1. Field of the Invention
The present invention relates to a method of producing nano-particles of a sulfide compound semiconductor containing Cu, Zn, Sn and S by use of a solvothermal method, and relates to a rod-like crystal of a sulfide compound semiconductor.
2. Description of the Related Art
As a material of compound semiconductor solar batteries, CuInGaSe2 (CIGS) is a mainstream material at the present time. However, since the CIGS contains In that is a rare earth element and Se that is a highly toxic element, development of an alternative material is in demand.
As an alternative material for the CIGS, a sulfide compound semiconductor Cu2ZnSnS4 (Copper Zinc Tin Sulfur: CZTS) that has a band-gap energy suitable for solar batteries and contains neither In nor Se is gathering attention. The CZTS is typically produced by solid phase reaction of metal powder and sulfur powder under high temperatures in a deaerated glass ample. Further, as another method, Japanese Patent Application Publication No. 2009-135316 (JP 2009-135316 A) describes a method where a CZTS precursor is prepared by sputtering, and a film of the precursor is heated under an atmosphere of hydrogen sulfide, or a method where a solution in which an organic metal is dissolved is coated on a substrate and dried in air to cause hydrolysis and degenerate reaction to form a metal oxide thin film, and the thin film is heated under an atmosphere of hydrogen sulfide.
As described above, some examples of the method of producing CZTS have been known. However, when a solid phase reaction is used to produce, it is difficult to control a temperature of formation of Cu—Zn—Sn system alloys and/or a composition of generation phase. Accordingly; there was a problem that a homogeneous CZTS is difficult to obtain. Further, when a method that uses hydrogen sulfide is used, because of toxicity of hydrogen sulfide, there was a problem that safety management is costly.
In view of the above-described problems, the present invention provides a method of producing nano-particles of sulfide compound semiconductor, which enables to obtain microparticulate particles at a low cost, and rod-like crystals of sulfide compound semiconductor.
The present inventors, after variously studying means for solving the problems, have found that when Cu, Zn, Sn and S are solvothermally reacted in an organic solvent, microparticulate CZTS particles can be produced at a cost lower than that of a conventional product that is obtained by solid phase reaction, and thereby the present invention was completed.
That is, according to a first aspect of the present invention, a method of producing a sulfide compound semiconductor containing Cu, Zn, Sn and S is provided, in which the method includes a solvothermal step of conducting a solvothermal reaction of Cu, Zn, Sn and S in an organic solvent.
Further, in the solvothermal step in the method of producing, S may be solvothermally reacted in the form of sulfur powder or thiourea.
Still further, in the solvothermal step in the method of producing, at least one kind of Cu, Zn and Sn may be solvothermally reacted in the form of metal.
Further, in the solvothermal step in the method of producing, Cu, Zn and Sn may be solvothermally reacted in the form of salt.
An organic solvent used in the solvothermal step in the method of producing may be selected from the group consisting of ethylenediamine, isopropyl alcohol, oleylamine, oleic acid, ethanol, acetone, ethylene glycol, water/oleylamine, ethanol/oleylamine and oleic acid/oleylamine.
Still further, in the solvothermal step in the method of producing, the solvothermal reaction is preferably conducted at a temperature in the range of 200 to 450° C. for 1 to 24 hours. Here, in the solvothermal step, the solvothermal reaction is more preferably conducted at a temperature in the range of 200 to 450° C. for 8 to 12 hours.
Further, the S may be also in the form of sulfur powder.
Still further, a concentration of the Cu may be in the range of 0.1 to 1.0 mol/L. Further, a concentration of each of the Zn and the Sn may be also in the range of 0.05 to 0.5 mol/L. Still further, a concentration of the S may be also in the range of 0.2 to 4.0 mol/L.
Further, a molar ratio of the Cu, Zn, Sn and S is preferably in the range of 2:1:1:4 to 2:1:1:12 as a composition ratio of S to Cu, Zn and Sn. Here, a molar ratio of the Cu, Zn, Sn and S is more preferably in the range of 2:1:1:6 to 2:1:1:8 as a composition ratio of S to Cu, Zn and Sn.
According to a second aspect of the present invention, a rod-like crystal of sulfide compound semiconductor containing Cu, Zn, Sn and S is provided.
