Fuel cell stack

Abstract

Disclosed herein is a fuel cell stack with improved manufacturing performance. The fuel cell stack includes: a separator that comprises a diffusion part, as being provided with a diffusion channel, configured to distribute reaction gas and cooling water and a reaction part, as being continuously formed from the diffusion part and provided with a reaction channel that has a height greater than that of the diffusion channel, configured to move reaction gas distributed from the diffusion part and generate electrons by a chemical reaction; and a gas diffusion layer configured to contact the separator at the diffusion part and the reaction part.

Claims

1. A fuel cell stack, comprising: a separator that comprises: a diffusion part, as being provided with a diffusion channel, the diffusion part configured to distribute reaction gas and cooling water, and a reaction part, as being continuously formed from the diffusion part and inserted with a porous body having a plurality of channels provided therein, the reaction part configured to move reaction gas distributed from the diffusion part and generate electrons by a chemical reaction; and a gas diffusion layer configured to contact the diffusion part of the separator and the reaction part of the separator, wherein the porous body is inserted between only the reaction part of the separator and the gas diffusion layer, and wherein a height of the porous body is greater than a height of the diffusion part of the separator.

2. The fuel cell stack according to claim 1, wherein a compression rate where the diffusion part and the gas diffusion layer are contacted to each other is less than a compression rate where the reaction part and the gas diffusion layer are contacted to each other.

3. The fuel cell stack according to claim 1, wherein when the gas diffusion layer is compressed, a summed value of a height of the gas diffusion layer contacting the diffusion part and a height of the diffusion part and a summed value of the height of the gas diffusion layer contacting the reaction part and a height of the reaction part are equal to each other.

4. The fuel cell stack according to claim 1, wherein the diffusion channel has a height less than that of the porous body, and the diffusion channel has a width greater than that of the porous body.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) The above and other objects, features and advantages of the present disclosure will be more apparent from the following detailed description taken in conjunction with the accompanying drawings.

(2) FIG. 1 illustrates a cross-sectional view of an exemplary separator including a diffusion part and a reaction part, and a gas diffusion layer in an exemplary fuel cell stack according to an exemplary embodiment of the present invention; and

(3) FIG. 2 illustrates a cross-sectional view of an exemplary separator including a diffusion part and a reaction part, and a gas diffusion layer in an exemplary fuel cell stack according to an exemplary embodiment of the present invention.

DETAILED DESCRIPTION

(4) It is understood that the term “vehicle” or “vehicular” or other similar term as used herein is inclusive of motor vehicles in general such as passenger automobiles including sports utility vehicles (SUV), buses, trucks, various commercial vehicles, watercraft including a variety of boats and ships, aircraft, and the like, and includes hybrid vehicles, electric vehicles, plug-in hybrid electric vehicles, hydrogen-powered vehicles and other alternative fuel vehicles (e.g. fuels derived from resources other than petroleum). As referred to herein, a hybrid vehicle is a vehicle that has two or more sources of power, for example both gasoline-powered and electric-powered vehicles.

(5) The terminology used herein is for the purpose of describing particular exemplary embodiments only and is not intended to be limiting of the invention. As used herein, the singular forms “a”, “an” and “the” are intended to include the plural forms as well, unless the context clearly indicates otherwise. It will be further understood that the terms “comprises” and/or “comprising,” when used in this specification, specify the presence of stated features, integers, steps, operations, elements, and/or components, but do not preclude the presence or addition of one or more other features, integers, steps, operations, elements, components, and/or groups thereof. As used herein, the term “and/or” includes any and all combinations of one or more of the associated listed items.

(6) Unless specifically stated or obvious from context, as used herein, the term “about” is understood as within a range of normal tolerance in the art, for example within 2 standard deviations of the mean. “About” can be understood as within 10%, 9%, 8%, 7%, 6%, 5%, 4%, 3%, 2%, 1%, 0.5%, 0.1%, 0.05%, or 0.01% of the stated value. Unless otherwise clear from the context, all numerical values provided herein are modified by the term “about.”

(7) Hereinafter, various exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings. However, the present disclosure will be not limited or restricted to the exemplary embodiments below. Like reference numerals proposed in each drawing denote like components.

(8) FIG. 1 shows a cross-sectional view schematically of a diffusion part, a reaction part, and a gas diffusion layer in an exemplary fuel cell stack according to an exemplary embodiment of the present invention.

(9) As illustrated in FIG. 1, the fuel cell stack may include: a separator and a gas diffusion layer (GDL) 30. The separator may include a diffusion part 10, as being provided with a diffusion channel 11, configured to distribute reaction gas and cooling water and a reaction part 20, as being continuously formed from the diffusion part 10 and provided with a reaction channel 21 that has a height greater than that of the diffusion channel 11, configured to move the reaction gas distributed from the diffusion part 10 and generate electrons by a chemical reaction. The gas diffusion layer 30 may contact the diffusion part 10 and the reaction part 20 of the separator.

(10) As shown in FIG. 1, h.sub.C refers to a height of the diffusion channel 11 of the diffusion part 10. The height of the diffusion channel 11 (h.sub.C) may be equal to or greater than about 300 μm. Further, in FIG. 1, H refers to a total thickness of the separator and the gas diffusion layer 30. H.sub.C refers to a height of a reaction channel 21 in the reaction part 20. As shown in FIG. 1, in the gas diffusion layer, h.sub.G refers to a height of the gas diffusion layer 30 disposed at the diffusion part 10 side, and H.sub.G refers to a height of the gas diffusion layer 30 disposed at the reaction part 20 side.

