JPH0796202A - Photocatalyst for treating harmful substance contained in liquid, and treating device therefor - Google Patents
Photocatalyst for treating harmful substance contained in liquid, and treating device thereforInfo
- Publication number
- JPH0796202A JPH0796202A JP4143692A JP14369292A JPH0796202A JP H0796202 A JPH0796202 A JP H0796202A JP 4143692 A JP4143692 A JP 4143692A JP 14369292 A JP14369292 A JP 14369292A JP H0796202 A JPH0796202 A JP H0796202A
- Authority
- JP
- Japan
- Prior art keywords
- titanium oxide
- liquid
- woven fabric
- harmful substance
- photocatalyst
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
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- Physical Water Treatments (AREA)
- Removal Of Specific Substances (AREA)
- Catalysts (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、光を照射することによ
り液中に存在するトリクロロエチレン、クロロホルム、
ダイオキシン等の有機ハロゲン化合物や、シアン、農薬
成分等の有害物質を効率良く分解、除去したり或いは液
中に存在する菌を殺菌して低減したり等して液中有害物
質を処理できる液中有害物質処理用光触媒とそれを利用
した液中有害物質処理装置に関する。TECHNICAL FIELD The present invention relates to trichloroethylene, chloroform, which is present in a liquid when irradiated with light,
In a liquid that can treat harmful substances in the liquid by efficiently decomposing and removing organic halogen compounds such as dioxins, and harmful substances such as cyanide and pesticide components, or by sterilizing and reducing bacteria present in the liquid. The present invention relates to a photocatalyst for treating harmful substances and an apparatus for treating harmful substances in liquids using the photocatalyst.
【0002】[0002]
【従来の技術】従来、光触媒を利用して液中の有害物質
を処理する方法としては、酸化チタン粉体を液中に分散
させてこれに有害物質を含む溶液を流し込み、光を照射
して分解処理する方法や、ガラス棒やガラス球に酸化チ
タン膜を被覆したものを液中に配置し、これに有害物質
を含む溶液を流し込み、光を照射して分解処理する方法
が知られている。2. Description of the Related Art Conventionally, as a method of treating harmful substances in a liquid by using a photocatalyst, titanium oxide powder is dispersed in the liquid and a solution containing the harmful substances is poured into the liquid and irradiated with light. There are known methods of decomposing and arranging glass rods or glass spheres coated with titanium oxide film in a liquid, pouring a solution containing harmful substances into this, and irradiating light to decompose. .
【0003】[0003]
【発明が解決しようとする課題】しかしながら、前記従
来の酸化チタン粉体を液中に分散させる方法は、粉体と
液体を分離するために下流側にろ過膜を設ける必要があ
り、そのために圧力損失が高くなるという欠点を有す
る。また、粉体を液中に分散させると光が最外層のみで
吸収され、照射光が内部まで透過しにくくなり、処理効
率が小さくなるという欠点を有する。また、前記従来の
酸化チタン膜を被覆したガラス棒やガラス球を用いる方
法は、粉体を回収するろ過膜を設置する必要はなく、光
も透過するが、水との接触界面が少なくなり処理効率が
悪いという欠点を有する。本発明は前記欠点を解消する
ことのできる液中有害物質処理用光触媒とそれを利用し
た液中有害物質処理装置を提供することを目的とする。However, in the conventional method of dispersing the titanium oxide powder in the liquid, it is necessary to provide a filtration membrane on the downstream side in order to separate the powder and the liquid. It has the disadvantage of high losses. Further, when the powder is dispersed in the liquid, the light is absorbed only in the outermost layer, and it becomes difficult for the irradiation light to penetrate to the inside, resulting in a drawback that the processing efficiency is reduced. Further, the conventional method using a glass rod or a glass sphere coated with a titanium oxide film does not require the installation of a filtration film for recovering powder and allows light to pass through, but the contact interface with water is reduced and the treatment is performed. It has the drawback of being inefficient. It is an object of the present invention to provide a photocatalyst for treating harmful substances in liquid and a device for treating harmful substances in liquid using the photocatalyst capable of eliminating the above-mentioned drawbacks.
【0004】[0004]
【課題を解決するための手段】前記目的を達成するため
に、本発明の液中有害物質処理用光触媒は、光透過性を
有する耐熱性繊維からなる織布の各耐熱性繊維自体に酸
化チタンの被膜を形成したことを特徴とする。In order to achieve the above object, the photocatalyst for treating harmful substances in a liquid of the present invention comprises titanium oxide on each heat-resistant fiber itself of a woven fabric made of heat-resistant fiber having light transmittance. Is formed.
【0005】前記酸化チタンの被膜は、該織布に光硬化
樹脂と加熱により酸化チタンになる前駆体とを相溶性の
ある溶媒に溶解してなる溶液を保持させ、該保持された
溶液中の光硬化樹脂を光硬化させた後、該織布を乾燥
し、焼成することにより形成したものであることが好ま
しい。The titanium oxide film is obtained by holding a solution obtained by dissolving a photocurable resin and a precursor which becomes titanium oxide by heating in a compatible solvent in the woven fabric, and holding the solution in the retained solution. It is preferably formed by photocuring a photocurable resin, then drying and firing the woven fabric.
