Classifications

• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
  • H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
  • H01M8/04201—Reactant storage and supply, e.g. means for feeding, pipes
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
  • H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
  • H01M8/04201—Reactant storage and supply, e.g. means for feeding, pipes
  • H01M8/04208—Cartridges, cryogenic media or cryogenic reservoirs
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/10—Fuel cells with solid electrolytes
  • H01M8/1009—Fuel cells with solid electrolytes with one of the reactants being liquid, solid or liquid-charged
  • H01M8/1011—Direct alcohol fuel cells [DAFC], e.g. direct methanol fuel cells [DMFC]
• • H—ELECTRICITY
  • H01—ELECTRIC ELEMENTS
  • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
  • H01M8/00—Fuel cells; Manufacture thereof
  • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
  • H01M8/2465—Details of groupings of fuel cells
  • H01M8/247—Arrangements for tightening a stack, for accommodation of a stack in a tank or for assembling different tanks
  • H01M8/2475—Enclosures, casings or containers of fuel cell stacks
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
  • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
  • Y02E60/30—Hydrogen technology
  • Y02E60/50—Fuel cells

Definitions

• Fuel cell storage container fuel cell mounted electronic device storage container, and fuel cell with container
• the present invention relates to a container used when a fuel cell or an electronic device equipped with a fuel cell is transported or stored.
• lithium ion secondary batteries In response to such a demand for secondary batteries, for example, lithium ion secondary batteries have been developed. In addition, the operation time of portable electronic devices tends to increase further. With lithium-ion secondary batteries, the power of materials and the power of structure have almost reached their limits in terms of energy density. Is becoming unable to meet the demands.
• Patent No. 3413111 and International Publication WO2005 / 112172A1 each relate to an internal vaporization type fuel cell that supplies vaporized fuel obtained by vaporizing liquid fuel such as methanol to an anode.
• the internal vaporization type DMFC described in Japanese Patent No. 3413111 includes a fuel permeation layer for holding liquid fuel, and a fuel vaporization layer for diffusing the vaporization component of the liquid fuel held in the fuel permeation layer. Thus, the vaporized liquid fuel is supplied from the fuel vaporization layer to the fuel electrode.
• Japanese Patent No. 3413111 and International Publication WO2005 / 112172A1 each relate to an internal vaporization type fuel cell that supplies vaporized fuel obtained by vaporizing liquid fuel such as methanol to an anode.
• the internal vaporization type DMFC described in Japanese Patent No. 3413111 includes a fuel permeation layer for holding liquid fuel, and a fuel vaporization layer for diffusing the vaporization component of the liquid fuel held in the fuel
• An object of the present invention is to provide a fuel cell storage container, a fuel cell-equipped electronic device storage container, and a fuel cell with a container capable of suppressing a decrease in output characteristics due to transportation or storage. .
• the fuel cell storage container according to the present invention includes a vent hole.
• the fuel cell-equipped electronic device storage container of the present invention includes a vent hole.
• a fuel cell with a container according to the present invention includes the fuel cell storage container and a fuel cell stored in the fuel cell storage container.
• a fuel cell with a container according to the present invention includes a container having a vent
• a container-equipped fuel cell comprising:
• the fuel cell includes an outer container having an air inlet
• a fuel cell with a container according to the present invention includes a container having a vent
• a container-equipped fuel cell comprising:
• the fuel cell includes an outer container having an air inlet
• Vaporized fuel supply means for supplying vaporized fuel to the anode, housed in the outer container,
• Water supply means for supplying the anode with water generated by the force sword, housed in the outer container;
• FIG. 1 is a schematic view showing a container-equipped fuel cell according to an embodiment of the present invention.
• FIG. 2 is a cross-sectional view schematically showing an example (direct methanol fuel cell) of the fuel cell of FIG.
• FIG. 3 is a schematic view showing a fuel cell storage container according to an embodiment of the present invention.
