1. Technical Field
Embodiments described herein relate to a carbon nanowall and a production method thereof, and to an oxygen reduction catalyst, an oxygen reduction electrode and a fuel cell each of which utilizes a carbon nanowall.
2. Description of the Related Art
Recently, as a source of clean energy, fuel cells have been focused. There are several kinds of fuel cells, and a solid polymer type fuel cell, which is a kind of them, utilizes a carbon material that carries platinum, as a catalyst for its electrode. For example, platinum may be allowed to be carried on a carbon nanowall and this is usable as a catalyst. However, platinum is a rare and expensive material. Thus, such an electrode that utilizes the carbon material carrying platinum as the catalyst requires high manufacturing cost. Accordingly, the use of platinum has been one of the causes of the insufficient prevalence of fuel cells.
As a material that can be utilized for the catalyst as a substitute for the carbon material carrying platinum, a carbon material doped with nitrogen has been proposed (see Non Patent Literature 1 or 2, for example). Since nitrogen is an easily available material, if using nitrogen as a material for the catalyst, it is possible to produce the catalyst which is to be utilized for the fuel cell, at low cost.
Non Patent Literature 1: Kuanping Gong and four others, “Nitrogen-Doped Carbon Nanotube Arrays with High Electocatalytic Activity for Oxygen Reduction”, Science vol. 323, p. 760-764, February 2009
Non Patent Literature 2: Liangti Qu and three others, “Nitrogen-Doped Graphene as Efficient Metal-Free Electorocatalyst for Oxygen Reduction in Fuel Cells” ACS Nano. 4, 2008
As described above, the conventional method had the problem of increasing the manufacturing cost of the electrode because of using platinum for the catalyst.
In the light of the problem described above, an object of the disclosure is to provide a carbon nanowall, an oxygen reduction catalyst, an oxygen reduction electrode and a fuel cell easily at low cost.
In order to achieve the above-described object, according to a first aspect, an oxygen reduction catalyst having a carbon nanowall doped with nitrogen is possibly provided.
Moreover, according to a second aspect, the oxygen reduction catalyst in which an amount of the nitrogen that is doped into the carbon nanowall ranges from 0.5 at % to 20.0 at % is possibly provided.
Further, according to a third aspect, the oxygen reduction catalyst in which a degree of crystallinity of the carbon nanowall doped with nitrogen ranges from 0.5 to 3.5 is possibly provided.
Furthermore, according to a fourth aspect, an oxygen reduction electrode comprising: a gas diffusion layer; and a catalyst layer which is arranged on the gas diffusion layer and which is of the oxygen reduction catalyst provided according to any one of the first to third aspects.
Moreover, according to a fifth aspect, the oxygen reduction electrode wherein the gas diffusion layer is of a carbon substrate and the catalyst layer is of the oxygen reduction catalyst formed on the gas diffusion layer that is made of the carbon substrate is possibly provided.
Further, according to a sixth aspect, the oxygen reduction electrode in which the catalyst layer is 1 μm or more can be provided.
Furthermore, according to a seventh aspect, a fuel cell comprising: an electrolyte membrane; the oxygen reduction electrodes which are respectively arranged on both sides of the electrolyte membrane and are provided according to any one of the fourth to sixth aspects; and separators that are respectively positioned outside the electrodes, is possibly provided.
According to the disclosure, it is possible to provide the carbon nanowall, the oxygen reduction catalyst, the oxygen reduction electrode and the fuel cell at low cost.
The features and advantages of the carbon nanowall and production method thereof, the oxygen reduction catalyst, the oxygen reduction electrode and the fuel cell according to the disclosure will more clearly understood from the following description of the conjunction with the accompanying drawings in which identical reference letters designate the same or similar elements or cases throughout the figures and in which:
The term “carbon nanowall” used herein is defined as a two-dimensional carbon nanostructure or a carbon material having a wall-like structure of nanometer size.
An oxygen reduction catalyst according to a first embodiment is a carbon nanowall doped with nitrogen or nitrogen-doped carbon nanowall pieces. Moreover, an oxygen reduction electrode according to the first embodiment includes: a gas diffusion layer; and an oxygen reduction catalyst that is to be a catalyst layer. Further, a fuel cell according to the first embodiment comprises: an electrolyte membrane; a gas diffusion layer; an oxygen reduction catalyst that is to be the catalyst layer; and a separator.
(Oxygen Reduction Catalyst)
The oxygen reduction catalyst according to the first embodiment is the carbon nanowall doped with nitrogen or carbon nanowall pieces composed of one or plural domains of nanographite which are smaller than the carbon nanowall. The carbon nanowall pieces are obtained by pulverizing the carbon nanowall doped with nitrogen. The carbon nanowall doped with nitrogen is produced on a substrate, for example, a silicon substrate or the like, and it is stripped from the substrate after doped with nitrogen.