【0006】前記光透過性を有する耐熱性繊維からなる
織布としてはガラス繊維からなる織布が好ましく、また
その目付け(g/m2 )は、特に限定されるものではな
いが、取扱い性や分解効率の観点から、一般には100
〜900g/m2 程度のものを用いる。尚、ガラス繊維
の種類としては、石英ガラス、高石英ガラス、Eガラ
ス、Cガラス、Sガラス、Aガラス等、光を透過させる
ものならばどのような組成でも構わないが、経済性の観
点からEガラス繊維が好ましい。また、アルミナ繊維
等、光透過性を有する耐熱性繊維であれば、織布を構成
する繊維の種類は何ら限定されるものではない。また、
耐熱性繊維の平均繊維径は、特に限定されるものではな
いが、製造可能でしかも液体との接触面積を確保して効
率を得るため5〜15ミクロンが好ましい。また、織布
の織り方は平織、綾織、朱子織など、どのような織り方
でも構わないが、光透過性の観点から平織が好ましい。
また、打込み密度、厚さ、引張強度は特に限定されるも
のではないが、液体に対する強度の観点から、各々タ
テ、ヨコ共に10〜80本/25mm、0.01〜2.
0mm、5kgf/25mm巾以上が好ましい。As the woven cloth made of the heat-resistant fiber having light transmittance, a woven cloth made of glass fiber is preferable, and its basis weight (g / m 2 ) is not particularly limited, but it is easy to handle or From the viewpoint of decomposition efficiency, generally 100
The thing of about 900 g / m 2 is used. The type of glass fiber may be any composition that transmits light, such as quartz glass, high quartz glass, E glass, C glass, S glass, and A glass, but from the viewpoint of economy. E glass fibers are preferred. Further, as long as it is a heat-resistant fiber having a light-transmitting property such as an alumina fiber, the kind of fiber constituting the woven fabric is not limited at all. Also,
The average fiber diameter of the heat resistant fiber is not particularly limited, but is preferably 5 to 15 microns in order to be manufacturable and to secure the contact area with the liquid to obtain efficiency. The weave may be any weave, such as plain weave, twill weave and satin weave, but plain weave is preferred from the viewpoint of light transmission.
Further, the implantation density, thickness, and tensile strength are not particularly limited, but from the viewpoint of strength against liquid, both vertical and horizontal are 10 to 80 pieces / 25 mm, 0.01 to 2.
A width of 0 mm, 5 kgf / 25 mm or more is preferable.
【0007】前記光硬化樹脂は、紫外線硬化樹脂、放射
線硬化樹脂等、光エネルギーで硬化する樹脂であればよ
い。The photocurable resin may be a resin curable by light energy, such as an ultraviolet curable resin or a radiation curable resin.
【0008】前記加熱により酸化チタンとなる前駆体と
しては、チタンアルコキシド、チタン塩化物、チタン硫
化物、チタン金属酢酸塩等が使用できるが、前記光硬化
樹脂との相溶性の関係から、アルコール類を相溶性溶媒
とする場合はチタンアルコキシド、水を相溶性溶媒とす
る場合はチタン塩化物を選択することが好ましい。しか
し、前記前駆体と光硬化樹脂が相溶する場合はどのよう
な組み合わせを選択しても構わない。Titanium alkoxide, titanium chloride, titanium sulfide, titanium metal acetate, etc. can be used as the precursor which becomes titanium oxide when heated, but alcohols are used because of their compatibility with the photocurable resin. It is preferable to select titanium alkoxide when using as a compatible solvent and titanium chloride when using water as a compatible solvent. However, when the precursor and the photocurable resin are compatible with each other, any combination may be selected.
【0009】このようにして得られた光硬化樹脂と酸化
チタン前駆体を含んだ溶液に、前記織布を浸漬するなど
して、織布に溶液を保持させた後、光硬化樹脂が光硬化
するエネルギーを有する光を照射し、酸化チタンの前駆
体を含む溶液を硬化させる。After the woven cloth is held in the woven cloth by soaking the woven cloth in the solution containing the photocurable resin and the titanium oxide precursor thus obtained, the photocurable resin is photocured. The solution containing the titanium oxide precursor is cured by irradiating light having the energy required to cure the solution.
【0010】その後、乾燥機などにて織布を乾燥する。
このときの乾燥温度は40〜80℃の範囲で行うのが好
ましい。Then, the woven cloth is dried by a dryer or the like.
The drying temperature at this time is preferably in the range of 40 to 80 ° C.
【0011】次に、乾燥した織布を焼成することによ
り、光硬化樹脂や酸化チタンの前駆体を構成している有
機残基を取り除く。この焼成で酸化チタンの前駆体は酸
化チタンに変化し、織布を構成する繊維一本一本に酸化
チタンが被覆された織布が得られる。Next, the dried woven fabric is fired to remove the organic residues constituting the photocurable resin and the precursor of titanium oxide. By this firing, the titanium oxide precursor is changed to titanium oxide, and a woven fabric in which the fibers constituting the woven fabric are coated with titanium oxide is obtained.
