2002-08-27
Brouillette, Gabrielle (Department: 1745)
Chemistry: electrical current producing apparatus, product, and
With pressure equalizing means for liquid immersion operation
C429S010000, C429S010000, C429S010000, C429S006000, C429S006000, C429S006000, C429S006000, C429S010000
Reexamination Certificate
active
06440595
ABSTRACT:
BACKGROUND OF THE INVENTION
The present invention relates to a fuel cell system comprising a fuel cell which includes a feed line for a fuel and a feed line for an oxidant.
Fuel cells have been known for a long time and have become considerably more important in recent years, particularly in the automotive industry.
Similarly to battery systems, fuel cells generate electrical energy by chemical means. In a fuel cell, the individual reactants are supplied continuously (anode gas and cathode gas) and the reaction product is discharged continuously (anode off-gas and cathode off-gas). Fuel cells operate on the principle that electrically neutral molecules or atoms combine with one another and exchange electrons in the process. This phenomenon is referred to as a redox process. In the fuel cell, the oxidation and reduction processes are spatially separated, which can be achieved via a membrane, for example. Such membranes have the property of exchanging protons, but retaining gases. The electrons given off in the reduction can be passed as a current through a load, for example the electric motor of a motor vehicle.
Examples of gaseous reactants used for a fuel cell are hydrogen as the fuel gas (anode gas) and oxygen as the oxidant (cathode gas). If the fuel cells are to be operated with a fuel which is readily available and can easily be stored, e.g. natural gas or methanol, these hydrocarbons must first be converted into a hydrogen-rich gas, which can be achieved, for example, by reforming.
For a fuel cell to properly function, the membrane must be moistened continuously during operation. Since generating current and heat in the fuel cell produces water in the corresponding reactions, this water is used, as a rule, to moisten the membrane.
Moistening the fuel cell membrane by the customarily employed manner has a drawback, however, in that, particularly during the start-up phase of the fuel cell system, no water has at that time yet been produced. Nevertheless, even at that time it is necessary to moisten the membrane of the fuel cell to prevent damage.
U.S. Pat. No. 5,786,104 discloses a fuel cell system having one feed line and discharge line each for a fuel and for an oxidant. The feed line for the fuel and/or the feed line for the oxidant is connected to a water reservoir. The feed lines are each provided with a static mixer which can be heated to evaporate the water supplied from the water reservoir and thus to moisten the fuel and/or oxidant which is supplied to the fuel cell. The problems associated with humidification at temperatures below the freezing point of water are not discussed in this publication.
On the basis of the prior art described, it is therefore an object of the present invention to provide a fuel cell system which avoids the drawbacks described. A particular object is to provide a fuel cell system in which, especially even during the start-up procedure of the fuel cell, sufficient moisture is available for moistening the fuel cell membrane and which is fully functional even at ambient temperatures below the freezing point of water.
SUMMARY OF THE INVENTION
The above stated object is obtained by a fuel cell system of the invention. In the fuel cell system, a heating means is provided to heat the fluid present in the fluid reservoir. The heating means is disposed in the feed line for the fuel and/or in the feed line for the oxidant and is selected so as to provide sufficient heating power to completely evaporate an antifreeze present in the fluid. The system includes apparatus for collecting, condensing and recycling the evaporated antifreeze into the fluid reservoir.
Via the fluid reservoir it is possible to humidify the fuel and/or the oxidant, the fuel cell membrane subsequently being moistened by the humidified gas streams. In particular, this ensures that the fuel cell membrane is moistened even during the start-up procedure of the fuel cell, since the gas streams entering the fuel cell initially will be sufficiently humid to moisten the fuel cell membrane thus preventing damage to the membrane as could arise if the membrane dries out.
The fluid contained in the fluid reservoir is therefore able, in particular, to bridge the interval between start-up and production of water in the fuel cell.
The fuel used for the fuel cell can, for example, be hydrogen obtained from methanol, gasoline, natural gas, methane, coal gas, biogas or the like, but is not limited thereto. The oxidant used can advantageously be oxygen.
If the fluid present in the fluid reservoir is water, methanol or some other antifreeze is additionally admixed to lower the freezing point. In any case, the antifreeze is selected so as to have a lower boiling point than the fluid. In this context, the heating means in the connection line of the fluid container for the feed line for the fuel and/or for the feed line for the oxidant is provided to distill the antifreeze from the water to ensure that the fuel cell is supplied with pure water only. Expediently, the heating means is disposed e.g. in an injection nozzle through which the water can be injected into the gas stream of the fuel and/or the oxidant for the fuel cell. The heating means is designed so as to provide sufficient thermal energy for complete evaporation of the antifreeze present in the water stream flowing through the connection line, before the water is mixed with the respective gas stream to be supplied to the fuel cell. The evaporated antifreeze is collected by means of suitable arrangements, is condensed and then recycled into the fluid reservoir.
The invention overcomes a hitherto significant problem, i.e. that the fuel cell system can be operated even at temperatures below 0° C. The difficulty, after all, is that the fluid in the fluid reservoir, particularly if water is used, can freeze at such low temperatures. Consequently, adequate moistening of the fuel cell membrane during the start-up phase of the fuel cell would no longer be guaranteed. The antifreeze prevents freezing of the fluid. Using the heating means ensures that the antifreeze present in the fluid is distilled out before the fluid is admixed with the gas stream to be supplied to the fuel cell.
In a preferred embodiment, a fluid reservoir is provided to hold a fluid for humidifying the fuel and/or the oxidant. Advantageously, water is used as an appropriate fluid, water being suitable for humidifying the oxidant and/or the fuel and for moistening the membrane of the fuel cell.
Depending on the requirements and the specific application it is possible for only one of the oxidant or fuel to be humidified. Equally, however, it is possible to humidify both the fuel and the oxidant.
The heating means is preferably an electric heater. The electric heater is advantageously disposed in the fluid reservoir. The electrical energy required is initially, i.e. while the fuel cell is being started up, supplied by an electric battery. The electric heater can for example be configured as a heating filament, heating coil or the like, without being limited thereto, however.
In another embodiment, the heating means can include a flow conduit for a heating medium. In such an arrangement, the flow conduit is a coiled pipe or the like to increase its heat exchange area. The flow conduit has the heating medium flowing through it resulting in heat being exchanged between the heating medium and the fluid.
The heating means is preferably designed as a closed system. Thus the quantity of heating medium circulating in the flow conduit can be reduced, since no heating medium can escape from the flow conduit during a circulation cycle.
Advantageously, provision is made, in the flow conduit, for a delivery means for the heating medium. Via such a delivery means it is possible to adjust the flow rate of the heating medium within the flow conduit as required. The fact is that the flow rate of the heating medium affects the rate at which heat is exchanged between the heating medium and the fluid present in the fluid reservoir.
Different designs are possible for the delivery means depending on
Herdeg Wolfgang
Zapp Thomas
Brouillette Gabrielle
Cohen & Pontani, Lieberman & Pavane
Martin Angela J.
Siemens AG
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