• FIG. 4 is a schematic view showing a fuel cell storage container according to another embodiment of the present invention.
• FIG. 5 is a schematic view showing a fuel cell storage container according to another embodiment of the present invention.
• Fig. 6 is a characteristic diagram showing changes in battery voltage and output density when the current density is changed in the fuel cells of Examples:! To 3 and Comparative Example.
• the present invention is not limited to the following embodiments as they are, but can be embodied by modifying the constituent elements without departing from the spirit of the invention in the implementation stage.
• Various inventions can be formed by appropriately combining a plurality of constituent elements disclosed in the following embodiments. For example, some components may be deleted from all the components shown in the embodiment. Furthermore, constituent elements over different embodiments may be appropriately combined.
• FIG. 1 schematically shows a fuel cell storage container according to an embodiment of the present invention.
• the container 1 has a rectangular tube shape, and a large number of circular vent holes 2 are opened on the surface.
• the shape of the vent hole is not limited to a circle, but may be, for example, a triangle, a square, a rectangle, a rhombus, a hexagon, an ellipse, or the like.
• the entire container 1 is vented
• the vent hole 2 may be opened only in a specific side or direction that does not have a hole.
• the configuration is not limited as long as air is introduced into the fuel cell.
• the open area ratio of the container 1 is desirably 50% or less. This is because if the open area ratio exceeds 50%, the strength of the container 1 may be insufficient, and water may leak during transportation. In order to sufficiently suppress the decrease in output due to transportation and storage, it is desirable to set the hole area ratio to 10% or more. A more preferable range is 30 to 50%. By setting this range, it is possible to achieve output characteristics that are the same as before transport and storage.
• Examples of the material forming the container 1 include paper, hard resin, foamed resin, rubber, fiber, metal, leather, and a combination of these materials.
• the fuel cell 3 is stored in the container 1 at the time of shipment, distribution in the market, or at the time of carrying.
• the type of the fuel cell 3 is not particularly limited, but includes a vaporized fuel supply means for supplying vaporized fuel to the anode, and a water supply means for supplying water generated by the power sword to the anode.
• a fuel cell is preferred. According to the present invention, when a fuel cell provided with vaporized fuel supply means and water supply means or a fuel cell-equipped electronic device equipped with the fuel cell is housed in an airtight container for transportation and storage, After that, when the liquid fuel was replenished and used, the output characteristics were deteriorated compared to before transport and storage, and the output characteristics were stored in a container equipped with vents for transport and storage. It has been found that the decrease in the resistance is suppressed.
• FIG. 2 shows an example of a fuel cell (direct methanol fuel cell) provided with vaporized fuel supply means and water supply means.
• a membrane electrode assembly (MEA) 5 is accommodated in the outer container 4.
• the membrane electrode assembly (MEA) 5 includes a cathode (oxidizer electrode) composed of a force sword catalyst layer 6a and a force sword gas diffusion layer 6b, and an anode (fuel electrode) composed of an anode catalyst layer 7a and an anode gas diffusion layer 7b. And a proton conductive electrolyte membrane 8 disposed between the force sword catalyst layer 6a and the anode catalyst layer 7a.
• the force sword catalyst layer 6a preferably includes force sword catalyst particles and a proton conductive material. That's right.
• the anode catalyst layer 7a preferably contains anode catalyst particles and a proton conductive material.
• Examples of the force sword catalyst and the anode catalyst include platinum group element simple metals (Pt, Ru, Rh, Ir, Os, Pd, etc.), alloys containing platinum group elements, and the like. It is desirable to use platinum as the cathode catalyst, but this is not a limitation.
• the anode catalyst is preferably Pt_Ru, which is highly resistant to methanol and carbon monoxide, but is not limited to this. Further, a supported catalyst using a conductive support such as a carbon material may be used, or an unsupported catalyst may be used.
