Embodiments described herein generally relate to a photoelectrochemical reaction device.
In recent years, there has been concern about the depletion of fossil fuel such as petroleum and coal, and renewable energy that can be sustainably utilized is increasingly expected. As one of the renewable energies, a solar cell and heat power generation which use sunlight are under development. The solar cell has problems that it requires cost for storage batteries used when the generated power (electricity) is stored and a loss occurs at the time of the power storage. A technique of directly converting the sunlight to a chemical substance (chemical energy) such as hydrogen (H2), carbon monoxide (CO), methanol (CH3OH), or formic acid (HCOOH) instead of converting the sunlight to electricity has been drawing attention. Storing the chemical substance converted from the sunlight in a cylinder or a tank has advantages that it requires less cost for storing the energy and further the storage loss is smaller, as compared with storing electricity converted from the sunlight in the storage battery.
As a device that converts sunlight energy to chemical energy, there are known photoelectrochemical reaction devices in which a photovoltaic unit and an electrolytic unit are integrated together. The photoelectrochemical reaction devices are roughly classified into a cell-integrated type device in which a photovoltaic cell is not immersed in an electrolytic solution but integrally arranged on an electrolytic bath, and a cell-immersed type device in which a photovoltaic cell is immersed in an electrolytic solution. In the photoelectrochemical reaction device of the cell-integrated type, when a plurality of photovoltaic cells are used for enhancing the electromotive force, it is conceivable to connect the plurality of photovoltaic cells connected in parallel, to electrodes (anode and cathode). In this case, when part of the plural photovoltaic cells becomes shaded due to could or a failure occurs in part of the plural photovoltaic cells, not only electromotive force decreases correspondingly to the portion of the failed cell but also the conversion efficiency of the whole device decreases by the effect of the cell decreased in parallel resistance due to the failure.
According to one embodiment, there is provided a photoelectrochemical reaction device including: a first photovoltaic cell including a first electrode, a second electrode, and a photovoltaic layer provided between the first electrode and the second electrode; a second photovoltaic cell including a first electrode, a second electrode, and a photovoltaic layer provided between the first electrode and the second electrode; a reaction electrode pair including at least one third electrode and two divided fourth electrodes, and one of the third and fourth electrodes causing an oxidation reaction, and the other of the third and fourth electrodes causing a reduction reaction; a first connecting member electrically connecting the first electrodes of the first and second photovoltaic cells to the third electrode of the reaction electrode pair; a second connecting member electrically connecting the second electrode of the first photovoltaic cell to one of the two fourth electrodes of the reaction electrode pair; a third connecting member electrically connecting the second electrode of the second photovoltaic cell to the other of the two fourth electrodes of the reaction electrode pair; and an electrolytic bath storing a first electrolytic solution in which at least the third electrode is immersed and a second electrolytic solution in which at least the fourth electrodes are immersed.
Hereinafter, photoelectrochemical reaction devices of embodiments will be described with reference to the drawings.
Each of the first and second reaction electrode pairs 3A, 3B includes a third electrode 41 and a fourth electrode 42 arranged to be opposed to the third electrode 41. The first and second reaction electrode pairs 3A, 3B are arranged inside the electrolytic bath 4. The electrolytic bath 4 includes a first storage part 52 storing a first electrolytic solution 51 in which the third electrodes 41 are immersed, a second storage part 54 storing a second electrolytic solution 53 in which the fourth electrodes 42 are immersed, and an ion migration layer (an ion migration layer also serving as a separation wall) 55 allowing ions to migrate while separating the first electrolytic solution 51 and the second electrolytic solution 53. One of the third electrode 41 and the fourth electrode 42 causes an oxidation reaction and the other of the third electrode 41 and the fourth electrode 42 causes a reduction reaction. Specifically, a photoelectromotive force generated by radiating the sunlight or the like to the photovoltaic cells 2A, 2B causes the oxidation and reduction reactions by the reaction electrode pairs 3A, 3B.
As illustrated in
Though the photoelectrochemical reaction device 1 having a combination of the first photovoltaic cell 2A and the first reaction electrode pair 3A and a combination of the second photovoltaic cell 2B and the second reaction electrode pair 3B is illustrated in
The configuration of the photoelectrochemical reaction device 1 of the first embodiment will be described in detail. The photovoltaic cell 2 has a flat plate shape spreading in a first direction and a second direction perpendicular to the first direction, and is composed of, for example, the second electrode 21 as a substrate, and the photovoltaic layer 31 and the first electrode 11 which are formed in order on the second electrode 21. Here, a description will be given on assumption that a light irradiated side is a front surface (upper surface) and a side opposite the light irradiated side is a rear surface (lower surface). Concrete structural examples of the photovoltaic cell 2 will be described with reference to
In the photovoltaic cell 201 illustrated in
The photovoltaic layer 311 is formed on the second electrode 21. The photovoltaic layer 311 is composed of a reflective layer 32, a first photovoltaic layer 33, a second photovoltaic layer 34, and a third photovoltaic layer 35. The reflective layer 32 is formed on the second electrode 21 and has a first reflective layer 32a and a second reflective layer 32b which are formed in order from a lower side. As the first reflective layer 32a, metal such as Ag, Au, Al, or Cu, an alloy containing at least one of these metals, or the like that has light reflectivity and electrical conductivity is used. The second reflective layer 32b is provided in order to adjust an optical distance to enhance light reflectivity. The second reflective layer 32b is joined to a later-described n-type semiconductor layer of the photovoltaic layer 31 and therefore is preferably formed of a material having a light transmitting property and capable of coming into ohmic contact with the n-type semiconductor layer. As the second reflective layer 32b, a transparent conductive oxide such as ITO (indium tin oxide), zinc oxide (ZnO), FTO (fluorine-doped tin oxide), AZO (aluminum-doped zinc oxide), or ATO (antimony-doped tin oxide) is used.
