None.
This invention relates to a method for compressing a solid oxide fuel cell stack.
A solid oxide fuel cell (SOFC) stack can be subjected to various interruptions that can prevent or reduce electricity from being generated. One of those interruptions can be cell(s) cracking, which is usually a result of the stack pressure in a SOFC system exceeding the strength of the SOFC cells. Another interruption that can occur is the leaking of gases through compressive seals.
In conventional SOFC stack designs based on simple mechanics such as springs, pressure will increase or decrease with temperature-caused expansion or contraction during SOFC startup and operation due to a linear correlation between spring force and spring displacement. At some point, the stress placed on the cells may exceed the cell strength resulting in cell cracking and thus stack failure. On the other hand, pressure decrease may cause leaking of gases through compressive seals. There exists a need for an SOFC stack design that is able to handle the expansion and contraction due to the temperature change and maintain a constant pressure during SOFC operation.
A fuel cell stack that is in contact and below a top compression plate and in contact and above a bottom compression plate, wherein the top compression plate and the bottom compression plates are flat and rigid. A top compression device is above the top compression plate, wherein the top compression device applies a downward vertical force onto the top compression plate which applies a downward vertical force onto the fuel cell stack. An optional bottom compression device is below the bottom compression plate, wherein the bottom compression device applies an upward vertical force onto the bottom compression plate which applies an upward vertical force onto the fuel cell stack.
A fuel cell stack is in contact and below a top compression plate and in contact and above a bottom compression plate, wherein the top compression plate and the bottom compression plate are flat and rigid. In this fuel cell stack, a top compression rod is in contact and above the top compression plate, wherein the top compression rod applies a downward vertical force onto the top compression plate which applies a downward vertical force onto the fuel cell stack. Additionally, in this fuel cell stack, a bottom compression rod is in contact and below the bottom compression plate, wherein the bottom compression rod applies an upward vertical force onto the bottom compression plate which applies an upward vertical force onto the fuel cell stack. In this fuel cell stack there is also at least one alignment rod extending through at least one alignment hole in the top compression plate and extending through at least one alignment hole in the bottom compression plate, wherein the alignment rod does not apply any vertical compressive force onto the fuel cell stack. Additionally, in this fuel cell stack, the top compression plate and the bottom compression plate are enclosed within an insulated compartment and the top compression rod and the bottom compression rod extend outside the insulated compartment.
A fuel cell stack that is in contact and below a top compression plate and in contact and above a bottom compression plate, wherein the top compression plate and the bottom compression plate are flat and rigid. In this fuel cell stack a top compression cable is in contact and above the top compression plate, wherein the top compression cable applies a downward vertical force onto the top compression plate which applies a downward vertical force onto the fuel cell stack. Additionally, in this fuel cell stack a bottom compression cable is in contact and below the bottom compression plate, wherein the bottom compression cable applies an upward vertical force onto the bottom compression plate which applies an upward vertical force onto the fuel cell stack. In this fuel cell stack there is also at least one alignment rod extending through at least one alignment hole in the top compression plate and extending through at least one alignment hole in the bottom compression plate, wherein the alignment rod does not apply any vertical compressive force onto the fuel cell stack. Additionally, in this fuel cell stack, the fuel cell stack, top compression plate, bottom compression plate, part of the top compression cable and part of the bottom compression cable are enclosed inside an insulated compartment. Furthermore, the top compression cable and the bottom compression cable extend outside the insulated compartment and are connected to a pulley system, outside the insulated compartment, capable of pulling both the top compression cable and the bottom compression cable simultaneously.
A more complete understanding of the present invention and benefits thereof may be acquired by referring to the following description taken in conjunction with the accompanying drawings in which:
Turning now to the detailed description of the preferred arrangement or arrangements of the present invention, it should be understood that the inventive features and concepts may be manifested in other arrangements and that the scope of the invention is not limited to the embodiments described or illustrated. The scope of the invention is intended only to be limited by the scope of the claims that follow.
