Patent Application
20050175875
1. Field of the Invention
The present invention relates to electrochemical fuel cells and more particularly to subsystems and methods for controlling the temperature of a fuel cell system during startup.
2. Description of the Related Art
Electrochemical fuel cells convert reactants, namely fuel and oxidant fluid streams, to generate electric power and reaction products. Electrochemical fuel cells employ an electrolyte disposed between two electrodes, namely a cathode and an anode. The electrodes each comprise an electrocatalyst disposed at the interface between the electrolyte and the electrodes to induce the desired electrochemical reactions. The location of the electrocatalyst generally defines the electrochemically active area.
Polymer electrolyte membrane (PEM) fuel cells generally employ a membrane electrode assembly (MEA) consisting of an ion-exchange membrane disposed between two electrode layers comprising porous, electrically conductive sheet material as fluid diffusion layers, such as carbon fiber paper or carbon cloth. In a typical MEA, the electrode layers provide structural support to the ion-exchange membrane, which is typically thin and flexible. The membrane is ion conductive (typically proton conductive), and also acts as a barrier for isolating the reactant streams from each other. Another function of the membrane is to act as an electrical insulator between the two electrode layers. The electrodes should be electrically insulated from each other to prevent short-circuiting. A typical commercial PEM is a sulfonated perfluorocarbon membrane sold by E.I. Du Pont de Nemours and Company under the trade designation NAFION®.
The MEA contains an electrocatalyst, typically comprising finely comminuted platinum particles disposed in a layer at each membrane/electrode layer interface, to induce the desired electrochemical reaction. The electrodes are electrically coupled to provide a path for conducting electrons between the electrodes through an external load.
In a fuel cell stack, the MEA is typically interposed between two separator plates that are substantially impermeable to the reactant fluid streams. The plates act as current collectors and provide support for the electrodes. To control the distribution of the reactant fluid streams to the electrochemically active area, the surfaces of the plates that face the MEA may have open-faced channels formed therein. Such channels define a flow field area that generally corresponds to the adjacent electrochemically active area. Such separator plates, which have reactant channels formed therein are commonly known as flow field plates. In a fuel cell stack a plurality of fuel cells are connected together, typically in series, to increase the overall output power of the assembly. In such an arrangement, one side of a given plate may serve as an anode plate for one cell and the other side of the plate may serve as the cathode plate for the adjacent cell. In this arrangement, the plates may be referred to as bipolar plates.
The fuel fluid stream that is supplied to the anode typically comprises hydrogen. For example, the fuel fluid stream may be a gas such as substantially pure hydrogen or a reformate stream containing hydrogen. Alternatively, a liquid fuel stream such as aqueous methanol may be used. The oxidant fluid stream, which is supplied to the cathode, typically comprises oxygen, such as substantially pure oxygen, or a dilute oxygen stream such as air. In a fuel cell stack, the reactant streams are typically supplied and exhausted by respective supply and exhaust manifolds. Manifold ports are provided to fluidly connect the manifolds to the flow field area and electrodes. Manifolds and corresponding ports may also be provided for circulating a coolant fluid through interior passages within the stack to absorb heat generated by the exothermic fuel cell reactions. The preferred operating temperature range for PEM fuel cells is typically 50° C. to 120° C., most typically between 75° C. and 85° C.
Under typical conditions, start-up of the electrochemical fuel cell stack is under high ambient temperatures and the fuel cell stack can be started in a reasonable amount of time and quickly brought to the preferred operating temperature. In some fuel cell applications, it may be necessary or desirable to commence operation of an electrochemical fuel cell stack when the stack core temperature is below the freezing temperature of water and even at subfreezing temperatures below −25° C. However, at such low temperatures, the fuel cell stack does not operate well and rapid start-up of the fuel cell stack is more difficult. It may thus take a considerable amount of time and/or energy to take an electrochemical fuel cell stack from a cold starting temperature below the freezing temperature of water to efficient operation.
In U.S. Pat. No. 6,358,638, a method of heating a cold MEA to accelerate cold start-up of a PEM fuel cell is disclosed. In the '638 patent, either fuel is introduced into the oxidant stream or oxidant is introduced into the fuel stream. The presence of platinum catalyst on the electrodes promotes an exothermic chemical reaction between hydrogen and oxygen which locally heats the ion-exchange membrane from below freezing to a suitable operating temperature. However, there remains a need in the art for more efficient methods of efficiently starting a fuel cell stack at low and sub-freezing temperatures. The present invention fulfills this need and provides further related advantages.