The first photovoltaic layer 33, the second photovoltaic layer 34, and the third photovoltaic layer 35 are each a solar cell using a pin junction semiconductor and their light absorption wavelengths are different. Stacking them in a planar manner makes it possible for the photovoltaic layer 311 to absorb light in a wide range of wavelength of sunlight, which makes it possible to more efficiently utilize energy of the sunlight. Since the photovoltaic layers 33, 34, 35 are connected in series, it is possible to obtain a high open-circuit voltage.
The first photovoltaic layer 33 is formed on the reflective layer 32 and has an n-type amorphous silicon (a-Si) layer 33a, an intrinsic amorphous silicon germanium (a-SiGe) layer 33b, and a p-type microcrystalline silicon (mc-Si) layer 33c in order from a lower side. The a-SiGe layer 33b is a layer that absorbs light in a long wavelength range of about 700 nm. In the first photovoltaic layer 33, charge separation is caused by energy of the light in the long wavelength range.
The second photovoltaic layer 34 is formed on the first photovoltaic layer 33 and has an n-type a-Si layer 34a, an intrinsic a-SiGe layer 34b, and a p-type mc-Si layer 34c which are formed in order from a lower side. The a-SiGe layer 34b is a layer that absorbs light in an intermediate wavelength range of about 600 nm. In the second photovoltaic layer 34, charge separation is caused by energy of the light in the intermediate wavelength range.
The third photovoltaic layer 35 is formed on the second photovoltaic layer 34 and has an n-type a-Si layer 35a, an intrinsic a-Si layer 35b, and a p-type mc-Si layer 35c which are formed in order from a lower side. The a-Si layer 35b is a layer that absorbs light in a short wavelength range of about 400 nm. In the third photovoltaic layer 35, charge separation is caused by energy of the light in the short wavelength range. In the photovoltaic layer 311, the charge separations are caused by the lights in the respective wavelength ranges. Specifically, holes are separated to a first electrode (anode) 11 side (front surface side) and electrons are separated to a second electrode (cathode) 21 side (rear surface side), so that an electromotive force is generated in the photovoltaic layer 311.
The first electrode 11 is formed on the p-type semiconductor layer (p-type me-Si layer 35c) of the photovoltaic layer 311. The first electrode 11 is preferably formed of a material capable of coming into ohmic contact with the p-type semiconductor layer. As the first electrode 11, metal such as Ag, Au, Al, or Cu, an alloy containing at least one of these metals, a transparent conductive oxide such as ITO, ZnO, FTO, AZO, or ATO, or the like is used. The first electrode 11 may have, for example, a structure in which the metal and the transparent conductive oxide are stacked, a structure in which the metal and other conductive material are compounded, a structure in which the transparent conductive oxide and other conductive material are compounded, or the like.
In the photovoltaic cell (the photoelectrochemical cell using the silicon-based solar cell) 201 illustrated in
In order to enhance electrical conductivity while maintaining the light transmitting property, a collector electrode made of metal such as Ag, Au, or Cu, or an alloy containing at least one of these metals may be provided on at least part of the first electrode 11 on the light irradiated side. The collector electrode has a shape transmitting the light, and examples of its concrete shape are a liner shape, a lattice shape, a honeycomb shape, and so on. In order to maintain the light transmitting property, an area of the collector electrode is preferably 30% or less of an area of the first electrode 11, and more preferably 10% or less thereof.
In
Next, the photovoltaic cell (the photoelectrochemical cell using the compound semiconductor-based solar cell as the photovoltaic layer) 202 illustrated in
The first photovoltaic layer 321 is formed on the second electrode 21 and has a p-type Ge layer 321a and an n-type Ge layer 321b which are formed in order from a lower side. On the first photovoltaic layer 321 (Ge layer 321b), the buffer layer 322 containing GaInAs and the tunnel layer 323 are formed for the purpose of lattice matching and electrical joining with GaInAs used in the second photovoltaic layer 324.
