A high-temperature proton exchange membrane (PEM) fuel cell system may be air-cooled. Such a fuel cell system may comprise a stack of fuel cells with cooling plates interspersed within the stack. The cooling plates each may comprise airflow channels through which a cooling air passes to cool the fuel cells. Heat from the fuel cell stack is conducted to cooling plates, and removed from the plates by air flowing through the airflow channels.
One type of high-temperature PEM fuel cell utilizes an electrolyte membrane formed from polybenzimidazole (PBI) and phosphoric acid. Such fuel cells are often operated at temperatures within a range of 120° C. to 180° C., depending upon a specific fuel cell system design. In such a fuel cell, operating the fuel cell at too high of temperatures may damage the fuel cell system, while operating the fuel cell at too low of temperatures may limit cell performance and cause irrecoverable damage.
Various embodiments related to the air-cooled thermal management of a fuel cell stack are disclosed herein. For example, one disclosed embodiment comprises a cooling plate apparatus for an air-cooled fuel cell stack. The cooling plate comprises a body configured to receive heat from one or more fuel cells in thermal communication with the body. The cooling plate further comprises one or more airflow channels formed in the body and configured to allow a flow of a cooling air to pass across the body. Further, an insulating structure is disposed in the airflow channels, wherein the insulating structure has decreasing thickness from a cooling air inlet toward a cooling air outlet.
This Summary is provided to introduce a selection of concepts in a simplified form that are further described below in the Detailed Description. This Summary is not intended to identify key features or essential features of the claimed subject matter, nor is it intended to be used to limit the scope of the claimed subject matter. Furthermore, the claimed subject matter is not limited to implementations that solve any or all disadvantages noted in any part of this disclosure.
Continuing with
Due to the nature of heat transfer between air and metal, the cooling air may initially increase in temperature relatively rapidly as it flows through airflow channels 106. Because a rate of heat transfer between cooling plate 102 and the air is a function of a temperature difference between cooling plate 102 and the air, as the temperature of the cooling air rises, the rate of heat transfer slows. Due to the rapid initial heating of the cooling air, fuel cells 104 may have lower temperatures in the regions adjacent to a cooling air inlet of cooling plate 102 than in the regions adjacent to a cooling air outlet of cooling plate 102. Under some operating conditions, this non-uniform temperature profile, which may be referred to as an in-plane temperature difference across the fuel cell, may be sufficiently high such that portions of the fuel cell may be outside of the operating temperature range. As a result, performance of the fuel cell may be impaired or rapid degradation may take place.
Therefore, to help reduce the non-uniformity of the temperature across cooling plate 102, an insulating structure may be applied to cooling plate 102 in such a manner that heat is transferred to the cooling air more slowly toward the cooling air inlet of cooling plate 102, and then transferred more rapidly at a location toward the cooling air outlet of the cooling plate 102. For example,
In this manner, insulating structure 202 has a decreasing thickness from the cooling air inlet 110 toward a cooling air outlet 112 of cooling plate 102. The term “decreasing thickness” signifies any configuration in which the insulating structure has a greater thickness toward the inlet than toward the outlet, including but not limited to a zero thickness (i.e. no insulating structure) toward the outlet, as shown in
In embodiments in which the insulating structure covers only a portion of a cooling channel, insulating structure 202 may extend any suitable distance from the cooling air inlet toward the cooling air outlet. Suitable distances may depend upon the thermal characteristics of a specific fuel cell system. For example, the insulating structure may be located wholly within a front half of the cooling plate relative to a distance between the cooling air inlet and the cooling air outlet. In the specific embodiment of
Insulating structure 202 may restrict heat flow into the cooling air where it is present, such that heat is transferred between fuel cells 104 and the cooling air more slowly. Therefore, in the configuration described above, heat may be transferred more slowly to the cooling air as it first enters cooling plate 102, which may prevent over-cooling the portions of fuel cells 104 adjacent to cooling air inlet 110. Likewise, this also may help to prevent under-cooling of the portions of fuel cells 104 adjacent to cooling air outlet 112. Thus, cooling plate 102 depicted in
Any suitable material or materials may be used as insulating structure 202.
Continuing with
As mentioned above, an insulating structure may comprise more than one layer of insulating material.
An insulating structure comprising two layers or more layers of insulating material, such as insulating structure 414, may allow for flexibility in constructing a desired insulating profile. For example, layers 414 create a stair-step profile of decreasing thickness. In a similar matter, further layers may be added to create additional steps for further thickness adjacent to the cooling air inlet.
Any suitable method may be used to form an insulating structure as disclosed herein. Suitable methods include, but are not limited to, those that allow a layer of an insulating material of a desired thickness to be controllably deposited. Examples of such suitable methods may include, but are not limited to, dip coating, sputtering, chemical vapor deposition, evaporation, painting, and other such deposition methods.
One such method utilizing the above-described adhesive and microballons is depicted as method 500 in
Method 500 at 504 next comprises applying a single layer of insulating material to the cooling plate. In one embodiment, spherical glass microballoons may be used as the insulating material. The insulating material may be applied by dip coating, or in any other suitable manner. Method 500 next comprises, at 506, heating the cooling plate to cure the adhesive and secure the insulating material. In embodiments where rosin is used as the adhesive and spherical glass microballoons are used as the insulating material, heating the cooling plate may cause the rosin to convert to a rigid varnish-like coating that maintains good adhesion to the glass microballoons at high temperature and cooling air flow rates.
First referring to the uninsulated (“uncoated” in
It will be understood that the embodiments described herein are exemplary in nature, and that these specific embodiments or examples are not to be considered in a limiting sense, because numerous variations are contemplated. Accordingly, the present disclosure includes all novel and non-obvious combinations and sub-combinations of the various embodiments disclosed herein, as well as any and all equivalents thereof.
Number | Name | Date | Kind |
---|---|---|---|
4324844 | Kothmann | Apr 1982 | A |
4548196 | Torobin | Oct 1985 | A |
6773841 | Rapaport et al. | Aug 2004 | B2 |
7125624 | Tanno | Oct 2006 | B2 |
20030096147 | Badding et al. | May 2003 | A1 |
20050136317 | Ferguson | Jun 2005 | A1 |
20060127729 | Roscoe et al. | Jun 2006 | A1 |
20060204796 | Potnis | Sep 2006 | A1 |
20070003814 | Fisher et al. | Jan 2007 | A1 |
20080053592 | Khadilkar et al. | Mar 2008 | A1 |
Number | Date | Country | |
---|---|---|---|
20100216044 A1 | Aug 2010 | US |