【0012】酸化チタン被膜の厚みは、膜の接着性や光
透過性から1ミクロン以下が好ましい。1ミクロンを越
えると膜の剥離が生じ、水の濁りや処理効率の低下が生
じる。また、光の透過性も悪くなり、織布内部まで光が
到達しにくくなり分解効率的にも好ましくない。また、
織布全体から考えると、被覆した酸化チタンの被覆量は
織布全体に対して40重量%以下が好ましい。この場合
も、40重量%を越えると光の透過性が悪くなり、酸化
チタンの剥離も生ずるため好ましくない。尚、酸化チタ
ンの厚みは、溶液の酸化チタン前駆体の濃度を調整する
か、前記被膜作成工程を繰り返すことにより変化させる
ことが可能である。The thickness of the titanium oxide coating is preferably 1 micron or less in view of the adhesiveness and light transmittance of the film. If it exceeds 1 micron, peeling of the film occurs, resulting in turbidity of water and deterioration of treatment efficiency. In addition, the light transmittance also deteriorates, and it becomes difficult for light to reach the inside of the woven fabric, which is not preferable in terms of decomposition efficiency. Also,
Considering the woven fabric as a whole, the coating amount of the coated titanium oxide is preferably 40% by weight or less with respect to the entire woven fabric. Also in this case, if it exceeds 40% by weight, the light transmittance is deteriorated and the titanium oxide is also peeled off, which is not preferable. The thickness of titanium oxide can be changed by adjusting the concentration of the titanium oxide precursor in the solution or by repeating the film forming step.
【0013】また、酸化チタンに貴金属類を担持するの
が好ましく、この場合の貴金属類としては、白金、パラ
ジウム、ロジウム、金、銀、ルテニウム等の金属及びそ
の金属酸化物が好ましい。担持方法は、光析出法を用い
れば容易である。Further, it is preferable to support precious metals on titanium oxide. In this case, the precious metals are preferably metals such as platinum, palladium, rhodium, gold, silver and ruthenium and metal oxides thereof. The supporting method is easy if a photodeposition method is used.
【0014】本発明の液中有害物質処理装置は有害物質
を含む溶液を通過させる容器内に前記液中有害物質処理
用光触媒を配置すると共に該液中有害物質処理用光触媒
に光を照射するための光源を備えたことを特徴とする。
前記装置は例えば、容器をプラスチック類、ホウ珪酸塩
ガラス或いは、石英ガラス等による透明容器に構成し
て、該容器の外部から光を照射するようにしてもよく、
或いは、該容器を特に透明容器にすることなく該容器内
に光源を配置するようにしてもよい。また、光源は低圧
水銀灯やブラックライト蛍光灯等、光硬化樹脂が光硬化
するエネルギーを有するものであれば任意である。In the apparatus for treating harmful substances in liquid of the present invention, the photocatalyst for treating harmful substances in liquid is placed in a container through which a solution containing a harmful substance is passed and the photocatalyst for treating harmful substances in liquid is irradiated with light. It is equipped with a light source of.
In the above apparatus, for example, the container may be configured as a transparent container made of plastics, borosilicate glass, quartz glass or the like, and light may be irradiated from the outside of the container,
Alternatively, the light source may be arranged in the container without forming the container as a transparent container. Further, the light source may be any one such as a low pressure mercury lamp or a black light fluorescent lamp as long as it has energy for photo-curing the photo-curing resin.
【0015】[0015]
【作用】織布を構成する各光透過性を有する耐熱性繊維
自体に酸化チタンの被膜を形成した織布は、ガラス棒や
ガラス球に被覆した場合に比べて被膜の比表面積が数段
大きいため、水との接触面積が大きくなる。また、光透
過性を有する織布に酸化チタン膜を被覆した材料ゆえ、
粒子を分散させた如く光が吸収されることが少なく、織
布の内部まで充分に光が透過する。そのため、液中の有
害物質の分解等の処理効率が大幅に高くなる。また、酸
化チタンの被膜は前記の如く耐熱性繊維一本一本に、均
一にかつ強固に被覆されているため、高効率にもかかわ
らず酸化チタンの剥離が無く、従って水の濁りもなく、
粒子状物を回収する必要もない。[Function] A woven fabric having a titanium oxide coating formed on the heat-resistant fibers themselves having various light-transmitting properties, which forms the woven fabric, has a specific surface area several times larger than that when coated on a glass rod or glass sphere. Therefore, the contact area with water becomes large. In addition, since the woven cloth having light transmittance is coated with a titanium oxide film,
Light is hardly absorbed as if the particles were dispersed, and the light is sufficiently transmitted to the inside of the woven cloth. Therefore, the processing efficiency such as decomposition of harmful substances in the liquid is significantly increased. Further, since the titanium oxide film is uniformly and firmly coated on each heat-resistant fiber as described above, there is no peeling of titanium oxide despite the high efficiency, and therefore no turbidity of water,
There is no need to recover particulate matter.
【0016】この酸化チタンの表面に貴金属を担持させ
ると、電気化学的に有害物質の分解反応が促進されるた
め好ましい。It is preferable to support the noble metal on the surface of the titanium oxide, because the decomposition reaction of harmful substances is electrochemically promoted.