The second photovoltaic layer 324 is formed on the tunnel layer 323 and has a p-type GaInAs layer 324a and an n-type GaInAs layer 324b which are formed in order from a lower side. On the second photovoltaic layer 324 (GaInAs layer 324b), the tunnel layer 325 containing GaInP is formed for the purpose of lattice matching and electrical joining with GaInP used in the third photovoltaic layer 326. The third photovoltaic layer 326 is formed on the tunnel layer 325 and has a p-type GaInP layer 326a and an n-type GaInP layer 326b which are formed in order from a lower side.
The photovoltaic layer 312 in the photovoltaic cell (the photoelectrochemical cell using the compound semiconductor-based solar cell as the photovoltaic layer) 202 illustrated in
The first and second photovoltaic cells 2A, 2B are arranged on the electrolytic bath 4. The photovoltaic cells 2A, 2B are in close contact with the electrolytic bath 4. The photovoltaic cells 2A, 2B may be in close contact with the electrolytic bath 4 via an insulating member. The first photovoltaic cell 2A and the second photovoltaic cell 2B are preferably arranged to be as short as possible in connection distances to the first reaction electrode pair 3A and the second reaction electrode pair 3B respectively, namely, in length of connecting members 6A to 6D. The first photovoltaic cell 2A is preferably arranged to be located above the first reaction electrode pair 3A electrically connected thereto. The second photovoltaic cell 2BA is preferably arranged to be located above the second reaction electrode pair 3B electrically connected thereto.
The reaction electrode pair 3 has the third electrode 41 immersed in the first electrolytic solution 51, and the fourth electrode 42 immersed in the second electrolytic solution 53. The electrodes 41, 42 are formed of a material having electrical conductivity. As each of the electrodes 41, 42, a metal plate of Cu, Al, Au, Ti, Ni, Fe, Co, Ag, Pt, Pd, Zn, In or the like, an alloy plate containing at least one of these metals, a conductive resin plate, a semiconductor substrate of Si or Ge, or the like is used. The third electrode 41 and the fourth electrode 42 are preferably arranged to be opposed to each other for ions to rapidly migrate. The fourth electrode 42 is preferable arranged as close as possible to the third electrode 41. The distance between the electrodes 41 and 42 is preferably 500 mm or less, and more preferably 100 mm or less. To arrange the ion migration layer 55, the distance between the electrodes 41 and 42 is preferably 100 micrometer or more.
The ion migration layer 55 arranged in the electrolytic bath 4 is composed of an ion exchange membrane or the like which allows ions to migrate between the third electrode 41 and the fourth electrode 42 and can separate the first electrolytic solution 51 and the second electrolytic solution 53. As the ion exchange membrane, a cation exchange membrane such as Nafion or Flemion or an anion exchange membrane such as Neosepta or Selemion can be used. Materials other than the above are applicable as the ion migration layer 55, as long as they are materials allowing the ions to migrate between the third electrode 41 and the fourth electrode 42.
The third and fourth electrodes 41, 42 may have fine pores or slits for allowing ions to migrate. The fine pores or slits are provided to cause ions to migrate while maintaining the mechanical strength of the third and fourth electrodes 41, 42. The fine pores or slits only need to have a size enabling the ions to migrate. For example, a lower limit value of a diameter (circle-equivalent diameter) of the fine pores is preferably 0.3 nm or more. The circle-equivalent diameter is defined as ((4×area)/{pi})1/2. The shape of the fine pores is not limited to a circle and may be an ellipse, a triangle, a square, or the like. The fine pores are arranged in a square lattice form, a triangular lattice form, a random form, or the like. The fine pores or slits may be filled with an ion exchange membrane. The fine pores or slits may be filled with a glass filter or agar.
Though the state in which the third electrode 41 and the fourth electrode 42 are individually arranged in the electrolytic bath 4 is illustrated in
As illustrated in
When a solution (aqueous solution) containing H2O is used as the first electrolytic solution 51, the third electrode 41 oxidizes H2O to generate O2 and H+. Therefore, the first catalyst layer 43 is made of a material which reduces activation energy for oxidizing H2O. The first catalyst layer 43 is made of a material which lowers an overvoltage when H2O is oxidized to generate O2 and H+. Examples of such a material are binary metal oxides such as manganese oxide (Mn—O), iridium oxide (Ir—O), nickel oxide (Ni—O), cobalt oxide (Co—O), iron oxide (Fe—O), tin oxide (Sn—O), indium oxide (In—O), and ruthenium oxide (Ru—O), ternary metal oxides such as Ni—Co—O, Ni—Fe—O, La—Co—O, Ni—La—O, and Sr—Fe—O, quaternary metal oxides such as Pb—Ru—Ir—O and La—Sr—Co—O, or metal complexes such as a Ru complex and a Fe complex. A shape of the first catalyst layer 43 is not limited to a thin film shape, and may be an island, a lattice, a granular, or a wire.