The following examples of certain embodiments of the invention are given. Each example is provided by way of explanation of the invention, one of many embodiments of the invention, and the following examples should not be read to limit, or define, the scope of the invention.
It is envisioned that this configuration will allow for constant pressure on the fuel cell stack despite dimensional changes in the stacking direction.
In one embodiment the top device is a top compression rod and the bottom device is a bottom compression rod. In an alternate embodiment, the top device is a top compression cable and the bottom device is a bottom compression cable.
As depicted in this embodiment of
One way to ensure proper alignment of the compression plate(s) with the SOFC stack is to have the alignment holes in a position wherein they are in contact with the fuel cell stack to prevent it from moving; this possibility is shown in
In one embodiment not shown, the SOFC stack design can be used with a top compression cable and a bottom compression rod. Alternatively, the SOFC stack design can be used with a top compression rod and a bottom compression cable.
When the SOFC stack design is used with a top compression cable as a top device and/or a bottom compression cable as a bottom device, the top compression cable and/or the bottom compression cable can be made of stainless steel. In some embodiments, there can be two, three, four or even more top compression cables and/or bottom compression cables. In some embodiments, the top compression cable can be connected to a top pulley system to increase tension on the top compression cable thereby imparting a downward vertical force onto the fuel cell stack. In other embodiments, the bottom compression cable can be connected to a bottom pulley system to increase tension on the bottom compression cable thereby imparting an upward vertical force onto the fuel cell stack. In yet another embodiment, both the top compression cable and the bottom compression cable can be connected to a singular pulley system capable of pulling both the top compression cable and the bottom compression cable simultaneously.
As shown in
In an alternate embodiment a novel SOFC stack compression method can be done with a top compression cable and/or bottom compression cable similarly to
In some embodiments it is envisioned that the amount of pressure needed to seal the fuel cell stack without destroying the fuel cell stack will range from about 2 psi to 1,500 psi. This pressure is the pressure measured on the fuel cell stack and individual stack components such as seals may have a higher effective pressure due to reduced areas for transmitting the pressure in the stacking direction. In other embodiments the pressure can range from about 80 psi to 1,000 psi, or 5 psi to 200 psi, or 2 psi to 15 psi.
In one embodiment, a top pressure distribution plate and an optional bottom pressure distribution plate are used to ensure even distribution of the pressure from the top compression rod and optional bottom compression rod. Minimizing the deflection of the compression plates by adding the pressure distribution plates more evenly exerts pressure on the SOFC stack between the top compression plate and the bottom compression plate. While it is envisioned that the top compression plate and the bottom compression plate can be made of material that is partially inert to the extreme pressures and temperatures within the insulation box these materials are often subject to deflection and creep. Materials that the top compression plate and the bottom compression plate can be made from include ceramics, titanium, Inconel alloys, stainless steels and other materials with softening temperatures greater than the SOFC stack operating temperature. In this embodiment a top pressure distribution plate and an optional bottom pressure distribution plate can be made from the same materials as the top compression plate and the bottom compression plate.
In one embodiment, the compression rods are made of the same materials as the top and bottom compression plates.
In another optional method, spacers can be placed between the top pressure distribution plate and the top compression plate as well as spacers being placed between the optional bottom pressure distribution plate and the bottom compression plate to aid in minimizing the deflection at the furthermost edges of the SOFC stack. The primary transmission of SOFC stack pressure occurs in the seals and the maximum deflection during compression is found at the furthermost edges of the SOFC stack.
In one embodiment, electrolyte materials for the SOFCs can be any conventionally known electrolyte materials. One example of electrolyte materials can include doped zirconia electrolyte materials, doped ceria materials or doped lanthanum gallate materials. Examples of dopants for the doped zirconia electrolyte materials can include: CaO, MgO, Y2O3, Sc2O3, Sm2O3 and Yb2O3. In one embodiment the electrolyte material is an yttria-stabilized zirconia, (ZrO2)0.92(Y2O3)0.08.