Significant improvements in start-up time from freezing or sub-freezing temperatures can be achieved by using a two pump—dual loop cooling subsystem. For example, in an electrochemical fuel cell system, the cooling subsystem may comprise both a startup coolant loop comprising a startup pump fluidly connected to the electrochemical fuel cell stack; and a standard coolant loop comprising a standard pump and a stack valve. The coolant volume of the startup coolant loop is less than the coolant volume in the standard coolant loop. During start-up, the stack valve is closed such that the electrochemical fuel cell stack is fluidly isolated from the standard coolant loop. Coolant in the startup loop circulates through the fuel cell stack and helps to quickly bring the temperature of the stack to desired temperature. If coolant did not flow through the stack, localized heating within the stack could detrimentally affect the stack. By minimizing the coolant volume in the startup loop, and in particular, by having a smaller coolant volume than in the standard coolant loop, more efficient heating can occur.
In an alternate embodiment, a cooling subsystem for an electrochemical fuel cell system may comprise a startup coolant loop fluidly connected to the electrochemical fuel cell. The startup coolant loop comprises a startup pump. The cooling subsystem also comprises a standard coolant loop comprising a standard pump and a stack valve. When the stack valve is closed, only the startup coolant loop is fluidly connected to the electrochemical fuel cell stack. However, when the stack valve is open, both the startup coolant loop and the standard coolant loop are fluidly connected to the fuel cell stack. Thus, a smaller coolant volume is available to the fuel cell stack during start-up when efficient heating is needed and a larger coolant volume is available during normal operation from both coolant loops. In a preferred embodiment, the startup coolant loop is also fluidly connected to the standard coolant loop when the stack valve is open. This is simpler to manufacture and allows the coolants to mix, thereby reducing thermal shock when the colder coolant from the standard coolant loop flows to the fuel cell stack. Nevertheless, both coolant loops could remain fluidly isolated throughout.
A method for operating the coolant subsystem for an electrochemical fuel cell system during startup comprises: (a) directing a first coolant through a fuel cell stack; and (b) directing a second coolant through the fuel cell stack when the temperature of either the fuel cell stack or the first coolant reaches a first predetermined temperature. The first coolant is fluidly isolated from the second coolant during the initial step (a). When the temperature of either the fuel cell stack or the coolant in the startup loop has reached the predetermined threshold value, the stack valve may be opened such that the electrochemical fuel cell stack becomes fluidly connected to the standard coolant loop and thereby allow additional cooling of the fuel cell stack. In an embodiment, coolant from the standard coolant loop mixes with the coolant in the startup loop when the stack valve opens.
In an embodiment, the first predetermined temperature is the desired operating temperature of the fuel cell system, for example, 60 to 80° C. In another embodiment, the predetermined temperature is less than the desired operating temperature, for example less than 60° C., more particularly less than 50° C. Typically such a predetermined temperature would be greater than 30° C. or greater than 40° C.
The startup loop may further comprise a heater to help quickly bring the temperature of the coolant up to desired temperature. To further minimize the coolant volume in the startup coolant loop, the loop may be integrated into the stack manifold. Other components in the coolant subsystem may include a compressor, a cathode feed heat exchanger, or a radiator. If the fuel cell system is used in a motor vehicle, the coolant subsystem may further comprise a propulsion system and/or a car heating system.
These and other aspects of the invention will be evident upon reference to the attached figures and following detailed description.
In the above figures, similar references are used in different figures to refer to similar elements.
Temperature regulation of a fuel cell system is typically performed with a coolant circulated throughout a coolant subsystem. Common coolants include, for example, water, ethylene glycol, propylene glycol, fluoroinerts, alcohols or a combination thereof. Choice of coolant is dictated in part, by the physical conditions the fuel cell is expected to be subjected to. For example, if the fuel cell stack will be operated in freezing or sub-freezing temperatures, a coolant would likely be chosen such that it did not freeze under such conditions. The primary purpose of a coolant is to regulate temperature and prevent over-heating of the fuel cell stack, as well as other components in the fuel cell system such as, for example, the compressor, cathode feed, propulsion system, car heating, motors, electronics, etc. During startup, and particularly when the fuel cell stack is subjected to freezing or sub-freezing temperatures, the coolant can also assist in bringing the fuel cell stack to its optimal operating temperature.
Other components may also be coupled to coolant subsystem 10 as needed, particularly as used in automotive applications. For example, a propulsion system 80 may be reversibly fluidly connected to coolant subsystem 10 by a propulsion valve 85. Similarly, a car heating system 95 may be reversibly fluidly connected to coolant subsystem 10 by a car heating valve 95. Thus the same coolant subsytem 10 used to regulate the temperature of fuel cell stack 20 may be used to regulate the temperature of a number of other components as needed.
