Fuel cell

Abstract

A flattened tube double-sided power generation type fuel cell is comprised of the combination of one or more of the following means (1) and (2). That is, means (1) for optimizing the constitution of an current-collecting electrode thereby making the flow of fuel or air uniform over the entire region, andmeans (2) for dividing the current-collecting electrode into two regions thereby shunting the flow of the fuel into a flow directing to the anode of the cell and a flow directly directing to the downstream, for increasing the power generation amount in the cell, the means being applicable also to a cell of a cylindrical shape.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a schematic view of a flattened tube double-sided power generation type cell;

FIG. 2 is a view showing a cross section of the fuel cell of an embodiment according to the invention;

FIG. 3 is a view showing a longitudinal cross section of the fuel cell of the embodiment according to the invention;

FIG. 4 is a cross sectional view showing a current path in FIG. 1 of the embodiment of the invention;

FIG. 5 is a schematic view of an example according to the invention;

FIG. 6 is a cross sectional view showing a modified example of the invention;

FIG. 7 is a cross sectional view showing a modified example of the invention;

FIG. 8 is a cross sectional view showing a modified example of the invention;

FIG. 9 is a longitudinal sectional view showing a modified example of the invention;

FIG. 10 is a longitudinal sectional view showing a modified example of the invention; and

FIG. 11 is a cross sectional view showing a modified example of the invention.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

In an embodiment according to the invention, a combination of the following means (1) and (2) is proposed. That is, a flattened tubular type fuel cell comprises:

means (1) for optimizing the constitution of an current-collecting electrode thereby making the flow distribution of a fuel or air uniform across the entire cell region, andmeans (2) for shunting the flow of the fuel into a flow directing toward the anode of the cell and a flow directly directing toward the downstream of the current-collecting electrode. Further, such a structure is applicable also to a cell of a cylindrical shape.

FIG. 1 shows a schematic view of a flattened tube double-sided power generation type cell. A cell 5 comprises a solid electrolyte 1, an anode 2 (fuel electrode) formed on an outer surface of the solid electrolyte 1, a cathode 3 (air electrode) formed on an inner surface of the solid electrolyte 1, and an interconnector 4 for taking out a current from the cathode 3. A current-collecting electrode 6 is provided around the cell 5.

A current of the cell 5 flows from the anode 2 to the cathode 3 by way of the solid electrolyte 1. Further, it flows from the cathode 3 to the interconnector 4 for taking out the current. Since most of the current of the anode 2 flows in the circumferential direction, the current path is increased. In order to prevent the increased current path from becoming a large resistor factor, the current-collecting electrode 6 serves to increase a cross-sectional area of the current path in an auxiliary manner. Incidentally also in the cathode, a current path in the circumferential direction is present although it is not so larger in the anode 2. An air-feeding hole 7 is formed inside of the cathode 3 to feed air as an oxidizing agent, and thereby air region through which air flows is formed. On the other hand, the fuel flows along an outer circumference of the cell 5 to form a fuel region.

While the description for FIG. 1 shows a case of a cell in which the anode is formed on the outer side of the flattened tube type, a similar phenomenon as to the current path occurs also even in the case of a cell where the cathode is formed on the outside of the flattened tube type. The following description is to be made to a case where the anode is formed on the outside of the cell, and it is specified to an anode of the flattened tube double-sided power generation type cell.

In the fuel cell of the present invention, the flow of the fuel in the current-collecting electrode of the flattened tube cell is shunted into a flow toward the cell and a flow directly flowing to the downstream of the fuel (in the direction of exit). In addition, the thickness of the anode electrode is decreased to provide the current-collecting electrode with a role of the anode electrode to thereby increase the power generation amount of the cell.

FIG. 2 shows a cross sectional view of a flattened tube double-sided power generation type cell as an example of the present invention. An anode (fuel electrode) 2 is formed on the outer surface of the solid electrolyte 1, and a cathode (air electrode) 3 is formed on the inner surface of the same 1, and interconnectors 4 for taking out the current of the cathode are disposed at two positions in the outer surface of the cell. The anode 2 is disposed between the interconnectors 4 provided at two positions in the same manner as portions in the cell.

