Distribution structure for providing at least one reaction gas

Abstract

The invention relates to a distribution structure (10) for providing at least one reaction gas, in particular a gas mixture containing oxygen (O2), for a fuel cell (100) or an electrolyser, having a first structure element (11) and a second structure element (12), wherein the first structure element (11) and the second structure element (12) are designed and arranged with respect to one another such that: a distribution area (15) for the reaction gas is formed between the first structure element (11) and the second structure element (12); a plurality of feed channels (16) branch off from the distribution area (15) and are orientated substantially perpendicular to the distribution area (15); and a plurality of discharge channels (17) are formed below the second structure element (12) and are orientated parallel to the distribution area (15).

Claims

1. A distribution structure for supplying at least one reaction gas for a fuel cell or an electrolyzer, the distribution structure comprising a first structural element and a second structural element, wherein the first structural element and the second structural element are configured and arranged relative to one another in such a way that a distribution area for the reaction gas is formed between the first structural element and the second structural element, wherein a plurality of feed channels which are oriented essentially perpendicular to the distribution area are branched off from the distribution area, and wherein a plurality of discharge channels which are oriented parallel to the distribution area are formed underneath the second structural element, wherein the plurality of feed channels and the plurality of discharge channels are alternately arranged.

2. The distribution structure as claimed in claim 1, characterized in that the first structural element is configured in the form of a flat plate element.

3. The distribution structure as claimed in claim 1, characterized in that the second structural element is configured in the form of a plate element which is embossed and/or stamped and/or perforated at least in regions.

4. The distribution structure as claimed in claim 1, characterized in that at least one electrically conductive connecting element is provided between the first structural element and the second structural element.

5. The distribution structure as claimed in claim 1, characterized in that the second structural element has a dimpled and/or grooved structure in order to produce an alternating contact area to a gas diffusion layer at the bottom of the feed channels.

6. The distribution structure as claimed in claim 1, characterized in that the feed channels are formed on a first side of the second structural element which faces the first structural element, wherein the discharge channels are formed on a second side of the second structural element which is configured to face a gas diffusion layer.

7. The distribution structure as claimed in claim 1, further comprising at least one hole configured to have the reaction gas introduced therethrough essentially perpendicular to an extension plane of a gas diffusion layer into the gas diffusion layer, wherein the at least one hole is formed in the second structural element at the bottom of the feed channels.

8. The distribution structure as claimed in claim 1, characterized in that the feed channels have an increasing cross-sectional area in a direction of an introduction of reaction gas through the distribution area.

9. The distribution structure as claimed in claim 1, characterized in that, from one of the feed channels to an other of the feed channels, a number of holes which is variable or increases in a direction of an introduction of reaction gas through the distribution area is formed on the bottom of the feed channels.

10. A fuel cell comprising an anode space and a cathode space, and a distribution structure as claimed in claim 1 for supplying an oxygen-containing gas mixture to the cathode space.

11. An electrolyzer comprising an anode space and a cathode space, and a distribution structure as claimed in claim 1 for supplying an oxygen-containing gas mixture to the cathode space.

12. The distribution structure as claimed in claim 1, wherein the reaction gas is an oxygen-containing gas mixture.

13. The distribution structure as claimed in claim 1, characterized in that at least one electrically conductive, column-like connecting element is provided between the first structural element and the second structural element.

14. The distribution structure as claimed in claim 1, characterized in that, from one of the feed channels to an other of the feed channels, a plurality of holes which have different cross-sectional areas or cross-sectional areas which become larger in a direction of an introduction of reaction gas through the distribution area are formed on the bottom of the feed channels.

15. The distribution structure as claimed in claim 14, characterized in that, from the one of the feed channels to the other of the feed channels, a number of holes which is variable or increases in the direction of the introduction of the reaction gas through the distribution area is formed on the bottom of the feed channels.

16. The distribution structure as claimed in claim 2, wherein introduction of the at least one reaction gas defines a first direction, wherein the discharge channels are oriented in a second direction perpendicular to the first direction, and wherein the distribution area extends in the first direction and in the second direction and is parallel to the first structural element.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) The gas distribution structure of the invention and further developments and advantages thereof and the fuel cell or electrolyzer of the invention and further developments and advantages thereof will be illustrated in greater detail below with the aid of drawings. The drawings show, in each case schematically:

(2) FIG. 1 a schematic construction of a known bipolar plate as a gas distribution structure,

(3) FIG. 2 a schematic depiction of a gas distribution structure according to the invention,

(4) FIG. 3 a schematic depiction of a fuel cell or an electrolyzer having a gas distribution structure according to the invention, and

(5) FIG. 4 a schematic depiction of a gas distribution structure according to the invention as per a further working example.

