JP4437695B2 - Method for producing nitrogen-containing metal oxide photocatalyst - Google Patents
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Description
本発明は、窒素含有金属酸化物光触媒の製造方法に関する。 The present invention relates to a method for producing a nitrogen-containing metal oxide photocatalyst.
金属酸化物半導体は、光の照射によって酸化分解能や親水性を発現する光触媒として知られている。 Metal oxide semiconductors are known as photocatalysts that exhibit oxidation resolution and hydrophilicity when irradiated with light.
近年、金属酸化物半導体はこの光触媒作用が注目され、空気及び水質の浄化、抗菌、防汚など様々な用途で使用されている。 In recent years, metal oxide semiconductors have attracted attention for their photocatalytic action, and are used in various applications such as purification of air and water, antibacterial properties, and antifouling.
しかしながら、自然環境下で安定して高い光触媒作用を発現する金属酸化物半導体は、バンドギャップが大きいため紫外光照射においては光触媒作用を発現するが、紫外光の放出が極めて少ない蛍光灯などによる光照射では光触媒作用はほとんど発現しない。したがって、金属酸化物半導体を屋内用途の触媒として使用する場合には、紫外光を放出する特別な光源を別途設けなければならないという問題がある。 However, metal oxide semiconductors that stably exhibit high photocatalytic activity in the natural environment have a large band gap, so that they exhibit photocatalytic activity when irradiated with ultraviolet light, but light emitted by fluorescent lamps and the like that emit very little ultraviolet light. Irradiation shows little photocatalysis. Therefore, when a metal oxide semiconductor is used as a catalyst for indoor use, there is a problem that a special light source that emits ultraviolet light must be provided separately.
この問題を解決すべく、紫外光のみならず可視光照射によっても光触媒作用を発現する可視光応答型光触媒が既に提案されている(例えば、特許文献1、2参照)。 In order to solve this problem, visible light responsive photocatalysts that exhibit photocatalytic action not only by ultraviolet light but also by visible light irradiation have already been proposed (see, for example, Patent Documents 1 and 2).
特許文献1には、酸化物半導体を水素ガスプラズマ或いは希ガス類元素プラズマで処理して酸素欠陥を作ることで、可視光応答性を付与する方法が提案されている。しかしながら、この方法は、一度に処理できる量が少ないため工業的には不利である。 Patent Document 1, by making oxygen defects by processing the oxide semiconductor with a hydrogen gas plasma or rare gas element plasma, how to grant visible light response has been proposed. However, this method is industrially disadvantageous because the amount that can be processed at one time is small.
特許文献2には、酸化物を尿素と混合して加熱することにより酸化物に窒素を侵入させることで可視光応答性を付与する方法が提案されている。この方法は、一度に多量の処理が可能であるため工業的に有利である。 Patent Document 2 proposes a method of imparting visible light responsiveness by mixing nitrogen with urea and heating the oxide to cause nitrogen to enter the oxide. This method is industrially advantageous because a large amount of treatment is possible at one time.
しかし、特許文献2の方法で製造した可視光応答型光触媒の触媒作用の効果を確認したところ、蛍光灯照射では触媒作用はほとんど発現しなかった。これは、酸化物中に窒素が効果的に侵入していないためであると考えられる。また、紫外光特性も著しく劣化することが確認された。これは、加熱処理により結晶成長が促進されて比表面積が低減したためと考えられる。 However, when the effect of the catalytic action of the visible light responsive photocatalyst produced by the method of Patent Document 2 was confirmed, almost no catalytic action was exhibited by fluorescent lamp irradiation. This is presumably because nitrogen has not effectively penetrated into the oxide. In addition, it was confirmed that the ultraviolet light characteristics were significantly deteriorated. This is presumably because crystal growth was promoted by heat treatment and the specific surface area was reduced.
本発明の目的は、蛍光灯照射によっても高い活性を示す窒素含有金属酸化物光触媒を製造することである。 An object of the present invention is to produce a nitrogen-containing metal oxide photocatalyst that exhibits high activity even when irradiated with a fluorescent lamp.
本発明の別の目的は、蛍光灯照射によっても高い活性を示すことに加え、紫外光特性にも優れた窒素含有金属酸化物光触媒を製造することである。 Another object of the present invention is to produce a nitrogen-containing metal oxide photocatalyst excellent in ultraviolet light characteristics in addition to exhibiting high activity even when irradiated with a fluorescent lamp.
請求項1記載の発明の窒素含有金属酸化物光触媒の製造方法は、少なくとも非晶質水酸化亜鉛と尿素とを混合する工程と、この混合物を加熱する工程と、を含む。 The method for producing a nitrogen-containing metal oxide photocatalyst according to claim 1 includes a step of mixing at least amorphous zinc hydroxide and urea, and a step of heating the mixture .