When an aqueous solution containing CO2 is used as the second electrolytic solution 53, the fourth electrode 42 reduces CO2 to generate a carbon compound (CO, HCOOH, CH4, CH3OH, C2H5OH, C2H4 or the like). Therefore, the second catalyst layer 44 is made of a material which reduces activation energy for reducing CO2. The second catalyst layer 44 is made of a material which lowers an overvoltage when CO2 is reduced to generate the carbon compound. Examples of such a material are metals such as Au, Ag, Cu, Pt, Pd, Ni, and Zn, an alloy containing at least one of these metals, carbon materials such as carbon (C), graphene, CNT (carbon nanotube), fullerene, and ketjen black, and metal complexes such as a Ru complex and a Re complex.
When a solution containing H2O is used as the second electrolytic solution 53, H2 is sometimes generated by reducing H2O. In this case, the second catalyst layer 44 is made of a material which reduces activation energy for reducing H2O. The second catalyst layer 44 is made of a material which lowers an overvoltage when H2O is reduced to generate H2. Examples of such a material are metals such as Ni, Fe, Pt, Ti, Au, Ag, Zn, Pd, Ga, Mn, and Cd, an alloy containing at least one of these metals, and carbon materials such as carbon (C), graphene, CNT (carbon nanotube), fullerene, and ketjen black. A shape of the second catalyst layer 44 is not limited to a thin film shape, and may be an island shape, a lattice shape, a granular shape, or a wire shape.
When the photovoltaic cell 202 illustrated in
As a formation method of the first catalyst layer 43 and the second catalyst layer 44, a thin-film forming method such as a sputtering method or a vapor deposition method, a coating method using a solution in which the catalyst material is dispersed, an electrodeposition method, a catalyst forming method by heat treatment or electrochemical treatment of the third electrode 41 or the fourth electrode 42 itself, or the like is usable. Only one of the first catalyst layer 43 and the second catalyst layer 44 may be formed. The catalyst layers 43, 44 are arbitrarily formed and are formed according to desired oxidation and reduction reactions.
The electrolytic bath 4 includes the first storage part 52 storing the first electrolytic solution 51 and the second storage part 54 storing the second electrolytic solution 53. The third electrode 41 is arranged in the first storage part 52 storing the first electrolytic solution 51. The fourth electrode 42 is arranged in the second storage part 54 storing the second electrolytic solution 53. Of the first and second electrolytic solutions 51, 53, one is a solution containing, for example, H2O and the other is a solution containing, for example, CO2. In place of the solution containing CO2, a solution containing H2O may be used. When the photovoltaic cell 201 illustrated in
As the solution containing H2O, an aqueous solution containing an arbitrary electrolyte is used. The solution is preferably an aqueous solution that promotes the oxidation reaction of H2O. Examples of the aqueous solution containing the electrolyte are aqueous solutions containing phosphoric acid ions (PO42−), boric acid ions (BO33−), sodium ions (Na+), potassium ions (K+), calcium ions (Ca2+), lithium ions (Li+), cesium ions (Cs+), magnesium ions (Mg2+), chloride ions (Cl−), hydrogen carbonate ions (HCO3−), carbonate ions (CO32−), and so on.
The solution containing CO2 is preferably a solution having a high CO2 absorptance. Examples of the solution containing H2O are LiHCO3, NaHCO3, KHCO3, and CsHCO3 as aqueous solutions. As the solution containing CO2, alcohol such as methanol, ethanol, or acetone may be used. The solution containing H2O and the solution containing CO2 may be the same solution. Since the solution containing CO2 is preferably high in a CO2 absorption amount, a different solution from the solution containing H2O may be used as the solution containing CO2. The solution containing CO2 is desirably an electrolytic solution that reduces a reduction potential of CO2, has a high ion conductivity, and contains a CO2 absorbent which absorbs CO2.