According to the method of producing of the present invention as described above, a method of producing CZTS nano-particles, which enables to obtain microparticulate particles at a low cost, can be provided. Further, according to the present invention, a rod-like crystal of microparticulate sulfide compound semiconductor containing Cu, Zn, Sn and S can be obtained.
The features, advantages, and technical and industrial significance of this invention will be described in the following detailed description of example embodiments of the invention with reference to the accompanying drawings, in which like numerals denote like elements, and wherein:
The present invention relates to a method of producing a sulfide compound semiconductor containing Cu, Zn, Sn and S (Copper Zinc Tin Sulfur: CZTS). In the present specification, “a sulfide compound semiconductor (CZTS)” means a semiconductive compound containing Cu, Zn, Sn and S and has a kesterite structure represented by a formula Cu2ZnSnS4. Preferable embodiments of the present invention will be detailed below.
The method of the present invention includes a solvothermal step of conducting a solvothermal reaction of Cu, Zn, Sn and S in an organic solvent. The present inventors have found that when Cu, Zn, Sn and S are solvothermally reacted in an organic solvent, microparticulate CZTS nano-particles having high crystallinity are generated. Accordingly, when the step is conducted, microparticulate CZTS having high crystallinity can be produced.
In the present specification, “a solvothermal reaction” means a process where a plurality of raw materials is reacted in an organic solvent under high pressure to obtain a crystal of a reaction product. In the present step, an organic solvent used in the solvothermal reaction is preferably an organic solvent selected from the group consisting of aliphatic monoamine or polyamine, aliphatic monoalcohol or polyalcohol, aliphatic acid and aliphatic ketone or a combination of two kinds or more thereof, or a combination of water and at least one kind of the organic solvents, more preferably an organic solvent selected from the group consisting of aliphatic monoamine or diamine, aliphatic monoalcohol or dialcohol, aliphatic acid and aliphatic ketone or a combination of two kinds or more thereof, or a combination of water and at least one kind of the organic solvents, and still more preferably an organic solvent selected from the group consisting of straight, branched or cyclic saturated or unsaturated aliphatic monoamine or diamine, straight, branched or cyclic saturated or unsaturated aliphatic monoalcohol or dialcohol, straight, branched or cyclic saturated or unsaturated aliphatic acid, and straight, branched or cyclic saturated or unsaturated aliphatic ketone or a combination of two or more kinds thereof, or a combination of water and at least one kind of the organic solvents. In the case described above, the number of carbon atoms of the aliphatic group is preferably in the range of C1 to C20, more preferably in the range of C2 to C20, and still more preferably in the range of C1 to C18. For example, the organic solvent is preferably an organic solvent selected from the group consisting of ethylenediamine, isopropyl alcohol, oleylamine, oleic acid, ethanol, acetone and ethylene glycol, or a combination of two or more kinds thereof, or a combination of water and at least one kind of the organic solvents. Among the combinations of the organic solvents of two or more kinds or combinations of water and at least one kind of the organic solvents, water/oleylamine, ethanol/oleylamine or oleic acid/oleylamine is preferred. In these cases, a mixing ratio of water or organic solvents may be 1:1.
The present step is preferably conducted under the presence of, in addition to raw material substances and an organic solvent, one or more kinds of additives in certain cases. An additive used in the step is preferably polyvinylpyrrolidone. When the present step is conducted under the presence of the additive, a concentration of the additive is, with respect to a total mass of the raw material, 10% by mass to 50% by mass and preferably in the range of 30% by mass to 40% by mass. By conducting the present step under the presence of the additive, the dispersibility of the raw material can be improved.
In the present step, a solvothermal reaction temperature is preferably in the range of 200 to 450° C., more preferably in the range of 200 to 350° C., and still more preferably in the range of 250 to 350° C. Further, a solvothermal reaction time is preferably in the range of 1 to 24 hours, more preferably in the range of 8 to 24 hours and still more preferably in the range of 8 to 12 hours.
When the solvothermal reaction is conducted under the above-mentioned Conditions, CZTS can be obtained at a temperature lower than and for a time shorter than these of the conventional method like a solid phase reaction.
