Patent Application
20210123151
The present invention relates to a manganese oxide for a water oxidation catalyst, a manganese oxide/carbon mixture for a water oxidation catalyst, a manganese oxide composite electrode material, and their production methods and their applications. More particularly, the present invention relates to a manganese oxide, a manganese oxide/carbon mixture, and a manganese oxide composite electrode material, used as an anode catalyst for oxygen evolution in industrial water electrolysis conducted under alkaline conditions, under neutral conditions or under acidic conditions, or in water electrolysis using a polymer electrolyte membrane (PEM) type electrolytic cell, and their production methods.
From the viewpoint of depletion of fossil fuel and environmental pollution, utilization of hydrogen as a clean energy and its production process have attracted attention. Water electrolysis method is one of useful means to produce high purity hydrogen gas from a cathode by electrolyzing water and is characterized by oxygen evolution from an anode as the counter electrode at the same time. In order that the water decomposition reaction efficiently proceeds in the water electrolysis method, it is necessary to conduct electrolysis while the electrolysis voltage applied through the electrolysis is kept low, using an electrode catalyst with a low hydrogen overvoltage for the cathode and an electrode catalyst with a low oxygen overvoltage for the anode. As an electrode catalyst material capable of providing excellent low oxygen overvoltage for the anode, compounds represented by rare platinum group metals such as platinum (Pt), iridium (Ir) and ruthenium (Ru), and oxides containing such elements, have been proposed (Patent Documents 1 and 2, Non-Patent Documents 1 to 3).
On the other hand, since an electrode constituted by such a platinum group metal is very expensive, development of an electrode catalyst using an inexpensive transition metal has been in progress. For example, in recent years, transition metal materials constituted by manganese (Mn), iron (Fe), cobalt (Co) or nickel (Ni) have been proposed (Patent Documents 3 and 4, Non-Patent Documents 4 to 7).
However, the catalyst materials constituted by transition metals proposed are problematic in that their activity is very low (the oxygen overvoltage is high) as compared with platinum metal type electrode catalysts. That is, an oxygen evolution electrode catalyst material which is constituted by an inexpensive transition metal and which has a high catalytic activity comparable to platinum group metals such as Pt has not yet been realized, and development of such material is expected.
The object of the present invention is to provide a manganese oxide for a water oxidation catalyst, a manganese oxide/carbon mixture, a manganese oxide composite electrode material, and their production methods.
More particularly, it is to provide a manganese oxide for a water oxidation catalyst (hereinafter sometimes referred to as the manganese oxide of the present invention) which is an anode catalyst material for oxygen evolution in industrial water electrolysis conducted under alkaline conditions, under neutral conditions or under acidic conditions or in water electrolysis using a polymer electrolyte membrane (PEM) type electrolytic cell, which is available at a low cost and which has high oxygen evolution catalytic activity, a manganese oxide/carbon mixture for a water oxidation catalyst, a manganese oxide composite electrode material and their production methods.
The present inventors have conducted extensive studies on catalyst materials used as an oxygen evolution electrode catalyst in water electrolysis and as a result, found that a manganese oxide having a metallic valence of higher than 3.0 and at most 4.0 and having the average primary particle size controlled to be at most 80 nm and the average secondary particle size controlled to be at most 25 μm, has high oxygen evolution electrode catalytic activity, and accomplished the present invention. That is, the present invention provides a manganese oxide for an oxygen evolution electrode catalyst in water electrolysis, having a metallic valence of higher than 3.0 and at most 4.0, and having the average primary particle size controlled to be at most 80 nm and the average secondary particle size controlled to be at most 25 μm.
The present inventors have further found that when the manganese oxide of the present invention and carbon as an electrically conductive material are mixed, the optimum mixing ratio is, as the proportion of the manganese oxide, is at least 0.5 wt % and at most 40 wt %, whereby excellent catalytic activity of the manganese oxide of the present invention is sufficiently achieved, and more excellent catalytic activity is achieved particularly in PEM type water electrolysis under acidic conditions. That is, the present invention provides a manganese oxide/carbon mixture for an oxygen evolution electrode catalyst in water electrolysis, having a proportion of the manganese oxide to the total of the manganese oxide of the present invention and an electrically conductive carbon of at least 0.5 wt % and at most 40 wt %.
The present inventors have further found that a manganese oxide composite electrode material comprising fibers of an electrically conductive substrate, at least part of which are covered with the manganese oxide of the present invention, has further higher oxygen evolution electrode catalytic activity. That is, the present invention provides a manganese oxide composite electrode material for an oxygen evolution electrode, which comprises an electrically conductive substrate constituted by fibers at least part of which are covered with the manganese oxide of the present invention.
The manganese oxide of the present invention, the manganese oxide/carbon mixture of the present invention, and the manganese oxide composite electrode material of the present invention, have high activity and function as an inexpensive and excellent anode catalyst for oxygen evolution, in industrial water electrolysis conducted under alkaline conditions, under neutral conditions or under acidic conditions, and in water electrolysis using a PEM type electrolytic cell.
Further, by adding carbon dioxide to the electrolysis system, carbon dioxide is reduced at the cathode, whereby hydrocarbon compounds (such as formic acid, formaldehyde, methanol, methane, ethane and propane) may be produced.
Now, the present invention will be described in further detail.
First, decomposition of water by electrolysis will be described with reference to a reaction in which the reaction site is in an acidic environment, such as PEM type water electrolysis, as an example. On the cathode catalyst, hydrogen is formed by a reaction of two protons and two electrons as shown in Formula 1.
2H++2e−→H2 Formula 1
On the other hand, on the anode catalyst, oxygen is formed together with four electrons and four protons from two water molecules, as shown in Formula 2.
2H2O→O2+4H++4e− Formula 2
And, as a whole, a reaction by which two hydrogen molecules and one oxygen molecule are formed from two water molecules occurs, as shown in Formula 3.
2H2O→2H2+O2 Formula 3
The oxygen evolution reaction in the Formula 2 is generally considered as the rate-determining step in the whole reaction, and development of a catalyst which can promote the reaction with a minimum energy is considered to be important in this technical field. The present invention is to provide an oxygen evolution electrode catalyst which has high water oxidation catalytic performance.
The manganese oxide of the present invention has a manganese with metallic valence of higher than 3.0 and at most 4.0. A manganese oxide having a metallic valence of 3.0 or lower has low chemical stability as a catalyst material and particularly when used in acidic environment as in the case of PEM, it is likely to be eluted as divalent manganese ions one-sidedly and be exhausted.
On the other hand, a manganese oxide having a valence state higher than 4.0 also has low chemical stability since soluble pentavalent manganese or heptavalent manganese is contained, and stable catalytic activity is hardly obtained. In order to obtain favorable oxygen evolution catalytic activity, it is preferred to control the manganese metallic valence to be at least 3.5 and at most 4.0, more preferably at least 3.7 and at most 4.0.