請求項2記載の発明は、請求項1記載の窒素含有金属酸化物光触媒の製造方法において、前記混合物の加熱を外気の侵入を遮断した空間内で行う。 According to a second aspect of the invention, the method for producing nitrogen-containing metallic oxide photocatalyst according to claim 1, carried out within the heating of the mixture was cut off the outside air from entering the space.
請求項1記載の発明によれば、少なくとも非晶質水酸化亜鉛と尿素とを混合した混合物を加熱することにより、非晶質水酸化亜鉛が非晶質酸化亜鉛と水とに分解され、発生した水との反応により尿素が分解されてアンモニアが発生する。発生したアンモニアは、非晶質酸化亜鉛に一様に吸着し、吸着しなかった過剰なアンモニアはアンモニアガスとなって非晶質酸化亜鉛の周囲に漂い、このようなアンモニア雰囲気中で非晶質酸化亜鉛が結晶化するので、結晶化の過程で窒素が酸化亜鉛の結晶中に効果的に侵入する。これにより、蛍光灯照射によって高い活性を示す窒素含有金属酸化物光触媒が得られる。 According to the first aspect of the present invention, by heating a mixture of at least amorphous zinc hydroxide and urea, the amorphous zinc hydroxide is decomposed into amorphous zinc oxide and water and generated. As a result of the reaction with water, urea is decomposed to generate ammonia. Generated ammonia uniformly adsorbed in amorphous zinc oxide, drift around the amorphous zinc oxide become the excess ammonia that was not adsorbed ammonia gas, amorphous in such a ammonia atmosphere Since zinc oxide crystallizes, nitrogen effectively penetrates into the zinc oxide crystal during the crystallization process. Thereby, the nitrogen-containing metal oxide photocatalyst which shows high activity by fluorescent lamp irradiation is obtained .
また、請求項1記載の発明によれば、非晶質状態からの結晶化と同時に窒素を侵入させるため、既に結晶化している酸化亜鉛を加熱して窒素を侵入させる場合と異なり、過大な結晶成長による比表面積の低減を回避でき、紫外光による触媒性能である紫外光特性が維持される。 Further, according to the first aspect of the invention, in order to penetrate the crystallized simultaneously with nitrogen from the amorphous state, unlike the case already is entering the nitrogen by heating zinc oxide is crystallized, excessive crystal Reduction of the specific surface area due to growth can be avoided, and the ultraviolet light characteristic which is the catalytic performance by ultraviolet light is maintained.
請求項2記載の発明によれば、少なくとも非晶質水酸化亜鉛と尿素とを混合した混合物を加熱したときにおいて、非晶質酸化亜鉛の周囲が確実にアンモニア雰囲気となり、酸化亜鉛の結晶中への窒素の侵入効果が高くなる。 According to the second aspect of the present invention, when a mixture of at least amorphous zinc hydroxide and urea is heated, the atmosphere around the amorphous zinc oxide is surely an ammonia atmosphere, and the zinc oxide crystal enters. Increases the nitrogen penetration effect.
一実施の形態を説明する。まず、非晶質金属水酸化物と尿素とを用意する。非晶質金属水酸化物は湿式法で作製することができる。尿素は市販のものを使用することができる。
An embodiment will be described. First, an amorphous metal hydroxide and urea are prepared. The amorphous metal hydroxide can be produced by a wet method. A commercially available urea can be used.
つぎに、非晶質金属水酸化物と尿素とを混合する。混合比は特に限定されないが、尿素の量が少ないと発生するアンモニアの量が少ないため、後述する金属酸化物への窒素の侵入量が不十分となる。逆に、尿素の量が多いと尿素が分解しきれずに不純物として残留する。したがって、尿素が完全分解するのに必要な水の量と、加熱により非晶質金属水酸化物から発生する水の量とを考慮した混合比にすることが望ましい。 Next, an amorphous metal hydroxide and urea are mixed. The mixing ratio is not particularly limited, but when the amount of urea is small, the amount of ammonia generated is small, so that the amount of nitrogen entering the metal oxide described later becomes insufficient. Conversely, if the amount of urea is large, urea cannot be completely decomposed and remains as an impurity. Therefore, it is desirable to set the mixing ratio in consideration of the amount of water required for complete decomposition of urea and the amount of water generated from the amorphous metal hydroxide by heating.
