Patent Application
20060201800
1. Field of the Invention
The present invention relates to an electrolysis apparatus having a porous electrical conductor for use as an electrolysis power feeding element, an electrochemical reaction membrane apparatus having a porous electrical conductor provided at least on one surface of a membrane used in an electrochemical reaction, and the porous electrical conductor used in these apparatuses. Further, the present invention relates to a method of producing the porous electrical conductor.
2. Description of the Related Art
In recent years, systems for supplying electrical power using hydrogen as a fuel have been proposed. For example, a polymer electrolyte fuel cell is known. The polymer electrolyte fuel cell includes a membrane electrode assembly and separators sandwiching the membrane electrode assembly. The membrane electrode assembly includes an anode, a cathode, and a solid polymer electrolyte membrane (ion exchange membrane) interposed between the anode and the cathode. Each of the anode and the cathode has an electrode catalyst layer and a gas diffusion layer.
In the fuel cell, a fuel gas such as a gas chiefly containing hydrogen (hereinafter also referred to as the “hydrogen-containing gas”) is supplied to the anode. A gas chiefly containing oxygen or the air (hereinafter also referred to as the “oxygen-containing gas”) is supplied to the cathode. The catalyst of the anode induces a chemical reaction of the fuel gas to split the hydrogen molecule into hydrogen ions and electrons. The hydrogen ions move toward the cathode through the electrolyte membrane, and the electrons flow through an external circuit to the cathode, creating DC electrical energy.
In general, a water electrolysis apparatus is adopted for producing hydrogen as a fuel. The water electrolysis apparatus uses a solid polymer electrolyte membrane for decomposing water to produce hydrogen (and oxygen). Electrode catalyst layers are provided on both surfaces of the solid polymer electrolyte membrane to form a membrane electrode assembly. Power feeding elements are provided on both surfaces of the membrane electrode assembly to form a unit of the water electrolysis apparatus. That is, the unit of the water electrolysis apparatus substantially has the same structure as the fuel cell.
After a plurality of units are stacked together, the voltage is applied to the opposite ends in the stacking direction. Water is supplied to the anode side power feeding element. Therefore, the water is decomposed into hydrogen ions (protons) at the anode of the membrane electrode assembly. The hydrogen ions pass through the solid polymer electrolyte membrane toward the cathode. The hydrogen ions combine with electrons to produce hydrogen. Further, at the anode, oxygen is produced together with the hydrogen ion. The oxygen and the redundant water are discharged from the unit.
For example, the power feeding element is made of a porous electrical conductive plate as disclosed in Japanese Laid-Open Patent Publication No. 2004-71456. In the conventional technique, as shown in
In the conventional technique, for example, as shown in
Thus, water supply becomes difficult. The water electrolysis is not performed desirably, and the moisture of the solid polymer electrolyte membrane is not maintained. The membrane resistance is increased, and the electrolysis voltage becomes high.
A main object of the present invention is to provide an electrolysis apparatus, an electrochemical reaction membrane apparatus, a porous electrical conductor, and a production method thereof which make it possible to smoothen the surface of the porous electrical conductor, and increase the porosity in the surface of the porous electrical conductor.
According to the present invention, an electrolysis apparatus comprises a porous electrical conductor for use as an electrolysis power feeding element. The porous electrical conductor is subjected to a grinding process, and then, subjected to an etching process to have a smooth surface.
Further, according to the present invention, an electrochemical reaction membrane apparatus comprises a porous electrical conductor provided at least on one surface of a membrane used in an electrochemical reaction. The porous electrical conductor is subjected to a grinding process, and then, subjected to an etching process to have a smooth surface.
Further, according to the present invention, a porous electrical conductor is used as a power feeding element of an electrolysis apparatus, and also used in an electrochemical reaction membrane apparatus. The porous electrical conductor is subjected to a grinding process, and then, subjected to an etching process to have a smooth surface.
Further, it is preferable that the porous electrical conductor is used as a water electrolysis power feeding element, and the smooth surface faces a membrane. In the structure, for example, it is possible to produce hydrogen efficiently by water electrolysis, and it is possible to suitably use the hydrogen as a fuel.
Further, it is preferable that the porous electrical conductor is a sintered body of spherical titanium particles. The formability of the material is excellent. In the structure, it is possible to form the smooth surface of the porous electrical conductor easily.
Further, it is preferable that the sintered body of spherical titanium particles has a porosity in the range of 10% to 50%. If the porosity is less than 10%, the fluid does not flow sufficiently, and if the porosity is more than 50%, the porous electrical conductor does not contact the membrane suitably.