The average primary particle size of the manganese oxide of the present invention is adjusted to be at most 80 nm. If the average primary particle size is larger than 80 nm, the reaction catalyst active sites tend to decrease, and the catalytic activity tends to be insufficient. In order to obtain favorable catalytic activity, the average primary particle size is preferably at most 70 nm, particularly preferably at most 50 nm. The lower limit of the average primary particle size is not particularly limited, and the average primary particle size is usually at least 5 nm, preferably at least 10 nm.
The average primary particle size is defined as follows and is obtained as described hereinafter. Krumbein diameters are measured by microscope method to obtain number averages of major axis lengths and minor axis lengths, which are respectively taken as the average major axis length and the average minor axis length, from which the two axes average size (half of the sum of the average major axis length and the average minor axis length) is obtained and is defined as the average primary particle size.
The average secondary particle size of the manganese oxide of the present invention is at most 25 μm. If the average secondary particle size is larger than 25 μm, the contact site with carbon as an electrically conductive material decreases, as described hereinafter, and transfer of electrons which contribute to the reaction is inhibited, whereby the catalytic activity tends to be insufficient. In order to obtain favorable catalytic activity, the average secondary particle size is preferably at most 10 μm, more preferably at most 5 μm, further preferably at most 2 μm. The lower limit of the average secondary particle size is not particularly limited, and the average secondary particle size is usually at least 0.1 μm, preferably at least 0.5 μm.
The average secondary particle size is defined by a measured value of wet type particle size distribution equipment using laser diffraction method and is obtained as described hereinafter.
The manganese oxide of the present invention preferably has a BET specific surface area of at least 10 m2/g and at most 260 m2/g. If the BET specific surface area is smaller than 10 m2/g, penetration of the electrolytic solution into the reaction site is inhibited, and therefore, the catalytic activity tends to be insufficient. On the other hand, if it exceeds 260 m2/g, closed porous structures tend to be dominant, which inhibit not only penetration of the electrolytic solution into the manganese oxide particles but also electron conduction and ionic migration. Therefore the catalytic activity tends to be insufficient. The BET specific surface area is more preferably at least 30 m2/g and at most 260 m2/g, particularly preferably at least 35 m2/g and at most 255 m2/g.
The crystal structure of the manganese oxide of the present invention is not particularly limited, and is preferably so-called γ type or α type, particularly preferably γ type.
Further, the electrode potential of the manganese oxide of the present invention is not particularly limited, and as the alkali potential in a 40 wt % KOH solution, preferably at least 200 mV and at most 320 mV, particularly preferably at least 240 mV and at most 300 mV.
By making the manganese oxide of the present invention be supported on the electrode, the manganese oxide of the present invention functions as the oxygen evolution electrode active material in water electrolysis and can impart the catalytic performance for the water oxidation reaction to the oxygen evolution electrode. By laminating the oxygen evolution electrode containing the oxygen evolution electrode active material, a polymer electrolyte membrane and an electrode having a hydrogen evolution catalyst, a laminate is obtained. The polymer electrolyte membrane may, for example, be a fluororesin type cation exchange membrane, and the hydrogen evolution catalyst may, for example, be platinum fine particles. In the present invention, by the oxygen evolution electrode, a water electrolysis apparatus can be constituted, and by water electrolysis using the oxygen evolution electrode, hydrogen can be produced efficiently.
Now, the method for producing the manganese oxide of the present invention will be described.
Among the manganese oxides of the present invention, a manganese oxide having a relatively large BET specific surface area, for example, a BET specific surface area of larger than 50 m2/g, may be obtained by treating a manganese oxide having low valence, for example, lower than 3.0, preferably 2.5 to 3.0, with a high concentrated acid to conduct disproportionation reaction.
The low valence manganese oxide may, for example, be a manganese oxide such as trimanganese tetroxide (Mn3O4) obtained by mixing a solution containing divalent manganese ions with an alkaline solution and oxidizing the obtained mixed solution, manganese sesquioxide (Mn2O3) or a mixture thereof. The oxidation of the mixed solution may be conducted using an oxidizing agent such as air or oxygen. The low valence manganese oxide is preferably trimanganese tetroxide (Mn3O4).
The formulae 3 and 4 show disproportionation reaction in the case of using trimanganese tetroxide (Mn3O4) as the low valence Mn oxide.
Mn3O4+8H+→Mn2++2Mn3++4H2O Formula 3
2Mn3++2H2→MnO2+Mn2++4H+ Formula 4
Further, the formulae 5 and 6 show disproportionation reaction in the case of using manganese sesquioxide (Mn2O3) as the low valence Mn oxide.
Mn2O3+6H+→2Mn3++3H2O Formula 5
2Mn3++2H2O→MnO2+Mn2++4H+ Formula 6
The manganese oxide of the present invention may be obtained by immersing a low valence Mn oxide in a high concentrated acid solution, followed by stirring for a certain time with heating, and by filtration. The kind of the acid may, for example, be sulfuric acid or nitric acid, and the concentration of the acid solution may, for example, be at least 1 mol/L (liter) and at most 8 mol/L. The stirring may be conducted with heating to, for example, at least 40° C. and at most 90° C., for a stirring time of, for example, at least 1 hour and at most 72 hours. The liter may sometimes be represented as L for convenience, and the same applies hereinafter.
On the other hand, among the manganese oxides of the present invention, a manganese oxide having a BET specific surface area of, for example, at most 50 m2/g, may be obtained by electrolysis, for example, using as an electrolytic solution a sulfuric acid/manganese sulfate mixed solution, at a sulfuric acid concentration in the sulfuric acid/manganese sulfate mixed solution of higher than 25 g/L and at most 65 g/L for example, at an electrolysis current density of at least 0.3 A/dm2 and at most 0.9 A/dm2, at an electrolysis temperature of at least 93° C. and at most 98° C.
In the above method for producing the manganese oxide by electrolysis, a method by using a sulfuric acid/manganese sulfate mixed solution as an electrolytic solution, is different from an electrolysis method by using only manganese sulfate aqueous solution as an electrolytic solution, it is possible to control the sulfuric acid concentration during the electrolysis period, whereby the sulfuric acid concentration can be optionally set even when the electrolysis is carried out for a long period of time.
In the method for producing the manganese oxide by electrolysis using the sulfuric acid/manganese sulfate mixed solution, a sulfuric acid concentration is controlled preferably to higher than 25 g/L and at most 65 g/L, more preferably at least 32 g/L and at most 50 g/L.
Further, it is preferred to optionally change the sulfuric acid concentration during the electrolysis, particularly to control the sulfuric acid concentration at the time of completion of the electrolysis to be higher than the sulfuric acid concentration at the time of start of the electrolysis, so as to control the average primary particle size and the electrode potential to be within preferred ranges. In such a case, the sulfuric acid concentration at the time of start of the electrolysis is preferably higher than 28 g/L and at most 40 g/L, more preferably higher than 30 g/L and at most 35 g/L. Further, the sulfuric acid concentration at the time of completion of the electrolysis is preferably at least 32 g/L and at most 55 g/L, more preferably higher than 35 g/L and at most 50 g/L, further preferably higher than 40 g/L and at most 45 g/L.