At very cold temperatures, the viscosity of coolant in coolant loop A may be much higher than at warmer temperatures. This increased viscosity may affect the coolant flow rate and care should be taken that pump 55 maintains a sufficient coolant flow rate in coolant loop A. Otherwise localized heating may occur in fuel cell stack 20 leading to damage to individual cells from local overtemperature. However, when at freezing and sub-freezing temperatures, less heat is generated by fuel cell stack 20 and the individual fuel cells in stack 20 may absorb a significant amount of the heat that is generated so even with the increased viscosity, the coolant flow rate can be significantly less than that required at normal operating conditions. The flow rate is strongly dependent on stack design and materials and on the amount of heat generation in fuel cell stack 20 and can be easily determined by a person of ordinary skill in the art. Nevertheless, the coolant flow rate in coolant loop A during cold-start phase for a typical automotive fuel cell system can be as low as 5 to 25 slpm (standard litres per minute), more particularly 15 to 25 slpm for an 85 kW gross fuel cell stack and still meet cell cooling requirements with no local hot spots.
As fuel cell stack 20 heats up and coolant in coolant loop A similarly heats up, the viscosity drops and, depending on pump design (for example positive displacement or mixed flow), the flow rate will naturally increase. This natural increase in coolant flow rate may be sufficient in some fuel cell systems to meet the increased cooling requirements of fuel cell stack 20 during start-up. Thus, a low cost fixed speed pump may be all that is necessary in coolant loop A for pump 55. In comparison, pump 50 in coolant loop B may still have speed control to adjust flow rate of coolant during normal operation. Furthermore, during normal operation, pump 55 may be used to augment coolant flow through fuel cell stack 20 resulting in a smaller pump 50 than typically needed in a conventional cooling subsystem.
As coolant in coolant loop A heats up, it may expand and an expansion reservoir in coolant loop A (not shown) may be used to accommodate the increased coolant volume. In the embodiment illustrated in
Heater 25 may also be used to heat coolant in coolant loop A and assist with bringing fuel cell stack 20 to an operating temperature. A heater may also be used in conventional coolant designs or in coolant loop B (not shown). While heater 25 may be useful in some fuel cell systems, some heaters may not have the necessary heat flux to compensate for the increased thermal mass of the coolant needed to accommodate the heater itself.
The thermal mass of the coolant in coolant loop A may be minimized further by integration of coolant loop A into the fuel cell stack manifold (not shown).
When the temperature of either the coolant in coolant loop A or fuel cell stack 20 has reached a threshold temperature, stack valve 65 may open to begin letting coolant from coolant loop B in to fuel cell stack 20. This threshold temperature, may be, for example, between 30 and 80° C. In an embodiment, the threshold temperature is between 60 and 80° C., i.e., the normal operating temperature of fuel cell stack 20. In this embodiment, fuel cell stack 20 reaches its desired operating temperature in the minimum amount of time allowing greater power density to be drawn from fuel cell stack 20 at an earlier time. In another embodiment, the threshold temperature is at a temperature below 60° C., more particularly below 50° C. As cooler coolant from coolant loop B is introduced into warmer coolant in coolant loop A, a temperature gradient may develop. At lower temperatures, a fuel cell stack 20 can typically be subjected to higher temperature gradients without any adverse effects (for example, temperature gradients up to 30° C.). However, at 60 to 80° C., typical fuel cell stacks 20 can only safely be subjected to smaller temperature gradients, for example, less than 10° C. Accordingly, by having a lower threshold temperature (i.e., 30-60° C. instead of 60-80° C.) for letting coolant from coolant loop B into fuel cell stack 20, there is a reduced risk of damaging fuel cell stack 20 from thermal shock. Regardless of the threshold temperature, care should be taken to reduce the risk of thermal shock. This may be done, for example, by controlling the rate at which coolant from coolant loop B is introduced into coolant loop A.
In a further embodiment illustrated in
The additional precautions as shown in
A test chamber was constructed as illustrated in
Three different volumes of coolant were tested: standard coolant volume (5000 mL) for coolant path E, small coolant volume (1000 mL) for coolant path D and micro coolant volume (100 mL) for coolant path F.
While the above embodiments have been described with respect to automotive fuel cell applications, it is understood that the above embodiments could be adapted for any fuel cell application and in particular, any power generation applications where the unit is located outside or otherwise subjected to freezing or sub-freezing temperatures.
From the foregoing, it will be appreciated that, although specific embodiments of the invention have been described herein for purposes of illustration, various modifications may be made without deviating from the spirit and scope of the invention. Accordingly, the invention is not limited except as by the appended claims.
All of the above U.S. patents, U.S. patent application publications, U.S. patent applications, foreign patents, foreign patent applications and non-patent publications referred to in this specification and/or listed in the Application Data Sheet, are incorporated herein by reference, in their entirety.
This application relates to and claims priority benefits from provisional U.S. patent application Ser. No. 60/560,731 filed Feb. 9, 2004. The '731 application is incorporated herein by reference in its entirety.
| Number | Date | Country | |
|---|---|---|---|
| 60560731 | Feb 2004 | US |