When the present step is conducted, means for conducting a solvothermal reaction is not specifically limited. An apparatus used in the solvothermal reaction in the art such as an autoclave can be used. Specifically, when the solvothermal reaction is conducted at a temperature in the range of 200 to 250° C., an apparatus that uses a relatively cheap resin such as a fluororesin (for example, TEFLON™, PTFE manufactured by DuPont) may be used, and when the solvothermal reaction is conducted at a temperature more than 250° C. and 400° C. or lower, an apparatus that uses a heat-resistant and corrosion-resistant alloy such as a nickel alloy (for example, HASTELLOY™, manufactured by Haynes International, Inc.) may be used. When the present step is conducted by use of an autoclave, the filling rate of a reaction mixture containing Cu, Zn, Sn and S is preferably in the range of 30 to 70% by volume relative to an internal volume of the autoclave, and more preferably 40 to 60% by volume or less. When the above method is used, without preparing a special apparatus, the present step can be readily conducted.
In the present step, S may be used in the form of sulfur powder or thiourea. The present inventors have found that when the solvothermal reaction is conducted, with sulfur powder or thiourea as a raw material, the CZTS can be produced. Usually, when the CZTS is produced, in order to use sulfur powder, a solid phase reaction under high temperature and high pressure is necessary. On the other hand, when sulfide such as hydrogen sulfide is used, in order to prevent health damage due to toxic hydrogen sulfide, safety management is costly. Accordingly, when the solvothermal reaction is conducted with sulfur powder or thiourea as an S source, the CZTS can be obtained at a lower cost, at a lower temperature and for a shorter time than a conventional method like a solid phase reaction or a reaction that uses sulfide.
In the present step, Cu, Zn and Sn used may be in the form of either metal or salt. It is preferable that at least one kind of Cu, Zn and Sn is in the form of metal and the others are in the form of salt, and more preferable that all of Cu, Zn and Sn are in the form of salt. In the case of in the form of salt, examples of pair ions include a conjugate base of inorganic acid or organic acid, for example, a conjugate base of hydrogen halide or C1 to C4 aliphatic acid, preferably, Cl−1, CH3COO−(Ac−) and CH3CH2COO−. Among these, Cl− or CH3COO−(Ac−) is preferable. Further, in the case of salt form, the salt form may be an anhydride form or a hydride form. Salts of Cu, Zn and Sn are preferably salts selected respectively from the group consisting of CuAc2, CuAc2×H2O, CuCl2, CuCl2×2H2O, ZnAc2, ZnCl2, SnCl2, SnCl4×5H2O and SnAc2. Salts of Cu, Zn and Sn (for example, CuAc2×H2O, CuCl2, CuCl2×2H2O, ZnAc2, ZnCl2, SnCl2, SnCl4×5H2O and SnAc2) are cheap materials industrially utilized in the art. Accordingly, when the above-mentioned salts are used as Cu, Zn and Sn sources, the target CZTS can be produced at a low cost.
In the present step, a concentration of Cu is preferably in the range of 0.01 to 1.0 mol/L and more preferably in the range of 0.1 to 1.0 mol/L. Concentrations of Zn and Sn are preferably in the range of 0.01 to 0.5 mol/L, and more preferably in the range of 0.05 to 0.5 mol/L. Further, a concentration of S is preferably in the range of 0.1 to 4.0 mol/L and more preferably in the range of 0.2 to 4.0 mol/L. Specifically, a molar ratio of Cu, Zn, Sn and S is, as a composition ratio of S to Cu, Zn and Sn, preferably in the range of 2:1:1:4 to 2:1:1:12, more preferably in the range of 2:1:1:4 to 2:1:1:8 and still more preferably in the range of 2:1:1:6 to 2:1:1:8. When Cu, Zn, Sn and S of the above concentrations are used, the CZTS can be produced with high purity and at high yield.
The CZTS obtained from the solvothermal reaction can be separated from a reaction mixture after the solvothermal reaction by conventional means such as filtration and can be washed with water as desired.
When the present step is conducted under the above conditions, the CZTS can be produced with high purity and at high yield.
The present inventors have found that when metal salts are used as raw materials, the CZTS obtained according to the method of the present invention becomes a crystal form having a fine particle size. Specifically, the CZTS obtained according to the method of the present invention usually has a particle size of 5 to 200 nm and typically of 30 to 200 nm. In the CZTS obtained according to the method of the invention, primary particles having the above mentioned particle size flocculate to form secondary particles having particle size of 5 nm to 500 μm. The CZTS obtained from the solid phase reaction usually has a particle size of 1 μm or more. Accordingly, by use of the method of the present invention, CZTS nano-particles having a particle size finer than that of the conventional method can be obtained.