The mechanism of the effect obtained when the sulfuric acid concentration is changed as mentioned above is not clearly understood, but is considered as follows. By conducting electrolysis at a relatively low sulfuric acid concentration in a first half stage of the reaction, not only corrosion damages on the electrode substrate such as a pure titanium plate are directly reduced, but also a manganese oxide deposited layer having a relatively large primary particle size, a small BET specific surface area and high packing property can be obtained in a first half stage. Then, in the electrolysis at a relatively high sulfuric acid concentration in a latter half stage, since the electrode substrate such as a pure titanium plate has been already covered with the manganese oxide deposited layer, it is less susceptible to corrosion damages, and a manganese oxide with a higher anode electrode potential is likely to be obtained.
In the method for producing the manganese oxide by electrolysis, it is preferred to change the sulfuric acid concentration as between the first half stage of the electrolysis and the latter half stage of the electrolysis, not to gradually change the sulfuric acid concentration during the electrolysis from the start of the electrolysis until completion of the electrolysis.
The proportion of the electrolysis time in the first half stage of the electrolysis to the latter half stage of the electrolysis is not particularly limited and for example, the proportion of the electrolysis time at a low sulfuric acid concentration to the electrolysis time at a high sulfuric acid concentration is preferably within a range of from 1:9 to 9:1, particularly preferably within a range of from 3:7 to 7:3.
The sulfuric acid concentration in the sulfuric acid/manganese sulfate mixed solution is a value excluding divalent anion (sulfate ion) of manganese sulfate.
In the method for producing the manganese oxide by electrolysis, the electrolysis current density is not particularly limited but is preferably at least 0.3 A/dm2 and at most 0.9 A/dm2, so as to maintain an appropriate BET specific surface area, whereby the manganese oxide of the present invention can readily be produced by electrolysis efficiently and stably. In order to obtain the manganese oxide of the present invention more stably, the electrolysis current density is more preferably at least 0.5 A/dm2 and at most 0.88 A/dm2, further preferably at least 0.55 A/dm2 and less than 0.8 A/dm2.
In the production of the manganese oxide by electrolysis, it is possible to supply the sulfuric acid/manganese sulfate mixed solution, and the manganese concentration in the electrolytic solution supplied is not particularly limited and may, for example be from 30 to 60 g/L.
The electrolysis temperature may, for example, be at least 93° C. and at most 98° C. The efficiency for production of the manganese oxide deposited by electrolysis depends on the electrolysis temperature, and accordingly the electrolysis temperature is preferably higher than 94° C.
The manganese oxide formed on an electrode such as a pure titanium plate by electrolysis is separated from the electrode and roughly crushed e.g. by a jaw crusher, and ground and adjusted so to have a predetermined average secondary particle size as a manganese oxide simple substance e.g. by a roller mill, a vertical mill, a Loesche mill or a jet mill. Then, the produced manganese oxide is subjected to a washing step and a neutralizing step, to remove the remaining electrolytic solution and then dried e.g. by a flash drying apparatus. At the time of flash drying, a submicron-level manganese oxide fine powder formed as by-product by overgrinding in the grinding step may be recovered and separated by a bag filter of a dust collector. Further, a calcining step at a temperature of at least 200° C. and at most 500° C. may sometimes be conducted to obtain the manganese oxide of the present invention.
The manganese oxide/carbon mixture of the present invention preferably has a proportion of the manganese oxide of at least 0.5 wt % and at most 40 wt %. If the proportion is less than 0.5 wt %, the intrinsic reaction active sites of the manganese oxide decrease, and the catalytic activity will be insufficient, and if it exceeds 40 wt %, the contact between the manganese oxide and carbon as the electrically conductive material will be impaired, and it is supposed that transfer of electrons which contribute to the reaction is restricted.
In order that excellent catalytic activity is exhibited, the proportion of the manganese oxide is preferably at least 1 wt % and at most 20 wt %, more preferably at least 2 wt % and at most 17 wt %, further preferably at least 4 wt % and at most 10 wt %.
The XRD of the manganese oxide/carbon mixture of the present invention has characteristic diffraction lines. The diffraction pattern has, in order from the low angle side, at least diffraction lines which provide d representing the interplanar spacings of 0.355±0.01 nm, 0.265±0.01 nm, 0.250±0.05 nm, 0.240±0.004 nm, 0.219±0.004 nm, 0.208±0.004 nm, 0.167±0.002, and 0.143±0.002 nm.
By making the manganese oxide/carbon mixture of the present invention be supported on the electrode, the manganese oxide/carbon mixture of the present invention functions as the oxygen evolution electrode active material in water electrolysis and can impart catalytic performance in water oxidation reaction to the oxygen evolution electrode. By laminating the oxygen evolution electrode containing the oxygen evolution electrode active material, a polymer electrolyte membrane and an electrode having a hydrogen evolution catalyst, a laminate is obtained. The polymer electrolyte membrane may, for example, be a fluororesin type cation exchange membrane, and the hydrogen evolution catalyst may, for example, be platinum fine particles. In the present invention, by the oxygen evolution electrode, a water electrolysis apparatus can be constituted, and by water electrolysis using the oxygen evolution electrode, hydrogen can be produced.
As the method for producing the manganese oxide/carbon mixture of the present invention, it is preferred to mix the manganese oxide obtained by the above method, in its ratio of at least 0.5 wt % and at most 40 wt %, with carbon by the following wet mixing method.
In the wet mixing method, it is preferred that first, a predetermined amount of the manganese oxide and a predetermined amount of carbon are weighed, loosened and mixed in an agate mortar, and the mixture is put, for example, in a pot in which a dispersion medium such as ethanol and balls of e.g. zirconia are put, and rotated, for example, overnight or longer, in a slurry state to conduct ball mill mixing.
After completion of the ball mill mixing, the obtained slurry is subjected to sieving to remove the zirconia balls, and a manganese oxide/carbon mixture is recovered in the form of an ethanol slurry. To the recovered ethanol slurry of the manganese oxide/carbon mixture, materials necessary for an electrode, for example, Nafion (trademark by Chemours, the same applies hereinafter) dispersion (DE520, DE521, DE1020, DE1021, DE2020 or DE2021), are added to prepare an electrically conductive catalyst ink, which can be used as a catalyst-forming slurry to be applied on an electrode.
After the slurry is applied on an electrode, ethanol as the dispersion medium is evaporated e.g. by air-drying, whereby an electrode catalyst having a manganese oxide/carbon catalyst present in a thin film form on its surface can be formed.