The solid electrolyte 1 is in a flattened tubular shape with a bottom, and its material is yttrium stabilized zirconia (YSZ). The anode 2 is made of a porous cermet (sintered body of a metal ceramic) comprising nickel and YSZ. The cathode 3 is made of lanthanummanganate. The interconnectors 4 are made of a lanthanum chlomide. The fuel flows through the outside of the cell. The oxidizing agent (air) flows through air feeding holes 7 at three positions inside the cathode.

The current-collecting electrode 6 is filled in a fuel region 8 on the outside of the cell through which the fuel flows. The current-collecting electrode 6 is comprised of an inner current-collecting electrode 9 adjacent to the anode and an outer current-collecting electrode 10 placed outside the inner current-collecting electrode 9.

FIG. 3 shows a portion of a longitudinal cross section of the flattened tube double-sided power generation type cell as an embodiment of the invention. FIG. 3 shows the state of a flow of the fuel 19. The size of arrows schematically shows the level of the flow rate. That is, the flow rate is comparatively higher in the outer current-collecting electrode 10 and the flow rate is comparatively lower in the inner current-collecting electrode 9. The fuel 19 in the outer current-collecting electrode 10 does not have cell reaction in the lower portion and flows to the upper portion of the cell at the downstream. That is, the fuel not having the cell reaction (not used fuel) can be fed as far as the upper portion of the cell (downstream) and the cell reaction occurs uniformly over the entire surface of the cell 5.

The outer current-collecting electrode 10 mainly constitutes a flow path for feeding the fuel in the axial direction of the cell. Further, the outer current-collecting electrode 10 also functions as a current path. Accordingly, the conditions required for the outer current-collecting electrode 10 are preferably as follows. That is,

(1) the fuel gas can flow more easily compared with that in the inner current-collecting electrode 9 (with low flow resistance); and(2) the electro-conductivity is high.

The inner current-collecting electrode 9 mainly has a role of transporting the fuel fed to the outer current-collecting electrode 10 into the anode 2. Further, the inner current-collecting electrode 9 functions also as a current path. Accordingly, the conditions required for the inner current-collecting electrode 9 are preferably as follows. That is,

(1) the fuel gas is fed from the outer current-collecting electrode 10 and(2) the electro-conductivity is high.

For the inner current-collecting electrode 9 and the outer current-collecting electrode 10, a porous member having through pores, for example, a three-dimensional mesh porous member can be used. The gas flow rate V in the porous member can be represented by the following equation.

V=ε ₀ ³ D ² ΔP/{80μ(1−ε₀)²}l  (1)

in the equation, ε₀ represents a porosity, D represents a diameter of strand constituting the porous member, l represents the length of a porous layer, ΔP represents a differential pressure between the upstream and the downstream of the porous layer, and μ represents the viscosity of a flood. Accordingly, the flow rate increases more as the porosity is larger and the strand diameter constituting the porous member is larger assuming that the differential pressure on the porous layer with a length of l is identical. Naturally, the flow resistance increases more as the porosity is smaller and the wire diameter is smaller.

It is preferable that the gas flows more easily in the outer current-collecting electrode 10 compared with the inner current-collecting electrode 9 and it is preferable to flow at a fast flow rate. The outer current-collecting electrode 10 used in this case had a porosity of about 95% and the strand diameter of about 10 μm. On the other hand, for the inner current-collecting electrode 9, those having a porosity of about 90% and a strand diameter of about 10 μm was used. This can make the flow rate in the outer current-collecting electrode 10 higher by about one digit compared with the flow rate in the inner current-collecting electrode 9. Naturally, it is not necessary to provide a difference between the flow rate in the outer current-collecting electrode 10 and the flow rate in the inner current-collecting electrode 9 by so much as described above, and it may suffice that the difference of the flow rate may be at least about from 1.2 to 1.5.

As a material for the inner current-collecting electrode 9 and the outer current-collecting electrode 10, it is preferable that the electroconductivity is high as shown by the required condition (2) above. Then, a nickel material was used both for the inner current-collecting electrode 9 and the outer current-collecting electrode 10. Nickel was used as a three-dimensional mesh porous member. It may also be a stainless steel, nickel-based alloy, etc.

Further, for the outer current-collecting electrode 10 having a main purpose of flowing the gas, a ceramic material may also be used not being restricted to metal materials. Naturally, in a case of using a highly conductive material for the outer current-collecting electrode 10, the current path is enlarged, thereby contributing to the lowering of the internal resistance.