The particle size of the CZTS is not specifically limited, but can be determined by use of for example, a UV-laser meter or a transmission electron microscope (TEM).
Further, the present inventors have found that the CZTS obtained according to the method of the present invention is usually spherical crystals having the above mentioned particle size but a rod-like crystal depending on the case. The rod-like crystal CZTS is a novel crystalline form which could not be obtained according to the conventional method. Accordingly, the present invention relates to a rod-like crystal of CZTS.
The rod-like crystal of CZTS of the present invention is preferably produced according to the present method described above and more preferably produced according to a method of the present invention that uses acetone as an organic solvent in the solvothermal step. In this case, a length in a major axis direction of the rod-like crystal is usually in the range of 30 to 70 nm. A length in a minor axis direction of the rod-like crystal is usually in the range of 5 to 10 nm. Further, a ratio of the length in a major axis direction to the length in a minor axis direction is usually in the range of 4 to 10.
The rod-like crystals tend to orient, due to the shape thereof, so that axes along the major axis direction of crystals are contained each other in the same plane. Accordingly, when the rod-like crystals of CZTS of the present invention are used, a compound semiconductor having high crystal orientation can be produced.
As described above, according to the method of the present invention, CZTS nano-particles having a fine particle size can be produced. By use of the CZTS produced according to the method of the present invention, a compound semiconductor solar battery can be produced at a lower cost. Further, the rod-like crystal of CZTS obtained according to the method of the present invention has high crystal orientation. Accordingly, when the rod-like crystal of CZTS obtained according to the method of the present invention is used, a compound semiconductor solar battery having higher conversion efficiency can be produced.
The present invention will be described below in more detail with reference to examples and comparative examples. Firstly, 2 mmol of Cu source, 1 mmol of Zn source, and 1 mmol of Sn source were dispersed together with various mole numbers of sulfur (S) powder in 10 ml of an organic solvent, filled in an autoclave and stirred for 30 minutes. The dispersion was solvothermally reacted in the autoclave (solvothermal step). The resulting product was filtered and dried in air under conditions of 50° C. and 22 hours (drying step). Thereby, CZTS was obtained. Preparation conditions of the respective examples are shown in Table 1.
Obtained powders of Examples 1 to 21 were analyzed according to X-ray powder diffraction (XRD), differential thermal analysis (DTA), transmission electron microscope (TEM), energy dispersive fluorescent X-ray analysis (EDX) and scanning electron microscope (SEM). Results are shown in Table 1 and
As shown in Table 1, elements compositions of the powders of Examples 1 to 21 were in the range of 21 to 33: 9 to 27: 7 to 15: 39 to 51, and an average value thereof was 28:14:13:45.
As shown in
Powders obtained according to Examples 11 to 21 except Examples 12, 15, 17 and 18 were analyzed by use of TEM and high resolution TEM. Results are shown in
As shown in
As shown in
Then, 2 mmol of Cu source, 1 mmol of Zn source, 1 mmol of Sn source and 5 mmol of S source were filled in an autoclave of HASTELLOY™ and 30 ml of the organic solvent was added so that a filling rate becomes 50%. In the cases of Examples 33 and 35, polyvinylpyrrolidone as an additive was further added. The autoclave was, after hermetically sealing, heated at 240° C. for 24 hours to conduct the solvothermal reaction (solvothermal step). The resulted product was naturally cooled. Thereafter, the product was separated by centrifugation, and precipitate was washed with pure water and ethanol. The product after washing was dried under condition of 70° C. for 30 min to 10 hours (drying step). Thereby, a CZTS was obtained. The preparation condition of the respective Examples was shown in Table 2.
Each of resulted powders of Examples 31 to 35 was analyzed by scanning electron microscope (SEM), transmission electron microscope (TEM), energy dispersive fluorescent X-ray analysis provided to transmission electron microscope (TEM/EDX), X-ray powder diffraction (XRD), X-ray photoelectron spectrometry (XPS), Raman spectrometry, and thermogravimetric differential thermal analysis (TG-DTA).