The manganese oxide composite electrode material of the present invention comprises an electrically conductive substrate constituted by fibers at least part of which are covered with the manganese oxide of the present invention. In such a case, the amount of the covering manganese oxide of the present invention is, per geometrical area of the electrically conductive substrate, preferably at least 0.1 mg/cm2 and at most 25 mg/cm2. The geometrical area corresponds to the project area of the electrically conductive substrate, and the thickness of the substrate is not considered.
When the amount of the covering manganese oxide of the present invention is within the above range, the fibers can be covered with the manganese oxide in an islands form or substantially the whole outer surface of the fibers can be covered, depending on the diameter and the porosity of the fibers constituting the electrically conductive substrate, and the average covering thickness can be adjusted to be approximately at most 25 μm. Since the manganese oxide covering the fibers is constituted by secondary particles, usually, the average covering thickness and the average secondary particle size of the manganese oxide constituting the covering agree with each other.
In the manganese oxide composite electrode material of the present invention, in proportion to the amount of the covering manganese oxide, the average thickness of the manganese oxide covering the fibers of the electrically conductive substrate increases, and the amount of the covering manganese oxide is preferably at least 0.1 mg/cm2 and at most 20 mg/cm2, further preferably at least 0.2 mg/cm2 and at most 15 mg/cm2, particularly preferably at least 5 mg/cm2 and at most 10 mg/cm2. The thickness of the manganese oxide covering layer may be obtained also by, for example, subtracting the diameter of an electrically conductive fiber as a unit constituting the electrically conductive substrate, from a scanning electron microscope (SEM) image.
The XRD of the manganese oxide composite electrode material of the present invention has characteristic diffraction lines. In a case where the electrically conductive substrate is carbon paper, the XRD has, in order from the low angle side, at least diffraction lines which provide d representing the interplanar spacings of 0.405±0.01 nm, 0.34±0.01 nm, 0.306±0.005 nm, 0.244±0.004 nm, 0.213±0.004 nm, 0.169±0.002 nm, 0.164±0.002 nm and 0.139±0.002 nm. Further, in a case where the electrically conductive substrate is a titanium mesh, the XRD has, in order from the low angle side, at least diffraction lines which provide d representing the interplanar spacings of 0.40±0.01 nm, 0.256±0.005 nm, 0.244±0.004 nm, 0.235±0.004 nm, 0.225±0.004 nm, 0.213±0.004 nm, 0.164±0.002 nm and 0.139±0.002 nm.
The manganese oxide composite electrode material of the present invention may be obtained by electrodepositing a manganese oxide in the above sulfuric acid/manganese sulfate mixed solution, on the electrically conductive substrate represented by carbon paper or a titanium mesh, instead of the electrode substrate of the pure titanium plate. In such a case, electrodeposition of the manganese oxide is conducted preferably so that the amount of the covering manganese oxide per geometrical area of the electrically conductive substrate is within the above preferred range.
The electrically conductive substrate is preferably one, for example, obtained by forming or sintering electrically conductive fibers of e. g. carbon or titanium having a diameter of at most 100 μm, into a plate shape having a thickness of at most 1 mm. The porosity of the electrically conductive substrate is, for example, preferably at least 40%, more preferably from 50 to 90%. The porosity is defined by the volume of spaces without electrically conductive fibers and the like in the volume of the electrically conductive substrate.
The electrically conductive substrate is preferably subjected to an acid treatment with hydrochloric acid, sulfuric acid, nitric acid, oxalic acid or the like before electrodepositing the manganese oxide, so that a passive coating of the substrate surface is removed or the substrate surface is hydrophilized.
Further, it is preferred to immerse the electrically conductive substrate in e.g. a dispersion of a fluororesin to impart water repellency, for the purpose of controlling the electrodeposition position of the manganese oxide on the electrically conductive substrate, or to impart gas diffusion property which is important when practically used as an electrode in water electrolysis.
As conditions when the manganese oxide of the present invention is electrodeposited on the electrically conductive substrate, for example, as mentioned above, electrodeposition may be conducted selecting the respective ranges of the sulfuric acid concentration and the manganese concentration of the sulfuric acid/manganese sulfate mixed solution, the electrolysis current density, the electrolysis temperature and the like, for an electrolysis time of from 5 minutes to 120 minutes, and washing with water and drying are conducted after completion of the electrolysis, whereby the manganese oxide composite electrode material of the present invention is obtained.
By shielding one side of the electrically conductive substrate with e.g. a resin film, at the time of electrodeposition of the manganese oxide, an electrodeposited film of the manganese oxide is preferentially coated only on one side, whereas manganese oxide is not substantially electrodeposited on the other side, so that manganese oxide can be made unevenly electrodeposited on purpose.
Further, it is effective to apply, as the post treatment to the manganese oxide composite electrode material of the present invention, either one of acid immersion and heating or both of acid immersion and heating. The post treatment by acid immersion is carried out, for example, by immersing the manganese oxide composite electrode material in a 0.5 mol/L to 5 mol/L sulfuric acid for from 30 minutes to 2 hours, followed by washing with water and drying. Further, the post treatment by heating is carried out, for example, by heating the manganese oxide composite electrode in air or nitrogen atmosphere at from 180° C. to 300° C. for from 30 minutes to 2 hours.
The effect by such post treatment on the manganese oxide composite material has not yet been clearly understood, and is estimated to increase the adhesion between the manganese oxide and the electrically conductive fibers or to cause a change in the crystal structure or the crystallinity of the manganese oxide catalyst.
By laminating the manganese oxide composite electrode material of the present invention, a polymer electrolyte membrane and an electrode having a hydrogen evolution catalyst, a laminate is obtained. The polymer electrolyte membrane may, for example, be a fluororesin type cation exchange membrane, and the hydrogen evolution catalyst may, for example, be platinum fine particles. In the present invention, by the manganese oxide composite electrode material of the present invention, a water electrolysis apparatus can be constituted, and by water electrolysis using the manganese oxide composite electrode material, hydrogen can be produced.
Now, the present invention will be described in further detail with reference to Examples and Comparative Examples, but it should be understood that the present invention is by no means restricted thereto.
0.200 g of a manganese oxide is weighed in an Erlenmeyer flask, 10 mL of a 0.3 M/L oxalic acid aqueous solution and 20 mL of (1+1) sulfuric acid aqueous solution are added, and heated to 70° C. for dissolution. While keeping the mixture to be from 55 to 60° C., titration is conducted with a 0.1N potassium permanganate solution, and the liquid amount at the end point is obtained. The amount of the 0.1N potassium permanganate solution required for a blank test is obtained, and the tetravalent manganese oxide purity is calculated in accordance with the following formula 7.
Tetravalent manganese oxide purity (%)=(((B−A)×0.4347)/S)×100 Formula 7
A: liquid amount (mL) of 0.1N potassium permanganate solution required for blank test
B: liquid amount (mL) of 0.1N potassium permanganate solution required for titration
S: amount (g) of manganese oxide collected
Then, by ICP method, the total Mn purity (%) of the manganese oxide is obtained, and the metallic valence is determined from the tetravalent manganese oxide purity (%) in accordance with the following formula 8.