The cell reaction is shown here. At first, a method of reforming a hydrocarbon type fuel to form a reformed gas containing hydrogen is to be described in the case of methane as example of the hydrocarbon type fuel. On the reforming catalyst, methane and steams are reacted (reforming reaction) to generate hydrogen mainly according to the reaction of the following formula (1). As the reforming catalyst, catalysts such as Ni and Ru systems are used generally.

CH₄+H₂O=CO+3H₂  (1)

Simultaneously, CO reacted according to the chemical formula (1) is further converted into hydrogen as a fuel by the reaction with H₂O represented by the following formula (2) (CO conversion reaction).

CO+H₂O=CO₂+H₂  (2)

Since the reaction of forming hydrogen from a hydrocarbon type fuel is an endothermic reaction, heat has to be supplied for keeping the reaction and, generally, the reforming catalyst has to be kept at about 600 to 800° C.

The cell reaction (power generating reaction) occurs at the anode 2, which is an exothermic reaction represented by the following formulae (3) and (4):

H₂+½O₂=H₂O  (3)

CO+½O₂=CO₂  (4)

A current in the cell of this embodiment is schematically shown in FIG. 4. The current path is indicated by arrows 11. The current of the cell passes from the outer current-collecting electrode 10 to the inner current-collecting electrode 9, flows by way of an anode 2 and a solid electrolyte 1 into a cathode 3 and, further, flows from the cathode 3 to interconnectors 4 and is then taken out to the outside. Further, the current from the outer current-collecting electrode 14 and the inner current-collecting electrode 13 disposed between the two interconnectors, and from the anode 12 also flows through the similar path to the inter connectors 4 and is then taken out to the outside. Further, the anode 2 and the outer current-collecting electrode 14 are electrically connected at the respective adjacent cells as shown in FIG. 5.

In this embodiment, the interconnector 4 is circumferentially divided at two positions and also divided longitudinally at two positions but it may be divided at three or more portions with no problem.

FIG. 6 shows a modified example of this embodiment. A ceramic porous member that can be insulated electrically is used as the outer current-collecting electrode 15 in FIG. 1. In a case of using the ceramic porous member that can be insulated electrically for the outer current-collecting electrode 15, since electrical connection with the anode of an adjacent cell can be avoided upon serial connection of the cells, this is extremely effective in a case of connecting a plurality of cells in series or parallel.

FIG. 7 shows a modified example of this embodiment. A metal mesh or ceramic mesh that can be insulated electrically is used as the outer current-collecting electrode 17 of FIG. 1. A same metal mesh was used also for the inner current-collecting electrode 16.

For the mesh size, a coarse mesh of about #30 was used for the outer current-collecting electrode 17 and a fine mesh of about #100 was used for the inner current-collecting electrode 16.

FIG. 8 shows a modified example of the invention. The outer current-collecting electrode in FIG. 1 was removed to provide a fuel feed area 18. While the flow resistance is decreased but the electric resistance increases compared with FIG. 1.

FIG. 9 shows a modified example of the invention. The illustrated example has fuel-feeding holes 21 and anode-side fuel-feeding holes 22 as the fuel gas flow channels in the outer current-collecting electrode 10 and the inner current-collecting electrode 9. The fuel-feeding holes 21 serve to flow the fuel gas mainly in the axial direction of the cell, while the anode-side fuel-feeding holes 22 serves to flow the fuel gas in the radial direction of the cell. Provision of the flow channels enables to feed the unused fuel furthermore to the downstream by which the fuel is fed to the entire surface of the cell 5 making the cell reaction uniform. FIG. 11 shows a cross sectional view of this embodiment.

FIG. 10 shows a modified example of this embodiment. In the illustrated example, fuel-feeding holes 21 and anode-side fuel-feeding holes 22 as gas flow channels are disposed in the inner current-collecting electrode 9. The fuel-feeding holes 21 serve to flow the fuel gas mainly in the axial direction of the cell, while the anode-side fuel-feeding holes 22 serve to flow the fuel gas in the radial direction of the cell. Provision of the flow channels enables to feed the unused fuel further to the downstream and the fuel is fed to the entire surface of the cell 5 to make the cell reaction uniform. Since such fuel gas feeding channels can be also used for the axial feeding of the fuel gas, the outer current-collecting electrode 10 was removed. This can reduce the internal resistance.