【0017】従来より知られているところの、溶液に被
膜形成対象物を浸漬して被膜を形成する方法は、ガラス
棒、ガラス球、ガラス板等の単一物に酸化チタン被膜を
形成するのには適する。この方法で多くの繊維で構成さ
れている織布に一度に酸化チタン膜を被覆する場合は、
織布を酸化チタン前駆体溶液に浸漬し、該溶液を保持し
た織布を乾燥し、焼成するが、この場合、溶媒が乾燥さ
れると同時に酸化チタン前駆体も表面に移行し、いわゆ
るマイグレーションが起きるため、酸化チタン前駆体は
織布の表面に形成され、織布内部の繊維には被覆されな
い。しかしながら、織布に溶液を保持させた後、溶液を
乾燥する前に酸化チタン前駆体と相溶媒を含む溶液を光
照射により光硬化樹脂とともに固定させると、次の段階
の乾燥においては相溶媒のみが乾燥され、その結果、前
記従来法のように、相溶媒の乾燥と同時に酸化チタン前
駆体が表面に移行することがなく、織布内部の繊維の表
面にもそのまま残存する。この乾燥により、被覆物は織
布を構成する繊維全体を固定していた状態から単一繊維
の間に亀裂が生じ、繊維一本一本の周囲に酸化チタン前
駆体と光硬化樹脂が被覆された状態になり、繊維が分離
する。この状態の織布を焼成することにより、光硬化樹
脂が除去され、酸化チタン前駆体のゲルが収縮し、更に
酸化チタン前駆体が酸化チタンに変化し、繊維の垂直方
向に収縮して、繊維一本一本に均一にかつ強固に酸化チ
タンが被覆されることになる。また、前記光触媒はフレ
キシブルであり、どのような形状の容器にも設置するこ
とができる。A conventionally known method of immersing a film-forming object in a solution to form a film is to form a titanium oxide film on a single substance such as a glass rod, a glass ball or a glass plate. Suitable for When coating a titanium oxide film at once on a woven fabric composed of many fibers by this method,
The woven cloth is dipped in a titanium oxide precursor solution, and the woven cloth holding the solution is dried and fired. In this case, the solvent is dried and the titanium oxide precursor also migrates to the surface, so-called migration occurs. As it occurs, the titanium oxide precursor forms on the surface of the woven fabric and does not cover the fibers inside the woven fabric. However, when the solution containing the titanium oxide precursor and the compatibilizer is fixed together with the photocurable resin by light irradiation after the solution is held on the woven fabric and before the solution is dried, only the compatibilizer is used in the next drying step. As a result, unlike the conventional method, the titanium oxide precursor does not migrate to the surface at the same time as the drying of the compatibilizer, and remains on the surface of the fiber inside the woven fabric as it is. By this drying, the coating causes cracks between single fibers from the state where all the fibers constituting the woven fabric are fixed, and the titanium oxide precursor and the photocurable resin are coated around each fiber. And the fibers separate. By firing the woven fabric in this state, the photocurable resin is removed, the gel of the titanium oxide precursor is contracted, the titanium oxide precursor is converted to titanium oxide, and the fibers are contracted in the vertical direction of the fiber. Titanium oxide is uniformly and strongly coated on each one. Further, the photocatalyst is flexible and can be installed in a container of any shape.
【0018】[0018]
【実施例】以下、本発明の実施例を図面に基づき説明す
る。図1は本発明液中有害物質処理装置の一実施例を示
すもので、図中1は透明石英管からなる容器を示し、該
容器1内には液中有害物質処理用光触媒2が配置され、
該容器1内にポンプ3を介して有害物質を含む溶液を循
環通過させるようにし、容器1の近傍に設けた光源4か
ら光を照射して有害物質を処理するように構成してあ
る。尚、図中5は集光用ミラー、6は有害物質を処理さ
れた溶液を取り出したり、或いは新たな有害物質を含む
溶液を供給するための取入取出口を示す。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 shows an embodiment of the apparatus for treating harmful substances in liquid of the present invention. In the figure, reference numeral 1 denotes a container made of a transparent quartz tube, in which a photocatalyst 2 for treating harmful substances in liquid is arranged. ,
A solution containing a harmful substance is circulated in the container 1 via a pump 3, and light is emitted from a light source 4 provided in the vicinity of the container 1 to treat the harmful substance. In the figure, 5 is a light collecting mirror, and 6 is an inlet / outlet for taking out a solution treated with a harmful substance or supplying a solution containing a new harmful substance.