Examples of the aforesaid electrolytic solution are an ionic liquid which is made of salts of cations such as imidazolium ions or pyridinium ions and anions such as BF4− or PF6− and which is in a liquid state in a wide temperature range, or aqueous solutions thereof. Other examples of the electrolytic solution are amine solutions of ethanolamine, imidazole, or pyridine, or aqueous solutions thereof. Amine may be any of primary amine, secondary amine, and tertiary amine. Examples of the primary amine are methylamine, ethylamine, propylamine, butylamine, pentylamine, hexylamine, and the like. Hydrocarbons of the amine may be substituted by alcohol, halogen, or the like. Examples of the amine whose hydrocarbons are substituted are methanolamine, ethanolamine, chloromethyl amine, and so on. Further, an unsaturated bond may exist. These hydrocarbons are the same in the secondary amine and the tertiary amine. Examples of the secondary amine are dimethylamine, diethylamine, dipropylamine, dibutylamine, dipentylamine, dihexylamine, dimethanolamine, diethanolamine, dipropanolamine, and so on. The substituted hydrocarbons may be different. This also applies to the tertiary amine. Examples in which the hydrocarbons are different are methylethylamine, methylpropylamine, and so on. Examples of the tertiary amine are trimethylamine, triethylamine, tripropylamine, tributylamine, trihexylamine, trimethanolamine, triethanolamine, tripropanolamine, tributanolamine, triexanolamine, methyldiethylamine, methyldipropylamine, and so on. Examples of the cations of the ionic liquid are 1-ethyl-3-methylimidazolium ions, 1-methyl-3-propylimidazolium ions, 1-butyl-3-methylimidazole ions, 1-methyl-3-pentylimidazolium ions, 1-hexyl-3-methylimidazolium ions, and so on. A second place of imidazolium ions may be substituted. Examples in which the second place of the imidazolium ions is substituted are 1-ethyl-2,3-dimethylimidazolium ions, 1-2-dimethyl-3-propylimidazolium ions, 1-butyl-2,3-dimethylimidazolium ions, 1,2-dimethyl-3-pentylimidazolium ions, 1-hexyl-2,3-dimethylimidazolium ions, and so on. Examples of pyridinium ions are methylpyridinium, ethylpyridinium, propylpyridinium, butylpyridinium, pentylpyridinium, hexylpyridinium, and so on. In both of the imidazolium ions and the pyridinium ions, an alkyl group may be substituted, or an unsaturated bond may exist. Examples of the anions are fluoride ions, chloride ions, bromide ions, iodide ions, BF4−, PF6−, CF3COO−, CF3SO3−, NO3−, SCN−, (CF3SO2)3C−, bis(trifluoromethoxysulfonyl)imide, bis(perfluoroethylsulfonyl)imide, and so on. Dipolar ions in which the cations and the anions of the ionic liquid are coupled by hydrocarbons may be used.
Next, an operation principle of the photoelectrochemical reaction device 1 will be described with reference to an electrical connection diagram in
When the light is irradiated from above the first and second photovoltaic cell 2A, 2B, the irradiating light passes through the first electrode 11 to reach the photovoltaic layer 31. When absorbing the light, the photovoltaic layer 31 generates electrons and holes which make pairs with the electrons, and separates them. Specifically, in the first photovoltaic layer 33, the second photovoltaic layer 34, and the third photovoltaic layer 35 which constitute the photovoltaic layer 31, the electrons migrate to the n-type semiconductor layer side (second electrode 21 side) due to a built-in potential, and the holes generated as the pairs with the electrons migrate to the p-type semiconductor layer side (first electrode 11 side), to thereby cause charge separation. Such charge separation generates the electromotive force in the photovoltaic layer 31.
The holes generated in the photovoltaic layer 31 in each of the first and second photovoltaic cells 2A, 2B migrate to the first electrode 11. The holes combine with electrons which are generated by the oxidation reaction caused near the third electrode 41, via the connecting member 6A, 6B and the third electrode 41. The electrons which have migrated to the second electrode 21 are used in the reduction reaction caused near the fourth electrode 42, via the connecting member 6B, 6D and the fourth electrode 42. Concretely, near the third electrode 41 in contact with the first electrolytic solution 51, a reaction of the following formula (1) occurs. Near the second electrode 42 in contact with the second electrolytic solution 53, a reaction of the following formula (2) occurs.
2H2O→4H++O2+4e− (1)
2CO2+4H++4e−→2CO+2H2O (2)
Near the third electrode 41, H2O contained in the first electrolytic solution 51 is oxidized (loses electrons), so that O2 and H+ are generated, as expressed by the formula (1). H+ generated on the third electrode 41 side migrates to the fourth electrode 42 side via the ion migration layer 55. Near the fourth electrode 42, CO2 contained in the second electrolytic solution 53 is reduced (obtains electrons) as expressed by the formula (2). Concretely, CO2 contained in the second electrolytic solution 53, H+ which has migrated to the fourth electrode 42 from the third electrode 41, and the electrons which have migrated to the fourth electrode 42 react with one another, so that CO and H2O are generated, for instance.
In this event, the photovoltaic layer 31 needs to have an open-circuit voltage equal to or larger than a potential difference between a standard oxidation-reduction potential of the oxidation reaction occurring near the third electrode 41 and a standard oxidation-reduction potential of the reduction reaction occurring near the fourth electrode 42. For example, the standard oxidation-reduction potential of the oxidation reaction in the formula (1) is 1.23 V, and the standard oxidation-reduction potential of the reduction reaction in the formula (2) is −0.1 V. Therefore, the open-circuit voltage of the photovoltaic layer 31 needs to be 1.33 V or more. The open-circuit voltage of the photovoltaic layer 31 is preferably equal to or more than the potential difference inclusive of overvoltages. Concretely, when the overvoltages of the oxidation reaction in the formula (1) and the reduction reaction in the formula (2) are both 0.2 V, the open-circuit voltage is desirably 1.73 V or more.
Near the fourth electrode 42, it is possible to cause not only the reduction reaction from CO2 to CO expressed by the formula (2) but also a reduction reaction from CO2 to formic acid (HCOOH), methane (CH4), ethylene (C2H4), methanol (CH3OH), ethanol (C2H5OH), acetic acid (CH3COOH) or the like. It is also possible to cause the reduction reaction of H2O used in the second electrolytic solution 53 to generate H2. By varying an amount of moisture (H2O) in the second electrolytic solution 53, it is possible to change a generated reduced substance of CO2. For example, it is possible to change a generation ratio of CO, HCCOH, CH4, C2H4, CH3OH, C2H5OH, CH3COOH, H2, and the like which are generated by the reduction reaction of CO2.