Metallic valence=(tetravalent manganese purity (%)×63.19)/total Mn purity (%)×2 Formula 8
Measurement of primary particle sizes of the manganese oxide, and the manganese oxide and carbon in the manganese oxide/carbon mixture, was conducted by microscope method by observing a scanning electron microscope (SEM) image. As the measurement apparatus, a field emission scanning electron microscope (S-4800, manufactured by Hitachi High-Technologies Corporation) was used.
0.5 g of the manganese oxide was poured into 50 mL of pure water and ultrasonic irradiation was applied for 10 seconds to prepare a dispersion slurry, the predetermined amount of which was charged into a measurement apparatus (microtrac HRA, manufactured by HONEYWELL), and the particle size distribution was measured by laser diffraction method. From the obtained particle size distribution data, the average secondary particle size (D50) of 50% manganese oxide particles was obtained. For measurement, the refractive index of pure water of 1.33 and the refractive index of manganese dioxide of 2.20 were employed.
The BET specific surface areas of manganese dioxide and a manganese oxide/manganese dioxide mixture were measured by nitrogen adsorption by BET one point method. As the measurement apparatus, gas adsorption specific surface area measurement apparatus (FlowSorb III, manufactured by Shimadzu Corporation) was used. Prior to the measurement, the measurement sample was heated at 150° C. for 40 minutes for deaeration.
The alkali potential was measured in a 40 wt % KOH aqueous solution as follows.
To 3 g of the manganese oxide, 0.9 g of graphite (KS-44) as an electrically conductive agent was added to obtain a mixed powder, to which 4 mL of a 40% KOH aqueous solution was added to prepare a mixture slurry of the manganese oxide, the graphite and the KOH aqueous solution. The potential of the mixture slurry was measured on the basis of a mercury/mercury oxide reference electrode, whereby the alkali potential of the manganese oxide was obtained.
Using an x-ray diffraction apparatus (manufactured by Rigaku Corporation, Ultima IV), diffraction lines of the manganese oxide composite electrode material were measured. As a light source, CuKα rays (λ=1.5405 Å) were employed, the measurement mode was step scanning, the scanning speed was 4.0000° per minute, the step width was 0.02°, and the measurement range was 5° to 80° as 2θ. The diffraction lines of the obtained XRD pattern were subjected to Gaussian treatment to obtain 2θ at the peak top, and d values were obtained in accordance with Bragg' equation (nλ=2d sin θ, n=1) and taken as the interplanar spacings.
The manganese oxide was made to be supported on a fluorine-doped tin oxide electrode (FTO electrode) (manufactured by SPD Laboratory, Inc.) as follows. 40 mg of the manganese oxide was dispersed in 100 mL of ultrapure water, and the obtained dispersion was sprayed on the FTO electrode by an automatic spray gun (ST-6, manufactured by FUSO SEIKI Co., Ltd.) to prepare an electrode. The FTO electrode was put on a hotplate heated to 200° C. so that sprayed dispersion would not formed into droplets on the substrate.
To evaluate the water oxidation catalytic performance of the manganese oxide, linear sweep voltammetry was conducted. In the experiment, three-electrode system was employed, using the FTO electrode having the catalyst supported as the working electrode, a platinum wire as the counter electrode and a Ag/Ag Cl (saturated KCl) electrode (+0.199V vs. SHE) as the reference electrode. For the electrolytic solution, a 0.5M Na2SO4 aqueous solution prepared with sodium sulfate, adjusted to have pH −0.2 with sulfuric acid was used.
In this measurement, an electrochemical cell was used, the potential was swept from the negative direction. The electrochemical cell had the working electrode on the bottom and the counter and reference electrodes inserted from above. The distance between the working electrode and the reference electrode was 2 mm. The potential sweep rate was 10 mV/s so that the potential at which the current started to increase (onset potential) would readily be distinguished.
Using the above evaluation apparatus under the above conditions, the current density at a potential of 1.7 V vs. RHE and the overvoltage (polarization from the equilibrium potential) at 0.5 mA/cm2 were measured.
The manganese oxide/carbon mixture catalyst was made to be supported on a rotating disk electrode (RDE electrode) as follows. An ethanol slurry of the manganese oxide/carbon mixture in an amount containing 1 mg of the manganese oxide, and 6.17 μL of a 10 wt % Nafion dispersion (DE1021) were mixed, and ultrapure water was added to make the total amount to be 500 μL thereby to prepare an electrically conductive catalyst ink. 10 μL of the electrically conductive catalyst was dropped on a glassy carbon RDE electrode (diameter 5 mm) and applied, and air-dried to evaporate ethanol thereby to make the manganese oxide/carbon mixture catalyst be supported on the glassy carbon RDE electrode.
For comparison, the catalyst was supported in such a manner that 1 mg of the catalyst, 4 mg of electrically conductive carbon black (Vulcan XC-72, manufactured by Cabot Corporation), and 500 μL of diluted Nafion dispersion (mixture of 10 wt % Nafion dispersion (DE1021), ethanol and water in a volume ratio of 1:20:60) were mixed to prepare an electrically conductive catalyst ink, and 10 μL thereof was dropped and applied, and air-dried.
To evaluate water oxidation catalytic performance of the manganese oxide/carbon mixture catalyst, linear sweep voltammetry was conducted. As the experimental system, three-electrode system was employed, using the glassy carbon RDE electrode having the catalyst supported as the working electrode, a platinum wire as the counter electrode and a Ag/AgCl (saturated KCl) electrode (+0.199 V vs. SHE) as the reference electrode. For the electrolytic solution, a 0.5M Na2SO4 aqueous solution prepared with sodium sulfate, adjusted to have pH 7.5 with a 0.1M NaOH aqueous solution was used. In order to prevent accumulation of proton as a product of the water electrolysis, the electrode was rotated at 1,600 rpm during the measurement.
In this measurement, an electrochemical cell was used, and the potential was swept from the negative direction. The electrochemical cell had the working, counter and reference electrodes inserted from above. The potential sweep rate was 5 mV/s so that the potential at which the current started to increase (onset potential) would readily be distinguished.
Using the above evaluation apparatus under the above conditions, the current density at a potential of 1.5 V vs. SHE and the overvoltage (polarization from the equilibrium potential) at 1 mA/cm2 were measured.
To evaluate the water oxidation catalytic performance of the manganese oxide/carbon mixture catalyst, Tafel plot was measured. The vertical axis of the Tafel plot indicates the logarithm of the current density, and the vertical axis indicates the potential. The slope of the Tafel plot indicates how the potential should be increased to make the current density 10 times, and is an index of activity independent of the amount and the surface area of the catalyst. Plotting the value of the current when stabilized by conducting electrolysis at a constant potential, was repeatedly carried out while changing the potential stepwise, to prepare the Tafel plot. In the experiment, in the same manner as linear sweep voltammetry, three-electrode system was employed, using the glassy carbon RDE electrode having the manganese oxide/carbon mixture catalyst supported as the working electrode, a platinum wire as the counter electrode and a Ag/AgCl (saturated KCl) electrode (+0.199 V vs. SHE) as the reference electrode. For the electrolytic solution, a 0.5M Na2SO4 aqueous solution prepared with sodium sulfate, adjusted to have pH 7.5 with 0.1M NaOH aqueous solution was used. In order to prevent accumulation of proton as a product of the water electrolysis, the electrode was rotated at 1,600 rpm during the measurement.