For example, by utilizing an apparatus 1 illustrated in
For example, the substrate 2 on which the carbon nanowall is produced is placed on the supporting device 11 in the reaction chamber 10, and thereafter, the nitrogen gas is supplied into the reaction chamber 10 by the gas supplier 13. This reaction chamber 10 is a vacuum chamber so that other gas such as air may not enter from outside, while the carbon nanowall on the substrate 2 is doped with nitrogen. Moreover, it is preferred that the supporting device 11 possibly fixes the substrate 2 thereto. Further, the nitrogen gas supplied by the gas supplier 13 may be a gas that contains nitrogen and it is, for example, a mixed gas of argon and nitrogen.
Next, plasma is generated by the plasma generator 12 using a discharge gas for generating plasma, and the generated plasma is supplied into the reaction chamber 10. Subsequently, in the reaction chamber 10, the carbon nanowall on the substrate 2 is doped with nitrogen, which is contained in the nitrogen gas supplied by the gas supplier 13, by the plasma supplied from the plasma generator 12. That is, nitrogen atoms of the nitrogen gas are excited and ionized by the plasma, so that the carbon nanowall is doped therewith. Thus, the atoms that compose the nitrogen are possibly put into the carbon structure that constitutes the carbon nanowall.
Alternatively, it is also possible to support a substrate 2 on which the carbon nanowall is not produced, by the supporting device 11 of the reaction chamber 10, and to produce then the carbon nanowall on the substrate 2 by utilizing the apparatus 1, thereafter doping the carbon nanowall with the nitrogen by utilizing the apparatus 1 as described above.
A method for stripping the carbon nanowall doped with nitrogen from the substrate 2 is not limited, but may be, for example, a method utilizing a scraper. Moreover, a method for pulverizing the carbon nanowall that is stripped from the substrate 2 is also not limited, and an example of carbon nanowall pieces which are obtained by pulverizing the carbon nanowall manually with an agate mortar for 20 minutes will be described below.
For example, the carbon nanowall doped with nitrogen, which is the oxygen reduction catalyst according to the first embodiment, provides XPS spectra which are shown in
Condition A1: pressure of 0.67 Pa; heating temperature of 700° C.; a discharge current of 70 A; a flow rate of argon of 80 sccm; a flow rate of hydrogen of 10 sccm; a flow rate of methane of 10 sccm; and a growth time of 360 minutes.
Condition A2: pressure of 0.36 Pa; heating temperature of 600° C.; a discharge current of 50 A; a flow rate of argon of 80 sccm; a flow rate of hydrogen of 10 sccm; a flow rate of nitrogen of 10 sccm; and a processing time of 5 minutes.
A composition ratio of the carbon nanowall of
Further,
(Electrode)
As illustrated in
(Fuel Cell)
As shown in
As described above, the oxygen reduction catalyst according to the first embodiment can be produced at low cost by utilizing the nitrogen-doped carbon nanowall or carbon nanowall pieces. Also, by utilizing the oxygen reduction catalyst according to the first embodiment, the electrode and the fuel cell can be produced at low cost.
Condition B1: pressure of 0.67 Pa; heating temperature of 600° C.; a discharge current of 50 A; a flow rate of argon of 80 sccm; a flow rate of hydrogen of 10 sccm; a flow rate of methane of 10 sccm; and a growth time of 360 minutes.
Condition B2: pressure of 0.67 Pa; heating temperature of 700° C.; a discharge current of 70 A; a flow rate of argon of 80 sccm; a flow rate of hydrogen of 0 sccm; a flow rate of nitrogen of 20 sccm; and a processing time of 1 minute.
In the Raman scattering spectra of
In the XPS spectra shown in
In the example illustrated in
A carbon nanowall doped with nitrogen of Example 2 was obtained by: producing a carbon nanowall on a silicon substrate under Condition C1 by utilizing the apparatus 1 that was described above with reference to
Condition C1: pressure of 0.67 Pa; heating temperature of 800° C.; a discharge current of 50 A; a flow rate of argon of 80 sccm; a flow rate of hydrogen of 0 sccm; a flow rate of methane of 20 sccm; and a growth time of 360 minutes.
Condition C2: pressure of 0.67 Pa; heating temperature of 800° C.; a discharge current of 50 A; a flow rate of argon of 80 sccm; a flow rate of hydrogen of 10 sccm; a flow rate of nitrogen of 10 sccm; and a processing time of 1 minute.