つぎに、その混合物(非晶質金属水酸化物と尿素との混合物)を加熱する。加熱温度は、金属酸化物が結晶化する温度以上であればよい。しかし、加熱温度があまり低温であると、尿素が分解されずに不純物として残留する。一方、加熱温度が高すぎると、金属酸化物の結晶粒径が大きくなって比表面積が低減する。したがって、加熱温度としては、300〜800℃の範囲とすることが好ましい。 Next, the mixture (a mixture of amorphous metal hydroxide and urea) is heated. The heating temperature should just be more than the temperature which a metal oxide crystallizes. However, if the heating temperature is too low, urea remains as impurities without being decomposed. On the other hand, if the heating temperature is too high, the crystal grain size of the metal oxide increases and the specific surface area decreases. Therefore, the heating temperature is preferably in the range of 300 to 800 ° C.
また、加熱の方法は特に限定されないが、酸素の侵入がない空間内で加熱することが好ましい。その理由は、アンモニアと酸素とが反応して有害な窒素酸化物が発生することを防止するためである。空間内に不活性ガスやアンモニアガスを供給しながら加熱してもよいが、製造コストが高くなる。よって、窒素酸化物の発生防止、製造コストを考慮すると、密閉した空間内で加熱することが好ましい。さらに、安全性も考慮すると、内部で発生したガスが排気される方向に逆止弁を設けることが望ましい。 The heating method is not particularly limited, but it is preferable to heat in a space where oxygen does not enter. The reason is to prevent ammonia and oxygen from reacting to generate harmful nitrogen oxides. Although heating may be performed while supplying an inert gas or ammonia gas into the space, the manufacturing cost increases. Therefore, in consideration of prevention of generation of nitrogen oxides and production costs, it is preferable to heat in a sealed space. Furthermore, in consideration of safety, it is desirable to provide a check valve in the direction in which the gas generated inside is exhausted.
加熱時間は加熱温度に依存するために限定することはできないが、加熱時間が短いと金属酸化物への窒素の侵入量が不十分となり、逆に加熱時間が長いと金属酸化物の結晶粒径が大きくなって比表面積が低減する。したがって、加熱時間としては、数分から数時間とすることが好ましい。 The heating time depends on the heating temperature and cannot be limited. However, if the heating time is short, the amount of nitrogen entering the metal oxide becomes insufficient. Conversely, if the heating time is long, the crystal grain size of the metal oxide Increases and the specific surface area decreases. Therefore, the heating time is preferably several minutes to several hours.
非晶質金属水酸化物と尿素との混合物を加熱したときの反応について説明する。非晶質金属水酸化物と尿素とを混合して加熱することにより、まず、非晶質金属水酸化物が非晶質の金属酸化物と水とに分解される。発生した水との反応により尿素が完全に分解され、アンモニアが効率よく発生する。発生したアンモニアは、非晶質の金属酸化物に一様に吸着する。吸着しなかった過剰なアンモニアはガス(アンモニアガス)となって空間内に漂い、このようなアンモニア雰囲気中で非晶質の金属酸化物が結晶化するので、結晶化の過程で窒素を金属酸化物の結晶中に効果的に侵入させることができる。 The reaction when a mixture of amorphous metal hydroxide and urea is heated will be described. By mixing and heating the amorphous metal hydroxide and urea, first, the amorphous metal hydroxide is decomposed into an amorphous metal oxide and water. By reaction with the generated water, urea is completely decomposed and ammonia is efficiently generated. The generated ammonia is uniformly adsorbed on the amorphous metal oxide. Excess ammonia that has not been adsorbed becomes a gas (ammonia gas) and drifts into the space, and amorphous metal oxides crystallize in such an ammonia atmosphere, so nitrogen is oxidized into metal during the crystallization process. It can effectively penetrate into the crystal of the object.
さらに、結晶化と同時に窒素を侵入させるため、既に結晶化している酸化物を加熱して窒素を侵入させる場合と異なり、過大な結晶成長による比表面積の低減を回避できる。 Furthermore, since nitrogen is introduced at the same time as crystallization, a reduction in specific surface area due to excessive crystal growth can be avoided unlike in the case where nitrogen is introduced by heating an already crystallized oxide.
つぎに、実施例を挙げて本発明の詳細を説明するが、本発明はこの実施例に限定されるものではない。 Next, the present invention will be described in detail with reference to examples, but the present invention is not limited to these examples.
<実施例1>
湿式法により作製した非晶質の水酸化亜鉛1gと市販の尿素0.5gとをセラミックス皿上で攪拌混合し、それを酸素の侵入を遮断した電気炉内で500℃で1時間加熱し、光触媒(窒素含有金属酸化物光触媒)を得た。
<Example 1>
1 g of amorphous zinc hydroxide prepared by a wet method and 0.5 g of commercially available urea are mixed and stirred on a ceramic dish, and heated at 500 ° C. for 1 hour in an electric furnace where oxygen intrusion is blocked. A photocatalyst (nitrogen-containing metal oxide photocatalyst) was obtained.