• Examples of the proton conductive material included in the force sword catalyst layer 6a, the anode catalyst layer 7a, and the proton conductive electrolyte membrane 8 include fluorine having a sulfonic acid group such as perfluorocarbon sulfonic acid. It is also possible to use inorganic substances such as resin-based resins, hydrated carbon-based resins having sulfonic acid groups, and tungsten phosphotungstic acid.
• the force sword catalyst layer 6a is laminated on the force sword gas diffusion layer 6b, and the anode catalyst layer 7a is laminated on the anode gas diffusion layer 7b.
• the force sword gas diffusion layer 6b plays a role of uniformly supplying the oxidant gas to the force sword catalyst layer 6a.
• the anode gas diffusion layer 7b serves to uniformly supply fuel to the anode catalyst layer 7a.
• porous carbon paper can be used for the force sword gas diffusion layer 6b and the anode gas diffusion layer 7b.
• the anode conductive layer 9 as the anode current collector is laminated on the anode gas diffusion layer 7 b of the membrane electrode assembly 5.
• the force sword conductive layer 10 as the force sword current collector is laminated on the force sword gas diffusion layer 6 b of the membrane electrode assembly 5.
• the anode conductive layer 9 and the force sword conductive layer 10 are for improving the conductivity of the force sword and the anode.
• the anode conductive layer 9 and the force sword conductive layer 10 are provided with gas permeation holes (not shown) through which the oxidant gas or the vaporized fuel permeates.
• a gold electrode in which an Au foil is supported on a PET substrate can be used.
• One of the rectangular frame-shaped sealing materials 11 a is formed on the proton conductive electrolyte membrane 8 so as to surround the periphery of the force sword.
• the other l ib is the opposite side of the proton conducting electrolyte membrane 8.
• the sealing materials 11a and l ib function as O-rings for preventing fuel leakage and oxidant gas leakage from the membrane electrode assembly 5.
• a liquid fuel tank 12 as a fuel storage unit is disposed on the anode side of the membrane electrode assembly 5 (below the membrane electrode assembly 5 in FIG. 2).
• the liquid fuel tank 12 contains a liquid fuel 13 made of liquid methanol or methanol aqueous solution. It is desirable that the concentration of the methanol aqueous solution be higher than 50 mol%. The purity of pure methanol is desirably 95% by weight or more and 100% by weight or less.
• the liquid fuel stored in the liquid fuel tank 12 is not necessarily limited to methanol fuel.
• ethanol fuel such as ethanol aqueous solution and pure ethanol
• propanol fuel such as propanol aqueous solution and pure propanol
• aqueous glycol solution are pure.
• It can be Daricol fuel such as glycol, dimethyl ether, formic acid, or other liquid fuel.
• liquid fuel corresponding to the fuel cell is accommodated.
• liquid fuel tank 12 When the fuel cell is accommodated in the container 1, it is desirable to leave the liquid fuel tank 12 in an empty state, but there is no problem even when the fuel is filled. If the fuel is empty, occasionally the liquid fuel tank 12 can be supplemented with a small amount of liquid fuel 13 to reduce the output drop. Needless to say, liquid fuel 13 is replenished before the fuel cell is taken out of the container 1 and used.
• vaporized fuel supply means for supplying a vaporized component of the liquid fuel to the anode, for example, a gas-liquid separation membrane 14 is arranged.
• the gas-liquid separation membrane 14 is a membrane that allows only the vaporized component of the liquid fuel to permeate and does not allow the liquid fuel to permeate. Only the vaporized component of the liquid fuel permeates through the gas-liquid separation membrane 14, and the vaporized fuel can be supplied to the anode.
• a water-repellent membrane having methanol permeability can be used for the gas-liquid separation membrane 14.
• water-repellent membrane having methanol permeability examples include a silicone sheet, a polyethylene porous membrane, a polypropylene porous membrane, a polyethylene-polypropylene porous membrane, and a polytetrafluoroethylene porous membrane.