(11) As used herein, G refers to a thickness before the gas diffusion layer 30 is compressed, and C refers to a compression rate of the gas diffusion layer 30. In particular, the compression rate C of the gas diffusion layer may ranges from about 0.05 to about 0.5. As such, the following Formulae 1-3 may be satisfied or provided in connection with h.sub.C, h.sub.G, H.sub.C, H.sub.G, H.sub.G, H, G and C, according to an exemplary embodiment of the present invention.
0.05≤C≤0.25  [1]
H.sub.G=(1−C)*G  [2]
H=H.sub.C+H.sub.G=h.sub.C+h.sub.G  [3]

(12) As shown in a cross section of the diffusion part 10 of FIG. 1, the diffusion part 10 may be formed to be wrinkled and may have a channel shape where the diffusion channel 11 is formed at the wrinkled portion.

(13) Further, when the gas diffusion layer 30 contacts the diffusion part 10, due to a structure of the diffusion part 10 having the channel shape, a compressed surface 13 to which the gas diffusion layer 30 and the diffusion part 10 are contacted and a non-compressed surface 15 to which the gas diffusion layer 30 and the diffusion part 10 are not contacted may be present.

(14) Since the reaction channel 21 of the reaction part 20 which is continuously formed to the diffusion part 10 is a moving path of generated electrons, a contact pressure between the reaction part 30 and the gas diffusion layer (GDL) 30 may be increased to make electricity efficiency good.

(15) Meanwhile, when the contact pressure between the reaction part 20 and the gas diffusion layer 30 is increased, the contact pressure between the diffusion part 10 which is continuously formed to the reaction part 20 and the gas diffusion layer 30 may also be increased.

(16) In this case, when the non-compressed surface 15 is greater than a predetermined range (e.g., a range of about 0 mm to 3 mm), a permeated amount of the gas diffusion layer 30 into the diffusion channel 11 may be increased and when the gas diffusion layer 30 is permeated into the diffusion channel 11, a differential pressure may be increased or water discharge performance may be reduced, and thus a function of the diffusion part 10 may be reduced. As a result, the non-compressed surface 15 may be prevented from being increased greater than the predetermined value.

(17) However, when the diffusion channel 11 is formed to be less than a predetermined range to prevent the non-compressed surface 15 from being increased, the diffusion part 10 may be hardly manufactured and thus the manufacturing performance may be degraded.

(18) Accordingly, the reaction channel 21 having a height greater than that of the diffusion channel 11 without changing a size of the diffusion channel 11 may be provided to provide a suitable compression rate at which the diffusion part 10 and the gas diffusion layer 30 adhere to each other less than a compression rate at which the reaction part 20 and the gas diffusion layer 30 adhere to each other. As consequence, the contact pressure may be reduced substantially or barely generated in the diffusion channel 11 while the contact pressure is sufficiently increased in the reaction channel 21.

(19) As ΔH refers to the height difference between the reaction part 20 and the diffusion part 10, the following Formula 4 which obtains a height difference between the reaction part 20 and the diffusion part 10 may be provided.
ΔH=H.sub.C−h.sub.C=h.sub.G−H.sub.G  [4]

(20) Further, as C.sub.P refers to the compression rate of the gas diffusion layer 30 at the diffusion part 10 side, the following Equation 5 may be satisfied.
3%≤C.sub.p≤13%  [5]

(21) In addition, when the gas diffusion layer 30 is compressed by staking the cells of the fuel cell or assembling the fuel cell stack, a summed value of the height of the gas diffusion layer 30 at the diffusion part side and the height of the diffusion part 10 and a summed value of the height of the gas diffusion layer 30 at the reaction part side and the height of the reaction part 20 may be equal to each other and thus an outer side of the gas diffusion layer 30 may be flat without being inclined or bent.

(22) As shown in FIG. 1, in the fuel cell stack according to an exemplary embodiment of the present invention, the diffusion channel 11 and the reaction channel 21 may be continuously formed.

(23) Meanwhile, the diffusion channel 11 may be formed to have a height less than that of the reaction channel 21 but has a width greater than that of the reaction channel 21 such that the diffusion channel may maintain the water discharge performance which is a function of the diffusion part 10.

(24) FIG. 2 shows a cross-sectional view schematically of an exemplary fuel cell stack according to another exemplary embodiment of the present invention.

(25) As illustrated in FIG. 2, the reaction channel may not be formed in the reaction part 20 so that the diffusion channel 11 and the reaction channel may be formed discontinuously to each other and a micro porous body 21d may be inserted between the reaction part 20 and the gas diffusion layer 30.

(26) In particular, the micro porous body 21d may be formed to have a height greater than that of the diffusion channel 11.

(27) Further, an inside of the micro porous body 21d may be finely provided with a plurality of channels and thus a function of the reaction channel may be performed by the micro porous body 21d. Accordingly, the reaction part 20 may not be provided with a separate channel other than the micro porous body 21d.

(28) As described in FIGS. 1 and 2, a boundary between the diffusion part 10 and the reaction part 20 is represented by a virtual dotted line d and thus the diffusion part 10 and the reaction part 20 are represented by an arrow, being divided based on the virtual dotted line d.

(29) As described above, according various exemplary embodiments of the present invention, the compressed amount of the gas diffusion layer at the diffusion part side may be minimized even though the contact pressure of the reaction part is increased in response to the reduction in the height of the diffusion channel, such that the manufacturing performance may be improved without increasing the differential pressure and reducing the water discharge performance.

(30) Although the fuel cell stack according to exemplary embodiments of the present invention has been described with reference to the accompanying drawings, the present disclosure is not limited to the above-mentioned exemplary embodiment and drawings but may be variously modified and changed within the following claims by those skilled in the art to which the present invention pertains.