DETAILED DESCRIPTION

(6) In the figures, features having the same reference symbols will generally be described only once.

(7) FIG. 1 shows a known distribution structure 10* in the form of a bipolar plate comprising two embossed metal sheets, for example for a fuel cell 100 or an electrolyzer. A channel structure for a cooling liquid, for example water H2O, is formed between the metal sheets. Above the metal sheets, a first reaction gas, for example an oxygen-containing reaction gas O2, or a second reaction gas, for example a fuel-containing reaction gas H2, is in each case fed to a corresponding adjoining gas diffusion layer GDL. However, in the case of a fuel cell 100 liquid product water H2O collects on the cathode side of the distribution structure 10* at the contact faces between the webs of the bipolar plate and the gas diffusion layer GDL, and this water blocks the pores within the gas diffusion layer GDL. As a result, the transport of oxygen to the catalyst layer is locally greatly inhibited, so that the performance of the fuel cell 100 breaks down locally with the consequence that the total performance of the fuel cell 100 is impaired.

(8) FIG. 2 shows a distribution structure 10 according to the invention for supplying at least one reaction gas, in particular an oxygen-containing gas mixture O2, for a fuel cell 100 or an electrolyzer, which distribution structure is configured with a first structural element 11 and a second structural element 12. According to the invention, the first structural element 11 and the second structural element 12 are configured and arranged relative to one another in such a way that a distribution area 15 for the reaction gas is formed between the first structural element 11 and the second structural element 12, that a plurality of feed channels 16 which are oriented essentially in a direction F2 perpendicular to the distribution area 15 and thus perpendicular to an active surface of the fuel cell 100 or the electrolyzer are branched off from the distribution area 15, and that a plurality of discharge channels 17 which are oriented parallel to the distribution area 15 are formed underneath the second structural element 12. The discharge channels 17 are also oriented in a direction F3 perpendicular to a direction F1 of the introduction of reaction gas through the distribution area 15.

(9) According to the invention, not only one structural element, as shown in FIG. 1, but two structural elements 11, 12 are now provided at least on a cathode side of the distribution structure 10*, as shown in FIG. 2. The reaction gas, preferably oxygen-containing reaction gas O2, is conveyed between the structural elements 11, 12. Between the lower or second structural element 12 and a gas diffusion layer GDL, the discharge channels 17 for transporting away an exhaust gas with product water H2O are formed underneath the second structural element 12. The feed channels 16 and the discharge channels 17 are fluidically separated from one another.

(10) As can clearly be seen from FIG. 3, the reaction gas is distributed by the distribution area 15 which can be arranged parallel to the plane of extension of the fuel cell 100 and is provided with a plurality of feed channels 16 branching off from the distribution area 15. The distribution area 15 and the feed channels 16 are formed between two structural elements 11, 12 according to the invention, for example made of metallic sheets. The reaction gas can in this way be distributed uniformly and with a low pressure drop over the total active surface of the fuel cell 100 or the electrolyzer.

(11) As is indicated in FIG. 2, column-like or line-like connecting elements 13 for electrical contact and mechanical stability can be provided between the structural elements 11, 12 without inhibiting the free flow of the reaction gas through the distribution area 15.

(12) The feed channels 16 can, for example, be embossed in the form of grooves or dimples having different, e.g. rectangular or circular, cross-sectional areas in the second structural element 12. The reaction gas is supplied essentially perpendicular to the active surface of the fuel cell 100 or the electrolyzer through the feed channels 16.

(13) One or more holes 14 through which the reaction gas can escape into the gas diffusion layer GDL are formed on the underside of the feed channels 16. A membrane M through which hydrogen ions are transported adjoins the gas diffusion layer GDL.

(14) Between the depressions for the feed channels 16 underneath the second structural element 12 or between the gas diffusion layer GDL and the second structural element 12, the product gas (electrolyzer) or the product water H2O together with excess gas mixture (fuel cell 100) is discharged parallel to the distribution area 15 or parallel to the plane of extension of the gas diffusion layer GDL from the fuel cell 100 or from the electrolyzer.