【0019】次に前記装置の使用例に即し、具体的な実
施例を比較例と共に説明する。 (実施例1)平均繊維径7ミクロンのEガラスモノフィ
ラメント(単一繊維)約1000本からなるヤーンを織
ってなる平織の目付け500g/m2 、打込み密度タテ
20本/25mm、ヨコ25本/25mm、厚さ0.5
mm、引張強度100kgf/25mmのガラス織布
(ガラスクロス)を、酸化チタン前駆体であるチタンイ
ソプロポキシド76gと紫外線硬化樹脂40g及び濃塩
酸1gをエチルアルコール83gに溶解した溶液に浸漬
した。この溶液を保持させた織布を溶液から取り出し、
水銀ランプを用いて紫外線を織布に照射し、光硬化樹脂
を硬化させた。次に、60℃で1時間乾燥し、その後、
毎分1℃の昇温速度で400℃まで昇温し、400℃で
1時間保持することにより光硬化樹脂を完全に除去し、
更に500℃で5時間焼成した。この処理でチタンイソ
プロポキシドはアナターゼ型を主体とする酸化チタンに
変化し、更に織布を構成する繊維の一本一本に均一に、
かつ強固に酸化チタンが被覆できた。この場合の酸化チ
タンの膜厚は約0.3ミクロンであり、また、被覆した
酸化チタン膜の織布全体に対する量の比率は18重量%
であった。この織布(触媒)を直径12mm、長さ50
0mmの透明石英管に詰め、反応液を通し、ポンプによ
り循環させた。反応液は再蒸留水に200mg/リット
ルのクロロホルムを溶解させた水溶液で、液温40℃で
低圧水銀灯により光照射した。約5時間の光照射でクロ
ロホルムの95%が分解された。この場合、水の濁りは
なかった。次に反応液を取り替え、クロロホルムを同量
溶解させた水溶液で同じ試験を行った。この試験を50
回繰り返したが、水の濁りはなく、また、クロロホルム
の分解効率は最初の値から低下することなく、高効率を
保っていた。Next, a concrete embodiment will be described together with a comparative example in accordance with a usage example of the apparatus. (Example 1) A plain weave having a mean fiber diameter of 7 microns and a yarn made of about 1000 E-glass monofilaments (single fiber) having a basis weight of 500 g / m 2 , a shot density vertical 20/25 mm, and a horizontal 25/25 mm. , Thickness 0.5
A glass woven fabric (glass cloth) having a tensile strength of 100 kgf / 25 mm and a tensile strength of 100 kgf / 25 mm was immersed in a solution prepared by dissolving 76 g of titanium isopropoxide as a titanium oxide precursor, 40 g of an ultraviolet curable resin, and 1 g of concentrated hydrochloric acid in 83 g of ethyl alcohol. Remove the woven fabric holding this solution from the solution,
The woven cloth was irradiated with ultraviolet rays using a mercury lamp to cure the photocurable resin. Then dry at 60 ° C for 1 hour, then
The photo-curing resin was completely removed by raising the temperature to 400 ° C. at a temperature rising rate of 1 ° C./min and holding at 400 ° C. for 1 hour.
Further, it was baked at 500 ° C. for 5 hours. By this treatment, titanium isopropoxide changes to titanium oxide mainly composed of anatase type, and evenly on each fiber constituting the woven fabric,
Moreover, the titanium oxide could be firmly coated. In this case, the film thickness of titanium oxide was about 0.3 μm, and the ratio of the coated titanium oxide film to the entire woven fabric was 18% by weight.
Met. This woven cloth (catalyst) has a diameter of 12 mm and a length of 50.
The reaction solution was passed through a 0 mm transparent quartz tube and circulated by a pump. The reaction solution was an aqueous solution in which 200 mg / liter of chloroform was dissolved in double-distilled water, and light irradiation was performed with a low-pressure mercury lamp at a solution temperature of 40 ° C. After irradiation with light for about 5 hours, 95% of chloroform was decomposed. In this case, there was no turbidity in the water. Next, the reaction solution was replaced, and the same test was performed with an aqueous solution in which the same amount of chloroform was dissolved. 50 this test
Repeated times, there was no turbidity in water, and the decomposition efficiency of chloroform did not decrease from the initial value, maintaining high efficiency.
【0020】(実施例2)実施例1で作成した織布(触
媒)を直径12mm、長さ500mmの透明石英管に詰
め、反応液を通し、ポンプにより循環させた。反応液は
再蒸留水に200mg/リットルのトリクロロエチレン
を溶解させた水溶液で、液温40℃で低圧水銀灯により
光照射した。約1時間の光照射でトリクロロエチレンの
95%が分解された。この場合、水の濁りはなかった。
次に反応液を取り替え、トリクロロエチレンを同量溶解
させた水溶液で同じ試験を行った。この試験を50回繰
り返したが、水の濁りはなく、また、トリクロロエチレ
ンの分解効率は最初の値から低下することなく、高効率
を保っていた。(Example 2) The woven fabric (catalyst) prepared in Example 1 was packed in a transparent quartz tube having a diameter of 12 mm and a length of 500 mm, the reaction solution was passed through and circulated by a pump. The reaction solution was an aqueous solution in which 200 mg / liter of trichlorethylene was dissolved in double-distilled water, and light irradiation was performed with a low-pressure mercury lamp at a solution temperature of 40 ° C. Light irradiation for about 1 hour decomposed 95% of trichlorethylene. In this case, there was no turbidity in the water.
Next, the reaction solution was replaced, and the same test was performed with an aqueous solution in which the same amount of trichlorethylene was dissolved. This test was repeated 50 times, but there was no turbidity in water, and the decomposition efficiency of trichlorethylene did not decrease from the initial value, and high efficiency was maintained.
【0021】(実施例3)実施例1で作成した織布(触
媒)を直径12mm、長さ500mmの透明石英管に詰
め、反応液を通し、ポンプにより循環させた。反応液は
再蒸留水に10ppmのシアンイオンを溶解させた水溶
液で、液温40℃で低圧水銀灯により光照射した。約1
時間の光照射でシアンイオンの95%が無機化され、無
害物質に変わった。この場合、水の濁りはなかった。次
に反応液を取り替え、シアンイオンを同量溶解させた水
溶液で同じ試験を行った。この試験を50回繰り返した
が、水の濁りはなく、また、シアンイオンの除去率は最
初の値から低下することなく、高効率を保っていた。(Example 3) The woven fabric (catalyst) prepared in Example 1 was packed in a transparent quartz tube having a diameter of 12 mm and a length of 500 mm, the reaction solution was passed through and circulated by a pump. The reaction solution was an aqueous solution prepared by dissolving 10 ppm of cyanide ions in double-distilled water, and was irradiated with light by a low-pressure mercury lamp at a solution temperature of 40 ° C. About 1
After irradiation with light for 95 hours, 95% of the cyan ions were mineralized and turned into harmless substances. In this case, there was no turbidity in the water. Next, the reaction solution was replaced, and the same test was performed with an aqueous solution in which the same amount of cyan ions was dissolved. This test was repeated 50 times, but there was no turbidity in the water, and the cyan ion removal rate did not decrease from the initial value, and high efficiency was maintained.