When generating H2 near the fourth electrode 42, the reaction of the formula (1) occurs near the third electrode 41, and the reaction of the following formula (3) occurs near the second electrode 42.
2H2O→4H++O2+4e− (1)
4H++4e−→2H2 (3)
Near the third electrode 41, H2O contained in the first electrolytic solution 51 is oxidized (loses electrons), so that O2 and H+ are generated. H+ generated on the third electrode 41 side migrates to the fourth electrode 42 side via the ion migration layer 55. Near the fourth electrode 42, H2 is reduced (obtains electrons) to generate a H2 gas as expressed by the formula (3).
In the photoelectrochemical reaction device 1 of the first embodiment, electrical connection of the photovoltaic cell 2 and the reaction electrode pair 3 as a set prevents a failure, for example, even when occurring in the first photovoltaic cell 2A, from adversely affecting the combination of the second photovoltaic cell 2B and the second reaction electrode pair 3B. Accordingly, the conversion efficiency from light energy to chemical energy by the second photovoltaic cell 2B and the second reaction electrode pair 3B can be maintained. As a concrete example of the conversion efficiency from light energy to chemical energy, currents flowing through the first reaction electrode pair 3A and the second reaction electrode pair 3B are listed in Table 1. Table 1 lists the currents flowing through the reaction electrode pairs 3A, 3B regarding the case where the first and second photovoltaic cells 2A, 2B normally operate (case 1), the case where the first photovoltaic cell 2A does not generate power (case 2), and the case that the first photovoltaic cell 2A does not generate power and leakage occurs (case 3).
Since the amount of products by the above-described oxidation and reduction reactions, and the conversion efficiency from sunlight to chemical energy are proportional to the current flowing through the reaction electrode pair 3, a larger current flowing through the reaction electrode pair 3 is more preferable. As listed in Table 1, the currents flowing through the first and second reaction electrode pairs 3A, 3B are at the same level. As listed as the case 2, even in the case where the first photovoltaic cell 2A does not generate power due to cloud or the like, the current flowing through the second reaction electrode pair 3B does not change and is thus not adversely affected by the failure of the first photovoltaic cell 2A. Further, as listed as the case 3, even in the case where leakages occurs in the first photovoltaic cell 2A, the current through the second reaction electrode pair 3B does not change and is thus not adversely affected by the failure of the first photovoltaic cell 2A.
Table 2 lists, as comparative examples of the photoelectrochemical reaction device in the embodiment, currents flowing through the reaction electrode pairs in the case 1, the case 2, and the case 3, as in Table 1, regarding a photoelectrochemical reaction device in which an oxidation reaction electrode pair composed of the third electrode and the fourth electrode is not provided for every photovoltaic cell but two photovoltaic cells connected in parallel are connected to one reaction electrode pair. As indicated in the case 1 in Table 2, when the two photovoltaic cells normally operate, the current flowing through the reaction electrode pair is the same as that in the case 1 of the embodiment. In contrast, as indicated in the case 2 and the case 3 in Table 2, when a failure occurs in one photovoltaic cell, the current flowing through the reaction electrode pair decreases as compared with that of the embodiment even though the other photovoltaic cell normally operates. In particular, when leakage occurs in one photovoltaic cell, the current flowing through the reaction electrode pair greatly decreases.
As described above, in the case where a plurality of photovoltaic cells are provided but the reaction electrode pair is not provided for each of the photovoltaic cells, a failed photovoltaic cell affects the other photovoltaic cell, even normally operating, and therefore decreases the current which contribute to oxidation and reduction reactions. Regarding this point, in the photoelectrochemical reaction device 1 in the embodiment, even if a failure occurs in the photovoltaic cell (2A) being a part thereof, its effect is limited only to the operation of the reaction electrode pair (3A) connected to the failed photovoltaic cell (2A) but not to the operations of the other photovoltaic cell (2B) and the reaction electrode pair (3B). Accordingly, an excellent conversion efficiency from light energy to chemical energy can be maintained.
A photoelectrochemical reaction device according to a second embodiment will be described with reference to
A photoelectrochemical reaction device 1X illustrated in
Each of the first and second photovoltaic modules 7A, 7B has six photovoltaic cells 2A to 2F. In the six photovoltaic cells 2A to 2F, first electrodes 11 are connected to be three in series and two in parallel, and second electrodes 21 are also connected to be three in series and two in parallel. As illustrated in
As described above, also in the case where the plurality of photovoltaic modules 7A, 7B are applied, electrical connection of the photovoltaic module 7 and the reaction electrode pair 3 as one set prevents a failed photovoltaic module 7 from adversely affecting the other photovoltaic module 7. Even if a failure occurs in the photovoltaic module (7A) being a part, its effect is limited only to the operation of the reaction electrode pair (3A) connected to the failed photovoltaic module (7A) but not to the operations of the photovoltaic module (7B) and the reaction electrode pair (3B). Accordingly, an excellent conversion efficiency from light energy to chemical energy can be maintained.