• a frame 15 a is arranged between the gas-liquid separation membrane 14 and the anode conductive layer 9.
• the space enclosed by frame 15a is a vaporization to adjust the amount of vaporized fuel supplied to the anode. Functions as a fuel storage chamber 16.
• a frame 15 b is laminated on the force sword conductive layer 10 of the membrane electrode assembly 5.
• a moisturizing plate 17 for suppressing the transpiration of water generated in the force sword catalyst layer 6a is laminated.
• the moisturizing plate 17 functions as a water supply means for supplying water generated by the force sword to the anode.
• the moisture retaining plate 17 is made of an insulating material that is inert to methanol and has dissolution resistance, oxygen permeability, and moisture permeability.
• an insulating material include polyolefin such as polyethylene and polypropylene.
• moisture retention plate 17 it is preferable air permeability defined by JIS P- 8117- 1998 is 50 seconds ZlOOcm 3 below. This is because if the air permeability exceeds ZlOOcm 3 for 50 seconds, air diffusion to the air inlet 18 force sword may be hindered and high output may not be obtained. A more preferable range of the air permeability is 10 seconds / 100 cm 3 or less.
• the moisture retaining plate 17 has a moisture permeability of 6000 g / m 224 h or less as defined by the JIS L-1099-1993 A-1 method.
• the value of moisture permeability is JIS L-1099-1993.
• the temperature is 40 ⁇ 2 ° C. This is because if the moisture permeability exceeds 60 00 g / m 2 24 h, the amount of water evaporated from the power sword increases, and the effect of promoting water diffusion from the power sword to the anode may not be sufficiently obtained. In addition, if the moisture permeability is less than 500 g / m 2 24 h, excess water may be supplied to the anode and high output may not be obtained, so the moisture permeability is 500 to 6000 g / m 2 24 h. Ability to make range S desirable. A more preferable range of moisture permeability is 1000 to 4000 g / m 2 24 h.
• the exterior container 4 has a plurality of air inlets 18 formed on the surface facing the moisture retention plate 17. Since the outer container 4 also plays a role of pressurizing the stack including the membrane electrode assembly 5 to enhance its adhesion, for example, a metal such as SUS304, carbon steel, stainless steel, alloy steel, titanium alloy, nickel alloy, etc. Formed from.
• a metal such as SUS304, carbon steel, stainless steel, alloy steel, titanium alloy, nickel alloy, etc. Formed from.
• the vaporized component of the liquid fuel 13 in the liquid fuel tank 12 is supplied to the anode catalyst layer 7 a through the gas-liquid separation membrane 14.
• protons (H + ) and electrons (e are generated by the oxidation reaction of the fuel.
• the catalyst reaction that occurs in the anode catalyst layer 7a is as follows ( Shown in equation 1). [0038] CH OH + HO ⁇ CO + 6H + + 6e "(1)
• Protons (H + ) generated in the anode catalyst layer 7a diffuse to the force sword catalyst layer 6a through the proton conductive membrane 8. At the same time, the electrons generated in the anode catalyst layer 7a flow through the external circuit connected to the fuel cell, work on the load (resistance, etc.) of the external circuit, and flow into the cathode catalyst layer 6a.
• Oxidant gas such as air passes from the air inlet 18 of the outer container 4 to the force sword catalyst layer 6a through the moisture retaining plate 17, the space in the frame 15b, the force sword conductive layer 10 and the force sword gas diffusion layer 6b. Supplied. Oxygen in the oxidant gas undergoes a reduction reaction with the proton (H + ) that has diffused through the proton-conducting membrane 8 and the electrons (e—) that have flowed through the external circuit, producing reaction products. To do. For example, when air is used as the oxidant gas, the reaction in which oxygen contained in the air is generated in the force sword catalyst layer 6a is expressed by the following equation (2). In this case, the reaction product is water (H0). is there.