While the embodiment has been described with reference to a cell structure in which the outside of the flattened tube double-sided power generation type cell is provided the anode, the present invention can provide the same effect also in the cell structure in which the outside of the flattened tube double-sided power generation type cell is provided with the cathode.

While the embodiment has been described with reference to the examples in which the tubular shape with a bottom for the fuel cell is adapted for the flattened tube shape, the effect is not impaired at all also in an flattened tube with bottomless.

Further, since the cell shape is not restricted to the flattened tubular shape but the invention is applicable also to a cell of an oval shape in cross section or a cell of a cuboidal, rectangular or cylindrical shape with similar effect, the shape is not restricted to the flattened tubular shape.

In the fuel cell of this embodiment, since substantially the entire region of the flattened tubular cell contributes to the cell reaction and the area of power generation can be increased to increase the amount of power generation and the internal resistance can be decreased, the energy efficiency can be improved. In this case, the cell performance can further be improved by providing the current-collecting electrode not only to the anode but also to the cathode.

Claims

1. A fuel cell of a flattened tubular shape, a cuboidal shape, or a cylindrical shape comprising an anode and a cathode on both sides of an electrolyte, wherein a fuel feeding channel for feeding a fuel at a uniform concentration to the entire region of a cell is disposed in a current-collecting electrode.

2. A fuel cell according to claim 1, wherein the current-collecting electrode on the fuel cell is divided into two or more layers and the flow is shunted into a flow directing to a cell exit and a flow directing to a cell.

3. A fuel cell according to claim 1, wherein the current-collecting electrode on the fuel cell is divided into two or more layers, andwherein the flow resistance of an current-collecting electrode adjacent to the cell is made larger and the flow resistance of the other current-collecting electrode is made smaller, comparatively.

4. A fuel cell according to claim 1, wherein the current-collecting electrode on the fuel cell is divided into two or more layers, andwherein the flow rate in the current-collecting electrode adjacent to the cell is restricted to not be greater than the flow rate in other current-collecting electrode.

5. A fuel cell according to claim 1, wherein the current-collecting electrode on the fuel cell is divided into two or more layers, andwherein the divided current-collecting electrode are made of porous, mesh or wick members having through pores of mutually different porosities.

6. A fuel cell according to claim 1, wherein the current-collecting electrode for the anode is made of a porous member containing nickel.

7. A fuel cell according to claim 1, wherein the outer part of the current-collecting electrode is made of a ceramic porous member.

8. A fuel cell according to claim 1, wherein the current-collecting electrode for the cathode is made of a porous member containing chromium.

9. Fuel cells connected to each other in series or in parallel, wherein each of them is configured by the fuel cell according to anyone of claims 1-7.

10. A fuel cell according to claim 1, wherein the current-collecting electrode on the fuel cell is divided into two or more layers, andwherein the flow rate in the current-collecting electrode adjacent to the cell is restricted to about 0.8 times or less of the flow rate in other current-collecting electrode.

11. A fuel cell comprising: an electrolyte having ionic permeability;a first electrode and a second electrode placed on both sides of the electrolyte, respectively;a fluid flow channel region which is provided adjacent to the first electrode and that flows a fuel fluid therein to generate electrochemical reaction at the first electrode or the second electrode,a first region which is configured by a part of the fluid channel region and that is capable of passing the fluid through and has electrical conductivity, anda second region which is configured by a remaining part of the fluid channel region other than the first region and that is capable of moving the fluid to the first region,wherein the moving resistance of the fluid in the first region is larger than that in the second region.

12. A fuel cell comprising: an anode for oxidizing a fuel;a cathode for reducing an oxidizing agent;an ion permeable electrolyte formed between the anode and the cathode;a first region having a porous electroconductive member adjacent to the anode, anda second region layered on the first region and having a porosity larger than that of the first region.

13. A fuel cell comprising: an anode for oxidizing a fuel;a cathode for reducing an oxidizing agent;an ion permeable electrolyte formed between the anode and the cathode; anda fuel flow channel adjacent to the anode;wherein the fuel flow channel comprises a fuel feeding layer made of a porous electroconductive member and a fuel transport region being layered on the fuel feeding layer and having larger porosity and volume than the fuel feeding layer.