このようにして得られた触媒(窒素含有金属酸化物光触媒)0.2gを15mm×40mmのケースに平坦かつ均一に敷き詰め、それを、直径20mm、長さ200mmの石英管内に設置して光を照射し、空気で希釈した濃度1ppmのNOガスを毎分0.8リットルで1時間流通させ、NOガスの分解試験を行った。光源としては、100WのUVランプと、27Wの蛍光灯を用い、反応ガスの測定には化学発光式窒素酸化物濃度測定装置(堀場製作所製 APNA−360)を用いた。 0.2 g of the catalyst (nitrogen-containing metal oxide photocatalyst) obtained in this way was laid flat and uniformly in a case of 15 mm × 40 mm, and it was placed in a quartz tube with a diameter of 20 mm and a length of 200 mm to emit light. A NO gas decomposition test was conducted by irradiating and diluting NO gas with a concentration of 1 ppm at 0.8 liters per minute for 1 hour. As a light source, a 100 W UV lamp and a 27 W fluorescent lamp were used, and a chemiluminescent nitrogen oxide concentration measuring device (APNA-360 manufactured by Horiba, Ltd.) was used for reaction gas measurement.
<比較例1>
湿式法により作成した非晶質の水酸化亜鉛1gをセラミックス皿に載せ、それを酸素の侵入を遮断した電気炉内で500℃で1時間加熱し、光触媒を得た。
<Comparative Example 1>
1 g of amorphous zinc hydroxide prepared by a wet method was placed on a ceramic dish and heated at 500 ° C. for 1 hour in an electric furnace where oxygen intrusion was blocked to obtain a photocatalyst.
このようにして得られた光触媒を0.2g使用し、実施例1と同じ方法でNOガスの分解試験を行った。 Using 0.2 g of the photocatalyst thus obtained, a NO gas decomposition test was performed in the same manner as in Example 1.
<比較例2>
市販の酸化亜鉛を0.2g使用し、実施例1と同じ方法でNOガスの分解試験を行った。
<Comparative example 2>
Using 0.2 g of commercially available zinc oxide, a NO gas decomposition test was performed in the same manner as in Example 1.
<比較例3>
市販の酸化亜鉛1gと市販の尿素0.5gとをセラミックス皿上で攪拌混合し、それを酸素の侵入を遮断した電気炉内で500℃で1時間加熱し、光触媒を得た。
<Comparative Example 3>
1 g of commercially available zinc oxide and 0.5 g of commercially available urea were stirred and mixed on a ceramic dish, and heated at 500 ° C. for 1 hour in an electric furnace where oxygen intrusion was blocked to obtain a photocatalyst.
このようにして得られた光触媒を0.2g使用し、実施例1と同じ方法でNOガスの分解試験を行った。 Using 0.2 g of the photocatalyst thus obtained, a NO gas decomposition test was performed in the same manner as in Example 1.
上記実施例1及び比較例1〜3で行った試験結果を表1に示す。試験結果は、1時間の試験で供給されたNOガスの総量に対して転化されたNOxの割合で示した。 Table 1 shows the test results obtained in Example 1 and Comparative Examples 1 to 3. The test results are shown as the ratio of NOx converted to the total amount of NO gas supplied in the one hour test.
市販の酸化亜鉛を処理せずに用いた比較例2の結果と、市販の酸化亜鉛と尿素とを混合して加熱処理した比較例3とを比べることにより、比較例3の場合には、蛍光灯照射における触媒作用が発現されず、また、加熱処理する前よりも紫外光特性が劣化しているという問題があることがわかる。 In the case of Comparative Example 3, the result of Comparative Example 2 that was used without treatment with commercially available zinc oxide was compared with Comparative Example 3 in which commercial zinc oxide and urea were mixed and heat-treated. It can be seen that there is a problem that the catalytic action in the lamp irradiation is not exhibited and the ultraviolet light characteristics are deteriorated as compared with those before the heat treatment.
これに対し、実施例1に示した本発明の窒素含有金属酸化物光触媒の場合には、蛍光灯照射における触媒作用が発現され、また、紫外光特性が維持されていることがわかる。
In contrast, in the case of the nitrogen-containing metal oxide photocatalyst of the present invention shown in Example 1, it can be seen that the catalytic action in the fluorescent lamp irradiation is expressed and the ultraviolet light characteristics are maintained.
Claims (2)
この混合物を加熱する工程と、
を含む窒素含有金属酸化物光触媒の製造方法。 Mixing at least amorphous zinc hydroxide and urea ;
Heating the mixture ;
A method for producing a nitrogen-containing metal oxide photocatalyst comprising :
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