• the moisture retaining plate 17 is disposed between the force sword and the outer container 4, the evaporation of water from the force sword is suppressed, and the amount of water retained in the force sword catalyst layer 6a is increased as the power generation reaction proceeds. To increase. For this reason, it is possible to create a state in which the moisture retention amount of the force sword catalyst layer 6a is larger than the moisture retention amount of the anode catalyst layer 7a. As a result, a reaction in which water generated in the cathode catalyst layer 6a moves to the anode catalyst layer 7a through the proton conductive membrane 8 can be promoted by the osmotic pressure phenomenon. This makes it possible to realize a small and high-power fuel cell.
• the container for storing the fuel cell is not limited to the structure shown in FIG. 1 described above.
• the container 1 is formed of a mesh plate as shown in FIG. May be used.
• the shape of the container is not limited to the rectangular tube shape as shown in FIGS. 1 and 3, for example, a bag shape as shown in FIG. 4 or a cylindrical shape as shown in FIG. is there.
• the container for storing the fuel cell may be provided with a detecting means for detecting the oxygen concentration in the container to detect a decrease in the oxygen concentration in the container.
• a humidity control mechanism is provided in the container.
• the fuel cell storage container can be applied to a container that stores one or a plurality of fuel cells, but is applied to a storage container as a container that stores a plurality of the storage containers. It is also possible to do.
• the force described as a container for housing the fuel cell 3 in the above description can be applied to an electronic device equipped with the fuel cell on which the fuel cell 3 is mounted.
• the fuel cell-mounted electronic device is transported for shipping, market distribution, etc., a packaging container for sale or storage to a customer, a container for storing a plurality of the packaging containers, etc. It can also be applied.
• the direct methanol fuel cell shown in Fig. 2 was produced as follows.
• Carbon particles carrying platinum ruthenium alloy fine particles were mixed with Dupont DE2020 and a homogenizer to prepare a slurry, which was applied to a carbon paper which is the anode gas diffusion layer 7b. Then, this was dried at room temperature to prepare an anode in which the anode catalyst layer 7a was laminated on the anode gas diffusion layer 7b.
• a perfluorocarbon sulfonic acid membrane (nafion (registered trademark) membrane, manufactured by DuPont) having a thickness of 30 am and a water content of 10 to 20% by weight is prepared as the proton conductive electrolyte membrane 8 did .
• This electrolyte membrane was sandwiched between a force sword and an anode, and pressed under the conditions of a temperature of 120 ° C. and a pressure of 10 kgf / cm 2 , thereby producing a membrane electrode assembly (MEA) 5.
• this membrane electrode assembly 5 is used for taking in air and vaporized methanol.
• a force sword conductive layer 10 and an anode conductive layer 9 were formed by sandwiching them with a gold foil having a plurality of openings.
• the laminated body in which the membrane electrode assembly (MEA) 5, the anode conductive layer 9, and the force sword conductive layer 10 described above was laminated was sandwiched between two frames 15a and 15b made of resin. Rubber O-rings 11a and 1 lb are inserted between the force sword side of the membrane electrode assembly 5 and one frame 15b, and between the anode side of the membrane electrode assembly 5 and the other frame 15a, respectively. Sealed with interposition. Further, the anode-side frame 15a was fixed to the liquid fuel tank 12 via a gas-liquid separation membrane 14 with screws. For the gas-liquid separation membrane 14, a 0.1 mm thick silicone sheet was used.
• a polyethylene porous film was prepared.
• a moisturizing plate 17 is arranged on the frame 15b on the force sword side.
• the obtained laminate is stored in an outer container 4 having a 2 mm-thick stainless steel plate (SUS304) in which air inlets 18 (diameter 2.5 mm, number 8) for air intake are formed.
• the direct methanol fuel cell shown in Fig. 2 was obtained.
• the obtained fuel cell was stored in the container 1 having the shape shown in Fig. 1 in a state where the liquid fuel tank 12 was filled.