In one embodiment, anode materials for the SOFCs can be any conventionally known anode materials. Examples of the anode materials can include mixtures of NiO, yttria-stabilized zirconia, gadolinium doped ceria, CuO, CoO and FeO. In one embodiment the anode material is a mixture of 50 wt % NiO and 50 wt % yttria-stabilized zirconia.
In one embodiment, cathode materials for the SOFC can be any conventionally known cathode materials. One example of cathode materials can be perovskite-type oxides with the general formula ABO3, wherein A cations can be La, Sr, Ca, Pb, etc. and B cations can be Ti, Cr, Ni, Fe, Co, Zr, etc. Other examples of cathode materials can be mixtures of lanthanum strontium cobalt ferrite, lanthanum strontium manganite, yttria-stabilized zirconia or gadolinium doped ceria. Examples of the cathode materials include: Pr0.5Sr0.5FeO3-δ; Sr0.9Ce0.1Fe0.8Ni0.2O3-δ; Sr0.8Ce0.1Fe0.7Co0.3O3-δ; LaNi0.6Fe0.4O3-δ; Pr0.8Sr0.2Co0.2Fe0.8O3-δ; Pr0.7Sr0.3Co0.2Mn0.8O3-δ; Pr0.8Sr0.2FeO3-δ; Pr0.6Sr0.4Co0.8Fe0.2O3-δ; Pr0.4Sr0.6Co0.8Fe0.2O3-δ; Pr0.7Sr0.3Co0.9Cu0.1O3-δ; Ba0.5Sr0.5Co0.8Fe0.2O3-δ; Sm0.5Sr0.5CoO3-δ; and LaNi0.6Fe0.4O3-δ. In one embodiment the cathode material is a mixture of gadolinium-doped ceria (Ce0.9Gd0.1O2) and lanthanum strontium cobalt ferrite (La0.6Sr0.4Co0.2Fe0.8O3) or a mixture of gadolinium-doped ceria (Ce0.9Gd0.1O2) and samarium strontium cobaltite (Sm0.5Sr0.5CoO3).
In this example two different solid oxide fuel cell short stacks were created. Each SOFC stack comprised two fuel cells. Each fuel cell of both the first solid oxide fuel cell stack and the second solid oxide fuel cell stack had an anode comprising 50 wt. % Ni-50 wt. % (ZrO2)0.92(Y2O3)0.08, a cathode comprising 50 wt. % La0.6Sr0.4Co0.2Fe0.8O3-50 wt. % Ce0.9Gd0.1O2 and an electrolyte comprising (ZrO2)0.92(Y2O3)0.08. Both the first solid oxide fuel cell short stack and the second solid oxide fuel cell short stack were operated at 700° C. on hydrogen fuel with a current density of 200 mA/cm2. However, the first solid oxide fuel cell stack had a constant pressure of 30 psi exerted upon it while the second solid oxide fuel cell stack was held together using 6 steel bolts at the edges to achieve an effective pressure of 30 psi at ambient temperature. As shown in
In closing, it should be noted that the discussion of any reference is not an admission that it is prior art to the present invention, especially any reference that may have a publication date after the priority date of this application. At the same time, each and every claim below is hereby incorporated into this detailed description or specification as an additional embodiment of the present invention.
Although the systems and processes described herein have been described in detail, it should be understood that various changes, substitutions, and alterations can be made without departing from the spirit and scope of the invention as defined by the following claims. Those skilled in the art may be able to study the preferred embodiments and identify other ways to practice the invention that are not exactly as described herein. It is the intent of the inventors that variations and equivalents of the invention are within the scope of the claims while the description, abstract and drawings are not to be used to limit the scope of the invention. The invention is specifically intended to be as broad as the claims below and their equivalents.
This application is a non-provisional application which claims the benefit of and priority to U.S. Provisional Application Ser. No. 62/560,366 filed Sep. 19, 2017, entitled “Method for Compressing a Solid Oxide Fuel Cell Stack,” which is hereby incorporated by reference in its entirety.
Number | Date | Country | |
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62560366 | Sep 2017 | US |