In the present invention, after the surface of the porous electrical conductor is smoothened by the grinding process, it is possible to easily, and reliably eliminate deformation in the surface of the porous electrical conductor by the etching process. Thus, the surface of the porous electrical conductor is smoothened, and the porosity in the surface is increased desirably. Consequently, for example, the oxygen produced at the anode is discharged smoothly through the porous electrical conductor. Thus, the amount of the supplied water becomes sufficient, and the shortage of water supply does not occur.
Further, it is possible to achieve the desired porosity in the surface of the porous electrical conductor by the etching process. Therefore, it is possible to reduce the pressure loss, and reduce the pressure of the supplied water. Accordingly, the electrical power needed for the pump for supplying the water is reduced, and the energy efficiency in the system is improved.
The above and other objects, features and advantages of the present invention will become more apparent from the following description when taken in conjunction with the accompanying drawings in which preferred embodiments of the present invention are shown by way of illustrative example.
The water electrolysis apparatus 10 includes a stack body 14 formed by stacking a plurality of unit cells 12 in a horizontal direction indicated by an arrow A. At one end of the stack body 14 in the stacking direction, a terminal plate 16a is provided. An insulating plate 18a is provided outside the terminal plate 16a. Further, an end plate 20a is provided outside the insulating plate 18a. Likewise, at the other end of the stack body 14 in the stacking direction, a terminal plate 16b is provided. An insulating plate 18b is provided outside the terminal plate 16b. Further, an end plate 20b is provided outside the insulating plate 18b.
For example, components of the water electrolysis apparatus 10 between the end plates 20a, 20b are tightened together by a plurality of tie rods 22 extending in the direction indicated by the arrow A. Alternatively, the water electrolysis apparatus 10 may be placed in a box-shaped casing (not shown) including the rectangular end plates 20a, 20b.
As shown in
As shown in
The membrane electrode assembly 32 includes an anode side power feeding element (porous electrical conductor) 40, a cathode side power feeding element (porous electrical conductor) 42, and a solid polymer electrolyte membrane (electrolyte) 38 interposed between the anode side power feeding element 40 and the cathode side power feeding element 42. The anode side power feeding element 40 and the cathode side power feeding element 42 support the solid polymer electrolyte membrane 38. The solid polymer electrolyte membrane 38 is formed by impregnating a thin membrane of perfluorosulfonic acid with water, for example. An anode catalyst layer 44a and a cathode catalyst layer 44b are formed on both surfaces of the solid polymer electrolyte membrane 38. For example, an Ru (ruthenium) based catalyst is used for the anode catalyst layer 44a, and a platinum catalyst is used for the cathode catalyst layer 44b.
As described later, each of the anode side power feeding element 40 and the cathode side power feeding element 42 comprises a sintered body of spherical gas atomized titanium powder. The anode side power feeding element 40 and the cathode side power feeding element 42 have smooth surfaces 40a, 42a, which have been subjected to an etching process after a grinding process. The porosity of the anode side power feeding element 40 and the cathode side power feeding element 42 is preferably in the range of 10% to 50%, and more preferably in the range of 20% to 40%.
At one end of the unit cell 12 in a horizontal direction indicated by an arrow B in
As shown in
As shown in
A seal member 56a is formed integrally with the anode side separator 34, around the outer end of the anode side separator 34, and a seal member 56b is formed integrally with the cathode side separator 36, around the outer end of the cathode side separator 36. For example, the seal members 56a, 56b are made of seal material, cushion material or packing material such as EPDM (Ethylene Propylene diene terpolymer), NBR (Nitrile Butadiene Rubber), fluoro rubber, silicone rubber, fluoro silicone rubber, butyl rubber (Isobutene-Isoprene Rubber), natural rubber, styrene rubber, chloroprene rubber, or acrylic rubber.
As shown in
Next, operation of producing the anode side power feeding element 40 of the membrane electrode assembly 32 will be described. The cathode side power feeding element 42 is produced in the same manner as the anode side power feeding element 40, and detailed description thereof will be omitted. Further, it should be noted that the cathode side power feeding element 42 is provided as necessary. That is, only the anode side power feeding element 40 may be provided.
As in the case of Japanese Laid-Open Patent Publication No. 2004-71456, as shown in
Then, a surface of the sintered body 62 of titanium powder facing the solid polymer electrolyte membrane 38 is subjected to a grinding process to form a ground surface 64 (see
Thus, as shown in
Next, operation of the water electrolysis apparatus 10 will be described below.