Constitution of a PEM type electrolytic cell using the manganese oxide/carbon mixture catalyst was carried out as follows. An electrically conductive catalyst ink was prepared in the same manner as in the case of one to be supported on the RDE electrode. 500 μL of the electrically conductive catalyst ink was applied on carbon paper (EC-TP1-060T, ElectroChem Inc.) (shape: 4 cm×4 cm) and air-dried to evaporate ethanol, whereby the catalyst was made to be supported on the carbon paper to prepare the working electrode.
As the catalyst for the counter electrode, carbon supported 20 wt % platinum catalyst (20% Platinum on Vulcan XC-72, Item #PTC20-1, Fuel Cell Earth) was used. In the same manner as preparation of the working electrode, the counter electrode was prepared by preparing an electrically conductive catalyst ink, application to carbon paper and air-drying. As a polymer electrolyte membrane, Nafion 117 was used. The polymer electrolyte membrane was washed and protonated (pre-treatment) by being boiled in 3% hydrogen peroxide aqueous solution, pure water, a 1M sulfuric acid aqueous solution and then pure water each for one hour. Then, the polymer electrolyte membrane was sandwiched between the catalyst-coated surfaces of the working electrode and the counter electrode and hot-pressed using a hot pressing machine (A-010D, manufactured by FC-R&D) at 135° C. with a clamping force of 600 kg for 10 minutes to prepare a membrane/electrolyte assembly (MEA). The MEA was attached to a casing of a PEM type electrolytic cell (3036, manufactured by FC-R&D).
To evaluate the water oxidation catalytic performance of the manganese oxide/carbon mixture catalyst in an actual device, a current-voltage curve was measured using a PEM type electrolytic cell constituted by using the mixture catalyst. In this measurement, two-electrode system using only the working electrode and the counter electrode was employed, and the voltage applied was gradually increased to measure the current-voltage curve. Pure water was supplied to the PEM type electrolytic cell. The voltage increase rate was 5 mV/s so that the voltage at which the current started to increase would readily be distinguished.
Constitution of a PEM type electrolytic cell using an electrode material of an electrically conductive substrate having the manganese oxide catalyst deposited was carried out as follows. The electrode material (shape: 3 cm×3 cm (Examples 10 to 12), shape: 2 cm×2 cm (Examples 13 to 20)) was used as the working electrode, and the counter electrode was prepared using carbon supported 20 wt % platinum catalyst (20% Platinum on Vulcan XC-72, Item #PTC20-1, Fuel Cell Earth) as the catalyst for the counter electrode, by preparing an electrically conductive catalyst ink, application to carbon paper and air-drying. As a polymer electrolyte membrane, Nafion 117 was used. The polymer electrolyte membrane was washed and protonated (pre-treatment) by being boiled in 3% hydrogen peroxide aqueous solution, pure water, a 1M sulfuric acid aqueous solution and then pure water each for one hour. Then, the polymer electrolyte membrane was sandwiched between the catalyst-coated surfaces of the working electrode and the counter electrode and hot-pressed using a hot pressing machine (A-010D, manufactured by FC-R&D) at 135° C. with a clamping force of 600 kg for 10 minutes to prepare a membrane/electrolyte assembly (MEA). The MEA had adhesion improved even at the time of electrolysis by means of two sheets of stainless mesh (#100), and was attached to a casing of a PEM type electrolytic cell (3036, manufactured by FC-R&D).
To evaluate the water oxidation catalytic performance in an actual device, a current-voltage curve was measured at room temperature using a PEM type electrolytic cell constituted by using an electrode material of an electrically conductive substrate having the manganese oxide catalyst deposited. In this measurement, two-electrode system using only the working electrode and the counter electrode was employed, and the voltage applied was gradually increased to measure the current-voltage curve. Pure water was supplied to the PEM type electrolytic cell. The voltage increase rate was 5 mV/s so that the voltage at which the current started to increase would be readily be distinguished.
A manganese sulfate aqueous solution having a manganese concentration of 95 g/L was stirred, and a 1.05 mol/L sodium hydroxide aqueous solution was added while blowing air to obtain a manganese sulfate aqueous solution containing a manganese oxide. The obtained manganese oxide was single phase trimanganese tetroxide (Mn3O4). The XRD pattern of the obtained trimanganese tetroxide (Mn3O4) is shown in
45 mg of the obtained trimanganese tetroxide (Mn3O4) was immersed in a beaker in which 240 g of a 3 mol/L sulfuric acid solution was put and stirred at 60° C. for 24 hours to obtain a slurry containing black precipitates. An operation of subjecting the slurry to filtration through a membrane filter, putting the residue in a beaker in which 500 mL of pure water was put, and washing the solid with water for 1 hour, was repeated twice. Then, the slurry was subjected to filtration through a membrane filter again, the residue was put again in a beaker in which 500 mL of pure water was put, and the slurry was neutralized with a 1 mol/L NaOH solution until the slurry pH became 5.9, followed by filtration and drying to obtain a manganese oxide. The obtained manganese oxide showed an XRD pattern attributable to γ manganese oxide (γMnO2). Of the manganese oxide, physical properties are shown in Table 1, and the XRD pattern is shown in
Using the manganese oxide, properties of the oxygen evolution electrode catalyst were evaluated. The results of evaluation of the properties are also shown in Table 1 and
In an electrolytic cell in which a sulfuric acid/manganese sulfate mixed solution was put, electrolysis was conducted while a supplemental manganese sulfate solution having a manganese ion concentration of 47 g/L was continuously added, to electrodeposit a manganese oxide on a titanium anode. During the electrolysis, the electrolysis current density was 0.7 A/dm2, and the electrolysis temperature was 96° C. The supplemental manganese sulfate solution was added so that the sulfuric acid concentration in the electrolytic cell would be 32 g/L, the electrolysis was conducted for 10 days, and the electrolysis voltage at the time of completion of the electrolysis was 2.3 V.
The obtained electrodeposit was separated from the electrode, ground to have an average secondary particle size of 40 μm, and washed with water and neutralized. The manganese oxide was flash-dried to obtain a manganese oxide having an average secondary particle size of 40 μm and at the same time, a submicron-level manganese oxide fine powder formed as by-product by overgrinding at the time of grinding was recovered by a bag filter of a dust collector at the time of flash-drying. The manganese oxide fine powder had an average secondary particle size of 0.6 μm, and had γ crystal phase. Of the manganese oxide fine powder, physical properties are shown in Table 1, the secondary particle size distribution is shown in
Manganese sulfate and ammonium sulfate were dissolved in water to obtain an ammonium ion-containing sulfuric acid/manganese sulfate mixed solution having a manganese ion concentration of 27.6 g/L and an ammonium ion concentration of 54 g/L.