A photoelectrochemical reaction device according to a third embodiment will be described with reference to
The reaction electrode pair 3 includes a third electrode 41 as a common electrode and two fourth electrodes 42A, 42B as individual electrodes. In a first storage part 52 of the electrolytic bath 4, the third electrode 41 common to the first and second photovoltaic cells, 2A, 2B is arranged. In a second storage part 54 of the electrolytic bath 4, the fourth electrode 42A corresponding to the first photovoltaic cell 2A and the fourth electrode 42B corresponding to the second photovoltaic cell 2B are arranged. The reaction electrode pair 3 includes the third electrode 41 common to the first and second photovoltaic cells 2A, 2B, and the fourth electrode 42A and the fourth electrode 42B individually corresponding to the first and second photovoltaic cells 2A, 2B. The other configurations are the same as those in the first embodiment.
As illustrated in
As described above, also in the case where the electrode 42 that is one of electrodes of the reaction electrode pair 3 is an individual electrode, electrically connecting the individual electrode 42 and the photovoltaic cell 2 as a set makes it possible to decrease the effect of a failed photovoltaic cell 2 on the other photovoltaic cell 2. Table 3 lists, as in Table 1, currents flowing through the reaction electrode pair in the case 1, the case 2, and the case 3, regarding the third embodiment. It is found that the current flowing through the reaction electrode pair in the third embodiment is larger than that in the comparative example, in any of the case 2 and the case 3. Accordingly, an excellent conversion efficiency from light energy to chemical energy can be maintained. Note that in the case where a plurality of third electrodes 41 and fourth electrodes 42 are provided as illustrated in
A photoelectrochemical reaction device according to a fourth embodiment will be described with reference to
A photoelectrochemical reaction device 100 according to the fourth embodiment includes a photovoltaic cell 2, a reaction electrode 101, and an electrolytic bath 4. The photovoltaic cell 2 includes two divided first electrodes 11A, 11B, one second electrode 21, a first photovoltaic layer 31A which is provided between one first electrode 11A and the second electrode 21, and a second photovoltaic layer 31B which is provided between the other first electrode 11B and the second electrode 21. Note that concrete configurations and so on of the first electrode 11, the photovoltaic layer 31, the second electrode 21, the electrolytic bath 4 including the electrolytic solutions 51, 53, and the reaction electrode 101 corresponding to the fourth electrode are the same as those in the first embodiment, and their description will be omitted here.
The photovoltaic cell 2 of the fourth embodiment includes the second electrode 21 serving as a common electrode, a first stack unit 102A having the photovoltaic layer 31A and the first electrode 11A stacked in order on the second electrode 21, and a second stack unit 102B having the photovoltaic layer 31B and the first electrode 11B similarly stacked in order on the second electrode 21. The photovoltaic cell 2 is arranged in the electrolytic bath 4. The electrolytic bath 4 includes a first storage part 52 storing the first electrolytic solution 51 in which the photovoltaic cell 2 is immersed, a second storage part 54 storing the second electrolytic solution 53 in which the reaction electrode (corresponding to the fourth electrode) 101 is immersed, and an ion migration layer (an ion migration layer also serving as a separation wall) 55 allowing ions to migrate while separating the first electrolytic solution 51 and the second electrolytic solution 53. The concrete configuration of the ion migration layer 55 is as described above.
As illustrated in
In the photoelectrochemical reaction device 100 of the fourth embodiment, one of the first electrode 11A, 11B and the reaction electrode 101 causes an oxidation reaction and the other of the first electrode 11A, 11B and the reaction electrode 101 causes a reduction reaction. As in the first embodiment, the first electrodes 11A, 11B and the reaction electrode 101 may have a catalyst layer which promotes the oxidation reaction or the reduction reaction. When light is irradiated to the photovoltaic cell 2, H2O is oxidized so that O2 and H+ are generated (the formula (1)), for example, near the first electrodes 11A, 11B in contact with the first electrolytic solution 51. H+ generated on the first electrodes 11A, 11B side migrates to the reaction electrode 101 side via the ion migration layer 55. Near the reaction electrode 101 in contact with the second electrolytic solution 53, for example, CO2 is reduced so that CO and H2O are generated (the formula (2)).
To enhance the insulating property between the first stack unit 102A and the second stack unit 102B, an insulating member 103 may be arranged between them as illustrated in
The photoelectrochemical reaction device 100 of the fourth embodiment can be recognized as including a first photovoltaic cell based on the first stack unit 102A and a second photovoltaic cell based on the second stack unit 102B, because the second electrode 21 serves as a common electrode. Additionally, the first electrode 11A of the first stack unit 102A and the first electrode 11B of the second stack unit 102B are electrically insulated. Accordingly, as in the third embodiment, a failure, even when occurring in one photovoltaic cell (stack 102), never adversely affects the combination of the other photovoltaic cell (stack 102) and the reaction electrode 101. The conversion efficiency from light energy to chemical energy by the photoelectrochemical reaction device 100 can be maintained.