An SEM image of the powder of Example 31 is shown in
XRD spectra of powders of Examples 31 to 35 are shown in
Then, whether the CZTS is present is confirmed by Raman spectrometry. Results are shown in
TEM images and electron diffraction images of powders of Examples 31 to 35 are shown in
Composition analysis of powders of Examples 31 to 35 was conducted by EDX. As the result thereof, it was demonstrated that powders of Examples 31 to 35 contain elements Cu, Zn, Sn and S corresponding to CZTS; that is, almost stoichiometric CZTS is generated. However, a composition ratio of four elements was observed to be different depending on measurement sites.
In order to differentiate the CZTS contained in powders of Examples 31 to 35 from Cu2SnS3 and β-ZnS, TG-DTA measurement was conducted. It is reported that Cu2SnS3 has a transition temperature at 775° C. from triclinic to cubic and melts at 850° C. CZTS is reported to melt at 991° C. Further, ZnS is reported to cause transition at 1020° C. from cubic to wurtzite and to melt at 1650° C. However, it is considered that in nanosize crystals, these temperatures become lower. For example, it is reported that CZTS nanocrystal and Cu2SnS3 nanocrystal, respectively have a phase transition temperature at 830° C. and 747° C.
TG-DTA measurements of powders of Examples 31 to 35 were all similar. Accordingly, the TG-DTA measurement of powder of Example 34 is shown in
As shown above, in Examples 31 to 35, irrespective of use of raw materials having different valence, same products were obtained. Then, valence and composition of synthesized CZTSs were investigated by XPS. XPS spectra of four elements (Culp, Zn2p3, Sn3d5 and S2p) are shown in
In XPS spectrum of copper (Cu), there are two peaks at 932.0 and 951.8 eV, and from the peak difference of 19.8 eV, it is indicated that Cu(I) exists (
From analysis results of XPS, elemental composition of CZTS nanoparticles of Examples 31 to 35 were calculated. Results are shown in Table 3. Values in the table were calculated on the basis of Cu.
Since the results of Table 3 were calculated from results of XPS analysis, the results are based on elemental compositions of local regions on surfaces of samples. In this connection, in order to improve accuracy of quantitative analysis values, the respective elements of the CZTS nanoparticles of Examples 31 to 35 were quantitatively analyzed by use of ICP (high frequency plasma emission spectrometer).
About 20 mg of each of powders of Examples 31 to 35 was measured. To the powder, 3 ml of aqua regalis was added, further the mixture was subjected to white smoking by adding 3 ml of sulfuric acid (400° C., for 10 min). The processed mixture was cooled, 2 ml of hydrochloric acid was added, further a slight amount of pure water was added, and the resulted mixture was heated at 200° C. for 10 min. Thereafter, a reaction mixture was prepared to a constant volume of 100 ml for a sample for quantitative analysis. By use of ICP (trade name: ICP-8100, manufactured by Shimadzu Corporation), Cu (measurement wavelength: 327.396 nm), Zn (measurement wavelength: 213.856 nm) and Sn (measurement wavelength: 189.989 nm) contained in the sample for quantitative analysis were quantitatively analyzed. Further, by use of catalyst sulfur analyzer (trade name: EMIA-920V, manufactured by Horiba Limited), S contained in the sample for quantitative analysis was quantitatively: analyzed (measurement condition: integrated time 80 sec, current value 350 mA, 50 sec, combustion improver Sn: 0.3 g, W 1.5 g).
From analysis results by ICP and sulfur analyzer, elemental compositions of the CZTS nanoparticles of Examples 31 to 35 were calculated. Results thereof are shown in Table 4. Values in the table are values calculated based on Cu.
From analysis results described above, it was clarified that according to a solvothermal reaction, spherical CZTS powder having an almost uniform particle size of several hundreds nanometers can be produced. A particle size of primary particles of CZTS is about 10 nm and the primary particles flocculate to form secondary particle. Valence of each of metal elements configuring the CZTS was not affected by valence of the starting raw material.
According to the method of the present invention, CZTS nano-particles having a fine particle size can be produced at a low cost.
Number | Date | Country | Kind |
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2011-126267 | Jun 2011 | JP | national |
2012-114566 | May 2012 | JP | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/IB2012/001223 | 6/6/2012 | WO | 00 | 12/5/2013 |