【0022】(実施例4)実施例1で作成した織布(触
媒)を直径12mm、長さ500mmの透明石英管に詰
め、反応液を通し、ポンプにより循環させた。反応液は
再蒸留水に200mg/リットルの農薬(BPMC)を
溶解させた水溶液で、液温40℃で低圧水銀灯により光
照射した。約2時間の光照射で農薬(BPMC)の95
%が除去された。この場合、水の濁りはなかった。次に
反応液を取り替え、農薬(BPMC)を同量溶解させた
水溶液で同じ試験を行った。この試験を50回繰り返し
たが、水の濁りはなく、また、除去効率は最初の値から
低下することなく、高効率を保っていた。(Example 4) The woven fabric (catalyst) prepared in Example 1 was packed in a transparent quartz tube having a diameter of 12 mm and a length of 500 mm, the reaction solution was passed through, and circulated by a pump. The reaction solution was an aqueous solution prepared by dissolving 200 mg / liter of a pesticide (BPMC) in double-distilled water, and was irradiated with light by a low-pressure mercury lamp at a solution temperature of 40 ° C. 95% of pesticide (BPMC) by light irradiation for about 2 hours
% Removed. In this case, there was no turbidity in the water. Next, the reaction solution was replaced, and the same test was conducted with an aqueous solution in which the same amount of pesticide (BPMC) was dissolved. This test was repeated 50 times, but there was no turbidity in the water, and the removal efficiency did not decrease from the initial value, maintaining high efficiency.
【0023】(実施例5)実施例1で作成した酸化チタ
ンを被覆した織布(触媒)を塩化白金酸水溶液に浸漬し
て酸化チタンに対して10重量%の白金を担持し、光を
照射することにより、白金が酸化チタンの表面に析出し
た織布を作成した。この織布(触媒)を直径12mm、
長さ500mmの透明石英管に詰め、反応液を通し、ポ
ンプにより循環させた。反応液は再蒸留水に200mg
/リットルのクロロホルムを溶解させた水溶液で、液温
40℃で低圧水銀灯により光照射した。約30分の光照
射でクロロホルムの95%が分解された。この場合、水
の濁りはなかった。次に反応液を取り替え、クロロホル
ムを同量溶解させた水溶液で同じ試験を行った。この試
験を50回繰り返したが、水の濁りはなく、また、クロ
ロホルムの分解効率は最初の値から低下することなく、
高効率を保っていた。(Example 5) The woven fabric (catalyst) coated with titanium oxide prepared in Example 1 was immersed in an aqueous solution of chloroplatinic acid to carry 10% by weight of platinum on the titanium oxide and irradiated with light. By doing so, a woven fabric in which platinum was deposited on the surface of titanium oxide was prepared. This woven cloth (catalyst) has a diameter of 12 mm,
The reaction solution was passed through a transparent quartz tube having a length of 500 mm, which was then circulated by a pump. 200 mg of reaction liquid in double-distilled water
The solution was irradiated with light from a low pressure mercury lamp at a liquid temperature of 40 ° C. Light irradiation for about 30 minutes decomposed 95% of chloroform. In this case, there was no turbidity in the water. Next, the reaction solution was replaced, and the same test was performed with an aqueous solution in which the same amount of chloroform was dissolved. This test was repeated 50 times, but there was no turbidity of water, and the decomposition efficiency of chloroform did not decrease from the initial value.
It kept high efficiency.
【0024】(比較例1)実施例1で用いたガラス織布
を、酸化チタンの前駆体であるチタニアゾルに浸漬した
後、60℃で1時間乾燥し、その後500℃で5時間焼
成した。この処理でチタニアゾルはアナターゼ型を主体
とする酸化チタンに変化したが、マイグレーションが起
こり、酸化チタンは織布の表面付近に多く会合し、繊維
間のブリッジングや粒子の塊が生じ、粉落ちがあった。
この場合、被覆した酸化チタンの織布全体に対する量の
比率は50重量%であった。この織布(触媒)を直径1
2mm、長さ500mmの透明石英管に詰め、反応液を
通し、ポンプにより循環させた。反応液は再蒸留水に2
00mg/リットルのクロロホルムを溶解させた水溶液
で、液温40℃で低圧水銀灯により光照射した。約5時
間の光照射でクロロホルムの85%が分解されたが、酸
化チタンの脱落により水がかなり濁った。次に反応液を
取り替え、クロロホルムを同量溶解させた水溶液で同じ
試験を行った。2回目は同条件で60%が分解し、3回
目は50%が分解するとういうように、反応液を取り替
えて試験を行うたびに酸化チタンの脱落が起き、20回
目以降は0%となり、触媒機能を失っていた。Comparative Example 1 The glass woven fabric used in Example 1 was dipped in titania sol which is a precursor of titanium oxide, dried at 60 ° C. for 1 hour, and then fired at 500 ° C. for 5 hours. By this treatment, titania sol changed to titanium oxide mainly composed of anatase type, but migration occurred, titanium oxide was often associated near the surface of the woven fabric, bridging between fibers and agglomeration of particles were generated, and powder falling was caused. there were.