In the example illustrated in
A carbon nanowall doped with nitrogen of Example 3 was obtained by: producing a carbon nanowall on a silicon substrate under Condition D1 by utilizing the apparatus 1 that was described above with reference to
Condition D1: pressure of 0.67 Pa; heating temperature of 700° C.; a discharge current of 70 A; a flow rate of argon of 80 sccm; a flow rate of hydrogen of 10 sccm; a flow rate of methane of 10 sccm; and a growth time of 360 minutes.
Condition D2: pressure of 0.36 Pa; heating temperature of 600° C.; a discharge current of 50 A; a flow rate of argon of 80 sccm; a flow rate of hydrogen of 10 sccm; a flow rate of nitrogen of 10 sccm; and a processing time of 5 minutes.
In the example illustrated in
An oxygen reduction catalyst according to a second embodiment is a nitrogen-doped carbon nanowall which is produced on carbon paper or carbon cloth.
(Oxygen Reduction Catalyst)
Comparing the oxygen reduction catalyst according to the second embodiment with the oxygen reduction catalyst according to the first embodiment, the oxygen reduction catalyst according to the first embodiment was obtained by: producing the carbon nanowall on the substrate such as a silicon substrate; doping this carbon nanowall with nitrogen; and subsequently stripping this carbon nanowall from the substrate. On the other hand, the oxygen reduction catalyst according to the second embodiment is different from the oxygen reduction catalyst according to the first embodiment in that the carbon nanowall, which is to be doped with nitrogen, is produced on a carbon substrate such as the carbon paper and the carbon cloth. Incidentally, for the production of the carbon nanowall on the carbon substrate and the doping of the carbon nanowall with nitrogen, the apparatus which was described above with reference to
Condition E1: pressure of 0.67 Pa; heating temperature of 700° C.; a discharge current of 70 A; a flow rate of argon of 80 sccm; a flow rate of hydrogen of 10 sccm; a flow rate of methane of 10 sccm; and a growth time of 360 minutes.
Condition E2: pressure of 0.67 Pa; heating temperature of 700° C.; a discharge current of 70 A; a flow rate of argon of 80 sccm; a flow rate of hydrogen of 0 sccm; a flow rate of nitrogen of 20 sccm; and a processing time of 1 minute.
Incidentally, similar to the oxygen reduction catalyst according to the first embodiment, an amount of the nitrogen contained in the oxygen reduction catalyst according to the second embodiment preferably ranges from about 0.5 at % to about 20.0 at %. Moreover, as the oxygen reduction catalyst, an area ratio of the pyridine nitrogen to the sp2 nitrogen in the XPS spectrum preferably ranges from 1:0.4 to 1:1.5. Further, as the oxygen reduction catalyst, the degree of crystallinity (ID/IG) obtained by the intensity ratio of the D-band to the G-band in the Raman scattering spectrum preferably ranges from 0.5 to 3.5.
(Electrode)
As illustrated in
Further, the gas diffusion layer 32 is of the carbon paper or the carbon cloth that has been utilized as the carbon substrate for the production of the carbon nanowall. Here, the catalyst layer 31 has preferably a thickness of 1 μm or more.
(Fuel Cell)
As shown in
As described above, the oxygen reduction catalyst according to the second embodiment can be produced at low cost by utilizing the carbon nanowall doped with nitrogen.
Moreover, in the electrode 35 according to the second embodiment, the gas diffusion layer 32 can be of the carbon paper or the carbon cloth which has been utilized as the carbon substrate for the production of the carbon nanowall, and the catalyst layer 31 can be of the oxygen reduction catalyst produced on the gas diffusion layer 32 that is of the carbon substrate. Thus, the electrode 35 according to the second embodiment does not require the process of stripping from the substrate the carbon nanowall that is the oxygen reduction catalyst or the process of depositing the oxygen reduction catalyst to the gas diffusion layer 32, so that the production of the electrode 35 can be realized at the same time as the production of the oxygen reduction catalyst. That is, the electrode 35 that is the oxygen reduction electrode can be produced easily.
Further, since the oxygen reduction catalyst and the electrode 35 can be produced at the same time, the fuel cell 3 can also be produced easily.
As described above, the disclosure has been explained in detail by way of the embodiments, but it is to be understood that the disclosure is not limited to the specific embodiments that are described in the instant specification. The scope shall be determined by description of claims and equivalents thereof.
Number | Date | Country | Kind |
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2013-021911 | Feb 2013 | JP | national |
This application is a continuation application of International Application No. PCT/JP2014/052860, filed on Feb. 7, 2014, which claims priority of Japanese Patent Application No. 2013-021911, filed on Feb. 7, 2013, the entire contents of which are incorporated by references herein.
Number | Date | Country | |
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Parent | PCT/JP2014/052860 | Feb 2014 | US |
Child | 14818640 | US |