Using the ammonium ion-containing sulfuric acid/manganese sulfate mixed solution as the electrolytic solution, electrolysis was conducted while an ammonium sulfate-containing manganese sulfate solution was continuously added so that the ammonium ion concentration and the sulfuric acid concentration in the electrolytic solution would be constant at 54 g/L and 30 g/L, respectively, to obtain an electrodeposit. The electrolysis current density was 0.8 A/dm2, the electrolysis temperature was 96° C., and the electrolysis time was 25 hours.
The molar ratio of the ammonium ion concentration to the manganese ion concentration in the electrolytic solution (NH4+/Mn2+) was 5.98, and the electrolysis voltage at the time of completion of the electrolysis was 1.93 V.
The obtained electrodeposit was separated from the electrode, ground, washed with water and neutralized, and dried to obtain a manganese oxide having an average secondary particle size of 22 μm.
Of the manganese oxide, physical properties are shown in Table 1, and the XRD pattern is shown in
Physical properties and results of evaluation of properties of the trimanganese tetroxide (Mn3O4) used as the raw material for producing the manganese oxide in Example 1 are shown in Table 1 and
Physical properties and results of evaluation of properties of the manganese oxide having an average secondary particle size of 40 μm obtained at the time of flash drying in Example 2 are shown in Table 1 and
The manganese oxide having an average secondary particle size of 40 μm obtained at the time of flash drying in Example 2 was further subjected to calcining treatment at 420° C. for 36 hours. The obtained manganese oxide showed an XRD pattern attributable to β-phase manganese oxide (βMnO2). Of the manganese oxide, physical properties and results of evaluation of properties are shown in Table 1 and
The oxygen evolution electrode catalyst was evaluated using commercial iridium oxide catalyst (manufactured by Wako Pure Chemical Industries, Ltd.), and the results of evaluation of the properties are shown in Table 1 and
As shown in Table 1 and
0.25 g of the manganese oxide fine powder having an average secondary particle size of 0.6 μm obtained in Example 2 and 4.75 g of electrically conductive carbon (Vulcan XC-72) were weighed, and ground and mixed in an agate mortar. The ground mixture was put in a container in which 50 mL of ethanol and zirconia balls having a diameter of 0.3 mm were put, and rotated at 40 rpm for 24 hours to conduct ball mill mixing. The obtained slurry was subjected to sieving with a mesh size of 150 μm to remove the zirconia balls, whereby a manganese oxide/carbon mixture was recovered in the form of an ethanol slurry. To the recovered ethanol slurry, Nafion dispersion and the like were added to prepare an electrode, and properties of the oxygen evolution electrode catalyst were evaluated.
The ethanol slurry of the manganese oxide/carbon mixture was subjected to chemical analysis, whereupon the proportion of the manganese oxide to the total of the manganese oxide and carbon was 4.4 wt %. The XRD pattern of a mixed powder obtained by evaporating ethanol from the ethanol slurry of the manganese oxide/carbon mixture is shown in
Ethanol slurries of a manganese oxide/carbon mixture having a proportion of the manganese oxide to the total of the manganese oxide and carbon of 9.9 wt %, 35.5 wt %, 19.7 wt % and 16.7 wt % were obtained in the same manner as in Example 4 except for the amount of the manganese oxide fine powder having an average secondary particle size of 0.6 μm and the electrically conductive carbon (Vulcan XC-72) charged. Electrodes were prepared in the same manner as in Example 4 except that the respective slurries were used, and properties of the oxygen evolution electrode catalysts were evaluated. The XRD pattern of a mixed pattern obtained by evaporating ethanol from the ethanol slurry of the manganese oxide/carbon mixture obtained in Example 8 is shown in
A mixture containing only electrically conductive carbon black (Vulcan XC-72) and a diluted Nafion dispersion, without containing manganese oxide, was made to be supported on an glassy carbon RDE electrode, and general evaluation of oxygen evolution electrode catalyst properties was conducted, and the results are shown in Table 2,
An electrically conductive catalyst ink prepared by mixing commercial iridium oxide catalyst (manufactured by Wako Pure Chemical Industries, Ltd.), electrically conductive carbon black (Vulcan XC-72) and a diluted Nafion dispersion, was made to be supported on a glassy carbon RDE electrode, evaluation of oxygen evolution electrode catalyst was conducted, and the properties are shown in Table 2,
An electrically conductive catalyst ink prepared by mixing carbon supported 20 wt % iridium catalyst (20 wt % Iridium on Vulcan XC-72, Item #P40A200, Premetek) and a diluted Nafion dispersion was made to be supported on a glassy carbon RDE electrode, evaluation of oxygen evolution electrode catalyst was conducted, and the properties are shown in
An electrically conductive catalyst ink prepared by mixing carbon supported 20 wt % platinum catalyst (20 wt % Platinum on Vulcan XC-72, Item #PTC20-1, Fuel Cell Earth) and a diluted Nafion dispersion was made to be supported on a glassy carbon RDE electrode, evaluation of oxygen evolution electrode catalyst was conducted, and the properties are shown in
As shown in Table 2 and
A PEM type electrolytic cell was constituted by using the ethanol slurry of the manganese oxide/carbon mixture used in Example 5, and evaluation of oxygen evolution electrode catalyst properties was conducted. The results are shown in
A PEM type electrolytic cell (evaluation 3) was constituted by using a mixture containing only electrically conductive carbon black (Vulcan XC-72) and a diluted Nafion dispersion, without containing manganese oxide, and evaluation of oxygen evolution electrode catalyst properties was conducted. The results are shown in
A PEM type electrolytic cell (evaluation 3) was constituted by using an electrically conductive catalyst ink prepared by mixing carbon supported 20 wt % iridium catalyst (20% Iridium on Vulcan XC-72, Item #P40A200, Premetek) and a diluted Nafion dispersion, and evaluation of oxygen evolution electrode catalyst properties was conducted. The results are shown in
A PEM type electrolytic cell (evaluation 3) was constituted by using an electrically conductive catalyst ink prepared by mixing carbon supported 20 wt % platinum catalyst (20% Platinum on Vulcan XC-72, Item #PTC20-1, Fuel Cell Earth) and a diluted Nafion dispersion, and evaluation of oxygen evolution electrode catalyst properties was conducted. The results are shown in
As shown in
Electrolysis was conducted for 15 minutes under the same conditions as in Example 2 except that the titanium anode plate was changed to carbon paper (TGP-H-060, manufactured by Toray Industries, Inc.) as an electrically conductive substrate and that the temperature was 94° C. After completion of the electrolysis, the carbon paper having a manganese oxide electrodeposited thereon was washed with water, air-dried and cut into a size of 3 cm×3 cm to prepare an electrode material. As shown in the SEM photograph (
Electrolysis was conducted under the same conditions as in Example 10 except that the electrolysis time was 3 minutes. After completion of the electrolysis, the carbon paper having a manganese oxide electrodeposited thereon was washed with water, air-dried and cut into a size of 3 cm×3 cm to prepare an electrode material. As shown in the SEM photograph (