In this case, the ratio of the amount of coated titanium oxide to the entire woven fabric was 50% by weight. This woven fabric (catalyst) has a diameter of 1
The reaction solution was passed through a transparent quartz tube having a length of 2 mm and a length of 500 mm, which was circulated by a pump. The reaction solution is 2 in distilled water.
It was irradiated with a low-pressure mercury lamp at a liquid temperature of 40 ° C. with an aqueous solution in which 00 mg / liter of chloroform was dissolved. After irradiating with light for about 5 hours, 85% of chloroform was decomposed, but the water was considerably turbid due to the loss of titanium oxide. Next, the reaction solution was replaced, and the same test was performed with an aqueous solution in which the same amount of chloroform was dissolved. The second time, 60% decomposes under the same conditions, and the third time 50% decomposes.Titanium oxide drops off every time the reaction solution is replaced and the test is performed, and it becomes 0% after the 20th time. It had lost its catalytic function.
【0025】[0025]
【発明の効果】このように、本発明による液中有害物質
処理用光触媒は、光透過性が良く、かつ水との接触面積
が大きいため、液中の有害物質を高効率で処理できると
いう効果を有する。具体的には、液中に存在するトリク
ロロエチレン、クロロホルム、ダイオキシン等の有機ハ
ロゲン化合物や、シアン、農薬成分等の分解処理をでき
るため、有機物を含んだ水を用いて超純水を作ることも
できる。また、酸化チタン触媒の酸化力は非常に強いた
め、水中に存在する菌を殺すこともできる。この例とし
ては、生体の酵素であるCoAの働きを光照射した酸化
チタンによって止めて殺菌することができる。また、織
布を構成する繊維の一本一本に均一にかつ強固に酸化チ
タン膜が被覆されているため、酸化チタンの剥離や脱落
がなく、長期に亘り高効率を維持し、また、水の濁りも
ないので粉体等を回収する必要がないという効果を有す
る。また、フレキシブル性を有するので、複雑な形状の
容器にも適用することが可能となり、カラム化も可能で
あるという効果を有する。As described above, the photocatalyst for treating harmful substances in liquid according to the present invention has good light transmittance and has a large contact area with water, so that the harmful substances in liquid can be treated with high efficiency. Have. Specifically, since it is possible to decompose organic halogen compounds such as trichloroethylene, chloroform, dioxin, etc. existing in the liquid, cyanide, pesticide components, etc., it is possible to make ultrapure water using water containing organic substances. . Moreover, since the oxidizing power of the titanium oxide catalyst is very strong, it is possible to kill bacteria existing in water. As an example of this, the action of CoA, which is an enzyme of the living body, can be stopped by light-irradiated titanium oxide and sterilized. In addition, since the titanium oxide film is uniformly and firmly coated on each of the fibers constituting the woven fabric, there is no peeling or dropping of the titanium oxide, and high efficiency is maintained for a long period of time. Since it has no turbidity, it has an effect that it is not necessary to collect powder or the like. Further, since it has flexibility, it can be applied to a container having a complicated shape and can be columnized.
【図1】図1は本発明液中有害物質処理装置の一実施例
の説明線図である。FIG. 1 is an explanatory diagram of one embodiment of the liquid hazardous substance treating apparatus of the present invention.
1 容器 2 液中有害物質処理用光触媒 3 ポンプ 4 光源 5 集光用ミラー 6 取入取出口 1 Container 2 Photocatalyst for Treatment of Hazardous Substances in Liquid 3 Pump 4 Light Source 5 Focusing Mirror 6 Inlet / Outlet
───────────────────────────────────────────────────── フロントページの続き (72)発明者 伊藤 公紀 東京都目黒区鷹番1−14−11−106 (72)発明者 川島 孝一 岐阜県不破郡垂井町630 日本無機株式会 社垂井工場内 (72)発明者 増田 竜司 岐阜県不破郡垂井町630 日本無機株式会 社垂井工場内 (72)発明者 高橋 渉 岐阜県不破郡垂井町630 日本無機株式会 社垂井工場内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Koki Ito 1-14-11-106 Takaban, Meguro-ku, Tokyo (72) Inventor Koichi Kawashima 630 Tarui-cho, Fuwa-gun, Gifu Japan Inorganic Stock Company Tarui factory (72 ) Inventor Ryuji Masuda 630 Tarui-cho, Fuwa-gun, Gifu Prefecture, Tarui Plant, Japan Inorganic Stock Company (72) Wataru Takahashi 630, Tarui-cho, Fuwa-gun, Gifu Prefecture, Tarui Plant, Japan Inorganic Stock Company
Claims (5)
布の各耐熱性繊維自体に酸化チタンの被膜を形成したこ
とを特徴とする液中有害物質処理用光触媒。1. A photocatalyst for treating harmful substances in a liquid, characterized in that a film of titanium oxide is formed on each heat-resistant fiber itself of a woven fabric made of heat-resistant fiber having light transmittance.