As shown in
Thus, the water is decomposed by electricity in the anode catalyst layer 44a to produce hydrogen ions, electrons, and oxygen. That is, the following anodic reaction is induced.
H2O→2H++2e−+1/2O2 (anodic reaction)
The hydrogen ions produced in the anodic reaction pass through the solid polymer electrolyte membrane 38 toward the cathode catalyst layer 44b, and combine with electrons to produce hydrogen. That is, the following cathodic reaction is induced.
2H++2e31→H2 (cathodic reaction)
Thus, the hydrogen flows along the second flow field 54 formed between the cathode side separator 36 and the cathode side power feeding element 42. The hydrogen flows through the hydrogen flow passage 50 to the outside of the water electrolysis apparatus 10. The oxygen produced in the reaction and the redundant water flow through the first flow field 52, and are discharged to the outside through the discharge passage 48.
In the first embodiment, among the anode side power feeding element 40 and the cathode side power feeding element 42 of the membrane electrode assembly 32, at least in the anode side power feeding element 40, one surface of the sintered body 62 of titanium powder is subjected to the grinding process, and then, subjected to the etching process to form the smooth surface 40a. Therefore, in comparison with the case in which only the sintered body 62 of titanium powder is subjected to the grinding process, the porosity in the surface is increased desirably, and it becomes possible to desirably perform the water electrolysis process.
An experiment was conducted for comparison of electrolysis voltages at the time of electrolysis at high pressure in a first example according to the embodiment, a second example according to the embodiment, and a comparative example. In the first example, only the anode side power feeding element 40 was subjected to the surface grinding process, and then, subjected to the etching process. In the second example, both of the anode side power feeding element 40 and the cathode side power feeding element 42 were subjected to the surface grinding process, and then, subjected to the etching process. In the comparative example, both of the anode side power feeding element 40 and the cathode side power feeding element 42 were subjected to only the surface grinding process.
The etching process was performed under the etching condition in which solution obtained by mixing 10 ml of nitric acid, 10 ml of 10% hydrofluoric acid, and 180 ml of pure water was used as etching solution. The etching process was performed for an etching period of 90 seconds at room temperature. Further, the electrolysis process was performed under the high pressure electrolysis condition in which the hydrogen pressure produced on the side of the cathode catalyst layer 44b was 35 Mpa, and the temperature was 60° C.
As the solid polymer electrolyte membrane, Nafion, produced by DuPont was used. As the anode catalyst layer 44a, an RulrFeOx catalyst was used. As the cathode catalyst layer 44b, a platinum catalyst was used. The result is shown in
As shown in
In contrast, in the first example, the surface of the anode side power feeding element 40 is subjected to the grinding process, and then, subjected to the etching process. Thus, it becomes possible to desirably increase the porosity in the smooth surface 40a. Accordingly, even if the current density is increased, the oxygen produced in the anode catalyst layer 44a is smoothly discharged to the first flow field 52 through the anode side power feeding element 40, and the desired amount of water is supplied to the anode catalyst layer 44a. Accordingly, without any shortage of water supply, the desired water electrolysis process is performed advantageously.
In the second example, the same advantages as in the case of the first example can be obtained. Further, since the cathode side power feeding element 42 is also subjected to the grinding process, and then, subjected to the etching process to form the smooth surface 42a, it is possible to reduce the increase in the water electrolysis voltage even more reliably.
The unit cell 80 includes separators 82 sandwiching a membrane electrode assembly 32. In practice, a plurality of unit cells 80 are formed by stacking the separators 82 and the membrane electrode assemblies 32 alternately.
The separator 82 has a first flow field 52 on an anode surface 82a facing the anode side power feeding element 40, and a second flow field 54 on a cathode surface 82b facing the cathode side power feeding element 42. A seal member 84 is formed integrally with the separator 82 around the outer end of the separator 82.
In the second embodiment, the separators 82 and the membrane electrode assemblies 32 are stacked alternately. Therefore, the dimension in the stacking direction is effectively reduced advantageously. Further, the same advantages as in the case of the first embodiment can be obtained.
Though the first and second embodiments have been described in connection with the water electrolysis apparatus 10, the present invention is not limited in this respect. The present invention is applicable to various electrolysis apparatuses.
While the invention has been particularly shown and described with reference to preferred embodiments, it will be understood that variations and modifications can be effected thereto by those skilled in the art without departing from the spirit and scope of the invention as defined by the appended claims.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2005-51354 | Feb 2005 | JP | national |