A photoelectrochemical reaction device according to a fifth embodiment will be described with reference to
The photovoltaic cell 2 of the fifth embodiment includes, as in the fourth embodiment, a first stack unit 102A having the photovoltaic layer 31A and the first electrode 11A stacked in order on the second electrode 21, and a second stack unit 102B having the photovoltaic layer 31B and the first electrode 11B stacked in order on the second electrode 21. The photovoltaic cell 2 is arranged in the electrolytic bath 4. The electrolytic bath 4 includes a first storage part 52 storing a first electrolytic solution 51, a second storage part 54 storing a second electrolytic solution 53, and an ion migration layer (an ion migration layer also serving as a separation wall) 55 allowing ions to migrate while separating the first electrolytic solution 51 and the second electrolytic solution 53.
The photovoltaic cell 2 is arranged in the first storage part 52 of the electrolytic bath 4 so that the second electrode 21 is located on the ion migration layer 55. The ion migration layer 55 has an opening 55a for exposing the rear surface of the second electrode 21. The photovoltaic cell 2 is arranged in the first storage part 52, so that the first electrode 11A of the first stack unit 102A and the first electrode 11B of the second stack unit 102B are in contact with the first electrolytic solution 51. The second electrode 21 is in contact with the second electrolytic solution 53 via the opening 55a provided in the ion migration layer 55.
The second electrode 21 serves as the common electrode with respect to the first stack unit 102A and the second stack unit 102B and is thus equivalent to being connected in parallel. The first stack unit 102A and the second stack unit 102B are geometrically separated. The thicknesses of the first electrode 11 and the photovoltaic layer 31 are as thin as about 1 micrometer to 10 micrometer, and the solution resistance between the first stack unit 102A and the second stack unit 102B is high. Accordingly, the first stack unit 102A and the second stack unit 102B are equivalent to being electrically insulated. The number of the stack units 102 having the photovoltaic layer 31 and the first electrode 11 is not limited to two but may be three or more.
In the photoelectrochemical reaction device 100 of the fifth embodiment, one of the first electrode 11A, 11B and the second electrode 21 causes an oxidation reaction and the other of the first electrode 11A, 11B and the second electrode 21 causes a reduction reaction. As in the first embodiment, the first electrodes 11A, 11B and the second electrode 21 may have a catalyst layer which promotes the oxidation reaction or the reduction reaction. When light is irradiated to the photovoltaic cell 2, H2O is oxidized so that O2 and H+ are generated, for example, near the first electrodes 11A, 11B in contact with the first electrolytic solution 51 as in the fourth embodiment. H+ generated on the first electrodes 11A, 11B side migrates to the second electrode 21 side via the ion migration layer 55 or a later-described ion migration unit 104. Near the second electrode 21 in contact with the second electrolytic solution 53, CO2 is reduced so that CO and H2O are generated.
To enhance the insulating property between the first stack unit 102A and the second stack unit 102B, an insulating member 103 may be arranged between them as illustrated in
The photoelectrochemical reaction device 110 of the fifth embodiment can be recognized as including a first photovoltaic cell based on the first stack unit 102A and a second photovoltaic cell based on the second stack unit 102B, because the second electrode 21 serves as a common electrode. Additionally, the first electrode 11A of the first stack unit 102A and the first electrode 11B of the second stack unit 102B are electrically insulated. As in the fourth embodiment, a failure, even when occurring in one photovoltaic cell (stack 102), never adversely affects the combination of the other photovoltaic cell (stack 102) and the second electrode 21. Accordingly, the conversion efficiency from light energy to chemical energy by the photoelectrochemical reaction device 110 can be maintained.
Note that the configurations of the first to fifth embodiments can be applied in combination. Further, parts thereof can be substituted. While certain embodiments have been described, these embodiments have been presented by way of example only, and are not intended to limit the scope of the inventions. Indeed, the embodiments described herein may be embodied in a variety of other forms; furthermore, various omissions, substitutions and changes in the form of the embodiments described herein may be made without departing from the spirit of the inventions. The accompanying claims and their equivalents are intended to cover such forms or modifications as would fall within the scope and spirit of the inventions.
Number | Date | Country | Kind |
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2014-104620 | May 2014 | JP | national |
This application is a continuation of prior International Application No. PCT/JP2015/001232 filed on Mar. 6, 2015, which is based upon and claims the benefit of priority from Japanese Patent Application No. 2014-104620 filed on May 20, 2014; the entire contents of all of which are incorporated herein by reference.
Number | Date | Country | |
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Parent | PCT/JP2015/001232 | Mar 2015 | US |
Child | 15252932 | US |