• the material of the container was a resin material (polyethylene terephthalate) and the porosity was 50%. Storage conditions were stored in air at 30 ° C and 50% relative humidity for 48 hours.
• the fuel cell was taken out of the container 1, and 5 ml of pure methanol was injected into the liquid fuel tank 12 as the liquid fuel 13.
• the power density and the cell voltage were measured when the current density was increased.
• the results are shown in Fig. 6 where the change in output density is curve A1 and the change in battery voltage is curve B1.
• the horizontal axis in FIG. 6 is current density (mAZcm 2 ), the right vertical axis is output density (mW / cm 2 ), and the left vertical axis is battery voltage (V).
• Example 1 A fuel cell having the same configuration as described in Example 1 was manufactured, and the obtained fuel cell was stored in the container 1 having the shape shown in FIG. 1 in a state where the liquid fuel tank 12 was filled.
• container 1 the same one as in Example 1 was used except that the hole area ratio was 30%.
• the storage conditions were the same as in Example 1.
• Example 2 After storage, the fuel cell was taken out of the container 1 and liquid fuel 13 similar to that in Example 1 was injected into the liquid fuel tank 12. Next, the output density and battery voltage were measured in the same manner as in Example 1. The results are shown in Fig. 6 with the power density change as curve A2 and the battery voltage change as curve B2.
• Example 1 A fuel cell having the same configuration as described in Example 1 was manufactured, and the obtained fuel cell was stored in the container 1 having the shape shown in FIG. 1 in a state where the liquid fuel tank 12 was filled.
• the container 1 the same one as in Example 1 was used except that the opening ratio was 10%.
• the storage conditions were the same as in Example 1.
• Example 1 A fuel cell having the same configuration as described in Example 1 was manufactured, and the obtained fuel cell was stored in an airtight container without a vent hole in a state where the liquid fuel tank 12 was filled. .
• the storage conditions were the same as in Example 1.
• the present invention is not limited to the above-described embodiments as they are, and can be embodied by modifying the constituent elements without departing from the spirit of the invention in the implementation stage.
• Various inventions can be formed by appropriately combining a plurality of constituent elements disclosed in the embodiments. For example, some components may be deleted from all the components shown in the embodiment. Furthermore, constituent elements over different embodiments may be appropriately combined.
• the structure of the fuel cell has been described with the structure having the fuel storage part below the membrane electrode assembly (MEA).
• the fuel supply from the fuel storage part to the membrane electrode assembly is The fuel storage unit and the membrane electrode assembly may be connected via a flow path.
• a passive type fuel cell has been described as an example of the configuration of the fuel cell main body.
• the present invention can also be applied to other fuel cells.
• the semi-passive type fuel cell the fuel supplied from the fuel storage unit to the membrane electrode assembly is used for the power generation reaction, and is not circulated and returned to the fuel storage unit.
• the semi-passive type fuel cell is different from the conventional active method because the fuel does not circulate, and does not impair the downsizing of the device.
• the fuel cell uses a pump to supply fuel, and is different from the pure passive type such as the conventional internal vaporization type. For this reason, as described above, it is called a semi-passive fuel cell.
• a fuel cutoff valve may be arranged in place of the pump as long as fuel is supplied from the fuel storage unit to the membrane electrode assembly. In this case, the fuel cutoff valve is provided to control the supply of liquid fuel through the flow path.
• a fuel cell storage container a fuel cell-mounted electronic device storage container, and a fuel cell with a container that can suppress a decrease in output characteristics due to transportation or storage.

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• Electrochemistry (AREA)
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Citations (6)

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• 2007
  • 2007-03-26 JP JP2008509746A patent/JPWO2007116692A1/ja active Pending
  • 2007-03-26 WO PCT/JP2007/056238 patent/WO2007116692A1/ja not_active Ceased
  • 2007-03-29 TW TW096111096A patent/TW200810195A/zh not_active IP Right Cessation

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