(15) Consequently, two separate channel structures for the reaction water H2O (electrolyzer) or the reaction gas (fuel cell 100) and for the product gas (electrolyzer) or the product water H2O together with excess gas mixture (fuel cell 100) are formed by two structural elements 11, 12, so that the starting materials and the products of a corresponding electrochemical reaction are hydrodynamically separated from one another. A second distribution structure, essentially of any form, for example as embossed metal plate, for the second reaction gas, for example the fuel-containing reaction gas H2, can be realized from the other side of the fuel cell 100 or the electrolyzer. Furthermore, a channel structure for a cooling liquid, for example water H2O, can be provided between the first structural element 11 of the distribution structure 10 according to the invention for the first (for example oxygen-containing) reaction gas and the second distribution structure for the second (for example fuel-containing) reaction gas.

(16) The reaction gas fed in is advantageously distributed uniformly over the total active surface of the fuel cell 100 or the electrolyzer by means of the distribution area 15, preferably with a low pressure drop. Branching off therefrom, the active surface is supplied point-by-point with fresh gas (reaction gas). In contrast to known one-piece bipolar plates as shown in FIG. 1, the gas concentration does not decrease from inlet to outlet but instead the entire active surface is supplied point-by-point with fresh gas. A uniform fresh gas supply through all feed channels 16 is achieved by the pressure drop within the distribution area 15 being significantly smaller than the pressure drop through the feed channels 16. Secondly, the total pressure drop in the distribution structure 10 according to the invention from inlet to outlet is small since only a small part of the total gas introduced flows through each feed channel 16.

(17) Accumulation of liquid water under the depressions of the second structural element 12 is reliably prevented by the distribution structure 10 according to the invention since the reaction gas flows directly through the contact areas 12a between the distribution structure 10 and the gas diffusion layer GDL. The liquid water is thus reliably transported away and the depressions of the second structural element 12 are not flooded with liquid water.

(18) A further advantage is the introduction of gas perpendicular to the active surface, as a result of which convective gas transport into the gas diffusion layer GDL can be realized. In the case of bipolar plates as shown in FIG. 1, the reaction gas O2, H2 flows parallel to the active surface and the transport of gas to the catalyst layer occurs purely by diffusion. Convective gas transport as per the invention can advantageously be effected uniformly and in a controlled manner over the entire active surface.

(19) It is conceivable in the context of the invention for a fan or suction fan to be provided in order to draw off the exhaust gas underneath the second structural element 12 or between the second structural element 12 and the gas diffusion layer GDL and thus assist the flow of the exhaust gas through the discharge channels 17.

(20) As FIGS. 1 and 2 show, the first structural element 11 can be configured in the form of a flat plate element. The second structural element 12 can be configured in the form of a plate element which is embossed and/or stamped and/or perforated at least in regions. Such structural elements 11, 12 are simple and inexpensive components. Cheap and simple production of the distribution structure 10 is thus provided.

(21) The feed channels 16 are formed on a first side 12.1 of the second structural element 12 which faces the first structural element 11, with discharge channels 17 being formed on a second side 12.2 of the second structural element 12 which can face the gas diffusion layer GDL. A separate exhaust gas conduit in addition to a cathode conduit through the distribution area 15 according to the invention can be provided for the discharge channels 17. In addition, it is conceivable for a fan, for example in the form of a suction fan, to be provided at the outlet of the separate exhaust gas conduit.

(22) At least one hole 14, preferably a plurality of holes 14, through which the reaction gas can be introduced essentially perpendicular to the plane of extension of the gas diffusion layer GDL into the gas diffusion layer GDL is/are formed in the second structural element 12 at the bottom 16a of the feed channels 16. A Venturi effect in the direction perpendicular to the active surface on passage through the holes 14 in addition to the convective introduction of the reaction gas through the feed channels 16 can thus also be exploited in order to equalize and assist the distribution of the reaction gas.

(23) As FIG. 4 shows, either the holes 14 or the feed channels 16 themselves can have an increasing cross-sectional area in the direction F1 of the introduction of reaction gas in order to make a uniform introduction of the reaction gas into the gas diffusion layer GDL through the distribution area 15 possible despite a possible pressure drop from inlet to outlet. In addition, it is conceivable for a number of holes 14 which increases in the direction F1 of the introduction of reaction gas through the distribution area 15 to be formed, from feed channel 16 to feed channel 16, at the bottom 16a of the feed channels 16.

(24) As is also indicated in FIG. 3, a fuel cell 100 or an electrolyzer which has an anode space A and a cathode space K and is configured with an appropriate distribution structure 10 for supplying the oxygen-containing gas mixture O2 to the cathode space K is provided by the invention.

(25) The above description of FIGS. 1 to 4 describes the present invention exclusively by way of examples. It is of course possible to combine individual features of the embodiments, insofar as it is technically useful, freely with one another without going outside the scope of the invention.