を特徴とする請求項1記載の液中有害物質処理用光触
媒。2. The photocatalyst for treating harmful substances in a liquid according to claim 1, wherein the heat resistant fiber is glass fiber.
化樹脂と加熱により酸化チタンになる前駆体とを相溶性
のある溶媒に溶解してなる溶液を保持させ、該保持され
た溶液中の光硬化樹脂を光硬化させた後、該織布を乾燥
し、焼成することにより形成したものであることを特徴
とする請求項1または2記載の液中有害物質処理用光触
媒。3. The titanium oxide coating film holds a solution prepared by dissolving a photocurable resin and a precursor which becomes titanium oxide by heating in a compatible solvent in the woven fabric, and the retained solution. The photocatalyst for treating a harmful substance in a liquid according to claim 1 or 2, which is formed by photocuring the photocurable resin therein and then drying and firing the woven fabric.
ことを特徴とする請求項1乃至3の何れかに記載の液中
有害物質処理用光触媒。4. The photocatalyst for treating a harmful substance in a liquid according to claim 1, wherein a noble metal is supported on the titanium oxide.
に前記請求項1乃至4の何れかに記載の液中有害物質処
理用光触媒を配置すると共に該液中有害物質処理用光触
媒に光を照射するための光源を備えたことを特徴とする
液中有害物質処理装置。5. The photocatalyst for treating a harmful substance in liquid according to any one of claims 1 to 4 is arranged in a container through which a solution containing a harmful substance is passed, and the photocatalyst for treating a harmful substance in liquid is irradiated with light. An apparatus for treating harmful substances in liquid, comprising a light source for irradiating.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14369292A JP3358826B2 (en) | 1992-05-11 | 1992-05-11 | Photocatalyst for treating toxic substances in liquids and equipment for treating toxic substances in liquids |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14369292A JP3358826B2 (en) | 1992-05-11 | 1992-05-11 | Photocatalyst for treating toxic substances in liquids and equipment for treating toxic substances in liquids |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0796202A true JPH0796202A (en) | 1995-04-11 |
| JP3358826B2 JP3358826B2 (en) | 2002-12-24 |
Family
ID=15344745
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14369292A Expired - Lifetime JP3358826B2 (en) | 1992-05-11 | 1992-05-11 | Photocatalyst for treating toxic substances in liquids and equipment for treating toxic substances in liquids |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3358826B2 (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06315614A (en) * | 1993-03-11 | 1994-11-15 | Agency Of Ind Science & Technol | Method for removing contaminants and cleaning material |
| JP2004002176A (en) * | 2002-04-16 | 2004-01-08 | Nippon Sheet Glass Co Ltd | Photocatalyst-supporting glass fiber cloth, method for producing the same, and air filter device using the same |
| US6939611B2 (en) | 1994-10-31 | 2005-09-06 | Kanagawa Academy Of Science And Technology | Window glass employing titanium dioxide photocatalyst |
| WO2007004592A1 (en) * | 2005-06-30 | 2007-01-11 | K2R Co., Ltd. | Method for formation of alumina coating film, alumina fiber, and gas treatment system comprising the alumina fiber |
| US9561490B2 (en) | 2005-06-30 | 2017-02-07 | K2R Co., Ltd. | Method for manufacturing titania coated alumina fiber aggregate |
| CN116809051A (en) * | 2023-06-28 | 2023-09-29 | 重庆长安汽车股份有限公司 | Preparation method of light-transmitting leather with photocatalysis function |
-
1992
- 1992-05-11 JP JP14369292A patent/JP3358826B2/en not_active Expired - Lifetime
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06315614A (en) * | 1993-03-11 | 1994-11-15 | Agency Of Ind Science & Technol | Method for removing contaminants and cleaning material |
| US6939611B2 (en) | 1994-10-31 | 2005-09-06 | Kanagawa Academy Of Science And Technology | Window glass employing titanium dioxide photocatalyst |
| US7157840B2 (en) | 1994-10-31 | 2007-01-02 | Kanagawa Academy Of Science And Technology | Illuminating devices employing titanium dioxide photocatalysts |
| US7327074B2 (en) | 1994-10-31 | 2008-02-05 | Kanagawa Academy Of Science And Technology | Illuminating devices employing titanium dioxide photocatalysts |
| JP2004002176A (en) * | 2002-04-16 | 2004-01-08 | Nippon Sheet Glass Co Ltd | Photocatalyst-supporting glass fiber cloth, method for producing the same, and air filter device using the same |
| WO2007004592A1 (en) * | 2005-06-30 | 2007-01-11 | K2R Co., Ltd. | Method for formation of alumina coating film, alumina fiber, and gas treatment system comprising the alumina fiber |
| JPWO2007004592A1 (en) * | 2005-06-30 | 2009-01-29 | 有限会社K2R | Alumina coating forming method, alumina fiber, and gas treatment apparatus equipped with the same |
| US9561490B2 (en) | 2005-06-30 | 2017-02-07 | K2R Co., Ltd. | Method for manufacturing titania coated alumina fiber aggregate |
| CN116809051A (en) * | 2023-06-28 | 2023-09-29 | 重庆长安汽车股份有限公司 | Preparation method of light-transmitting leather with photocatalysis function |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3358826B2 (en) | 2002-12-24 |
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