Electrolysis was conducted under the same conditions as in Example 10 except that the electrically conductive substrate was changed to a titanium mesh (ST/Ti/20/300/67, Nikkotechno). After completion of the electrolysis, the titanium mesh having a manganese oxide electrodeposited thereon was washed with water, air-dried and cut into a size of 3 cm×3 cm to prepare an electrode material. Using the electrode material, in accordance with <Evaluation 4 of oxygen evolution electrode catalyst properties>, a PEM type electrolytic cell was constituted, and evaluation of oxygen evolution electrode catalyst properties was conducted. The results are shown in Table 3 and
A PEM type electrolytic cell was constituted by using an electrically conductive ink prepared by mixing carbon supported 20 wt % platinum catalyst (20 wt % Platinum on Vulcan XC-72, Item #PTC20-1, Fuel Cell Earth) and a diluted Nafion dispersion, in accordance with <Evaluation 4 of oxygen evolution electrode catalyst properties>, and evaluation of oxygen evolution electrode catalyst properties was conducted. The results are shown in Table 3 and
Electrolysis was conducted for 14 minutes under the same conditions as in Example 10 except that the temperature was 93° C. After completion of the electrolysis, the carbon paper having a manganese oxide electrodeposited thereon was washed with water, air-dried and cut into a size of 2 cm×2 cm to prepare an electrode material. The XRD pattern of the electrode material is shown in
Electrolysis was conducted for 29 minutes under the same conditions as in Example 13 except that the temperature was 94° C. After completion of the electrolysis, the carbon paper having a manganese oxide electrodeposited thereon was washed with water, air-dried and cut into a size of 2 cm×2 cm to prepare an electrode material. The XRD pattern of the electrode material is shown in
Electrolysis was conducted for 15 minutes under the same conditions as in Example 13 except that one side of carbon paper (TGP-H-060, manufactured by Toray Industries, Inc.) as the electrically conductive substrate was covered with a silicon film and that the temperature was 94° C. After completion of the electrolysis, electrodeposition only on one side was visually observed. The carbon paper having a manganese oxide electrodeposited thereon was washed with water, air-dried and cut into a size of 2 cm×2 cm to prepare an electrode material. The SEM photograph and EPMA photographs of the cut cross section of the electrode material are shown in
Electrolysis was conducted for 15 minutes under the same conditions as in Example 13 except that the carbon paper (TGP-H-060, manufactured by Toray Industries, Inc.) as the electrically conductive substrate was changed to water repellent carbon paper (TGP-H-060H, manufactured by Toray Industries, Inc.) having water repellent treatment applied thereto, that one side of the electrically conductive substrate was covered with a silicon film, and that the temperature was 93.5° C. After completion of the electrolysis, electrodeposition only on one side was visually observed. The carbon paper having a manganese oxide electrodeposited thereon was washed with water, air-dried and cut into a size of 2 cm×2 cm to prepare an electrode material. Using the electrode material, in accordance with <Evaluation 4 of oxygen evolution electrode catalyst properties>, a PEM type electrolytic cell was constituted, and evaluation of oxygen evolution electrode catalyst properties was conducted. The results are shown in Table 4 and
The electrode material of 2 cm×2 cm prepared in the same manner as in Example 13 was further subjected to, as the post-treatment, heat treatment in the air atmosphere at 230° C. for 2 hours, and washed with water and air-dried to prepare an electrode material. Using the electrode material, in accordance with <Evaluation 4 of oxygen evolution electrode catalyst properties>, a PEM type electrolytic cell was constituted, and evaluation of oxygen evolution electrode catalyst properties was conducted. The results are shown in Table 4 and
The electrode material of 2 cm×2 cm prepared in the same manner as in Example 13 was further subjected to, as the post-treatment, heat treatment in the air atmosphere at 230° C. for 2 hours, and immersed in a 1 mol/L sulfuric acid solution for one hour, washed with water and air-dried to prepare an electrode material. Using the electrode material, in accordance with <Evaluation 4 of oxygen evolution electrode catalyst properties>, a PEM type electrolytic cell was constituted, and evaluation of oxygen evolution electrode catalyst properties was conducted. The results are shown in Table 4 and
Electrolysis was conducted under the same conditions as in Example 13 except that the electrically conductive substrate was changed to a titanium mesh (ST/Ti/20/300/67, Nikkotechno) and that the temperature was 94° C. After completion of the electrolysis, the titanium mesh having a manganese oxide electrodeposited thereon was washed with water, air-dried and cut into a size of 2 cm×2 cm to prepare an electrode material. The XRD pattern of the electrode material is shown in
The electrode material of 2 cm×2 cm prepared in the same manner as in Example 19 was further subjected to, as the post treatment, heat treatment in the air atmosphere at 230° C. for 2 hours, and washed with water and air-dried to prepare an electrode material. Using the electrode material, in accordance with <Evaluation 4 of oxygen evolution electrode catalyst properties>, a PEM type electrolytic cell was constituted, and evaluation of oxygen evolution electrode catalyst properties was conducted. The results are shown in Table 4 and
Electrolysis was conducted for 30 minutes under the same conditions as in Example 19 except that the temperature was 93.5° C. After completion of the electrolysis, the titanium mesh having a manganese oxide electrodeposited thereon was washed with water, air-dried and cut into a size of 2 cm×2 cm to prepare an electrode material. The XRD pattern of the electrode material is shown in
As shown in Tables 3 and 4 and
The manganese oxide and the manganese oxide/carbon mixture of the present invention have high oxygen evolution electrode catalytic activity comparable to conventional noble metal type catalysts and accordingly when used as an anode catalyst for oxygen evolution in industrial water electrolysis conducted under alkaline or neutral conditions or in water electrolysis using a PEM type electrolytic cell, they are capable of producing hydrogen and oxygen at very low production costs.
Further, by adding carbon dioxide to the reaction system, carbon dioxide is reduced at the cathode, whereby hydrocarbon compounds (such as formic acid, formaldehyde, methanol, methane, ethane and propane) may be produced.
The entire disclosures of Japanese Patent Application No. 2017-239743 filed on Dec. 14, 2017 and Japanese Patent Application No. 2018-124708 filed on Jun. 29, 2018, including specifications, claims, drawings and summaries are incorporated herein by reference in their entireties.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2017-239743 | Dec 2017 | JP | national |
| 2018-124708 | Jun 2018 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2018/045681 | 12/12/2018 | WO | 00 |
