JP2004154742A - Water treatment apparatus and water treatment method - Google Patents

Water treatment apparatus and water treatment method Download PDF

Info

Publication number
JP2004154742A
JP2004154742A JP2002325207A JP2002325207A JP2004154742A JP 2004154742 A JP2004154742 A JP 2004154742A JP 2002325207 A JP2002325207 A JP 2002325207A JP 2002325207 A JP2002325207 A JP 2002325207A JP 2004154742 A JP2004154742 A JP 2004154742A
Authority
JP
Japan
Prior art keywords
water
treated
ozone
titanium
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
Application number
JP2002325207A
Other languages
Japanese (ja)
Other versions
JP4229363B2 (en
Inventor
Masao Tsuchiya
正夫 土屋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP2002325207A priority Critical patent/JP4229363B2/en
Publication of JP2004154742A publication Critical patent/JP2004154742A/en
Application granted granted Critical
Publication of JP4229363B2 publication Critical patent/JP4229363B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Abstract

<P>PROBLEM TO BE SOLVED: To provide a water treatment apparatus which can permanently maintain a sterilization effect by photocatalysts and are high in the sterilization effect, and a water treatment method. <P>SOLUTION: The water treatment apparatus has a pump 20 for flushing water 12 to be treated, such as bath water, and a reaction vessel 32 disposed in mid-way of piping 16 in which the water 12 to be treated flows. The reaction vessel 32 is internally provided with large-surface area materials 30, such as wire-shaped materials made of titanium or titanium alloy. An ozone generator 26 for injecting ozone into the water 12 to be treated is connected to the upstream side of the materials 30 and a UV light source 34 for irradiating the materials 30 with UV rays is disposed. The materials 30 made of the titanium or titanium alloy form the photocatalysts of titanium dioxide at all times as the titanium atoms of the materials are oxidized by the ozone even if the photocatalysts of the titanium dioxide on the surfaces are peeled off. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明の属する技術分野】
この発明は、浴槽水、生活排水、飲料水、プール水、冷却水、洗浄水、貯留水、養殖用水、産業廃水などの水を殺菌処理等する水処理装置および水処理方法に関する。
【0002】
【従来の技術】
【特許文献1】特開平8−89725号公報
【特許文献2】特開平11−262759号公報
従来、例えば温泉や健康施設における風呂水は、循環させながら温度管理、殺菌及び浮遊物の除去等が行なわれている。この浴槽水は、鉱物粒子が入った濾過槽、オゾン注入装置による殺菌装置を介して、浴槽の水をある程度きれいにして循環ポンプにより循環させているものであった。
【0003】
上記のような構成では、大規模な浴場で殺菌に必要なオゾン量が多く高濃度のオゾンを用いる必要がった。しかしながら高濃度のオゾンでは被処理水中に溶解しきらなかった高濃度オゾンが空気中に排出され、好ましいものでなかった。また、大規模な浴場施設の循環水の場合、循環する湯の量が多く低濃度のオゾンではオゾン発生装置が大型化し効率が悪いという問題があった。
【0004】
一方、特許文献1,2に開示されているように、被処理水を循環させる経路の途中に光触媒が設けられた反応容器を設け、この反応容器に紫外線を照射して、光触媒により被処理水中の菌を無害化するものも提案されている。この水処理装置は、酸化チタンが溶射された網を反応容器中に入れ紫外線ランプを照射して、被処理水を通過させ光触媒の作用により殺菌するものである。また、特許文献2では同様の装置を用いて、被処理水中にオゾンを含有した気体を供給する処理方法も提案されている。
【0005】
この光触媒を用いた殺菌処理等の原理は以下のようなものである。半導体物質である酸化チタン等の光触媒に波長が400nm以下の紫外光が照射されると、価電子帯に正孔が発生するとともに伝導帯に電子が生じる。この正孔の酸化電位は、フッ素、オゾン、過酸化水素等の酸化電位よりも高く、有機物は光触媒により完全に酸化分解されて最終的には二酸化炭素ガスと水、硫酸、硝酸などに完全酸化される。光触媒による酸化反応のメカニズムは、光触媒に紫外光が照射された際に生じる正孔またはこの正孔と水が反応して生じる極めて反応活性に富むヒドロオキシルラジカル(OHラジカル)により、酸化反応が起こると考えられている。このとき、紫外線が照射された際に生じる正孔と同時に発生する電子と酸素ガス等との還元反応が並行して進行する。光触媒の作用は、このような強力な酸化反応により、従来のオゾンや過酸化水素、塩素等の殺菌剤よりも強い殺菌能力を有し、有機物の分解機能も備えている。また、光照射により生じた正孔やOHラジカルの寿命はミリ秒以下と短いので、オゾンや過酸化水素等の酸化剤のように処理後に残留がなく、残留酸化剤を処理する装置が不要であるという利点がある。このようなことから、これまでに光触媒を用いた多くの水処理装置が提案されている。
【0006】
【発明が解決しようとする課題】
しかしながら、光触媒による作用は光が照射される光触媒表面のみで起こるため、効率良く処理を行うには光触媒の表面積を大きくして被処理水との接触効率を高める必要がある。また、光触媒に紫外光が照射された際に生じる正孔またはOHラジカルは寿命が短いので短時間で反応させる必要がある。また、紫外光は水に吸収されやすく、水中で減衰しやすいという問題がある。
【0007】
さらに、上記従来の技術の場合、酸化および殺菌作用は紫外線が照射された光触媒の表面のみで起こり、酸化チタン等の光触媒が表面に溶射された網の表面に接触するごく一部の被処理水のみしか処理されず、処理能力が低いものであった。また、酸化チタン等の光触媒が溶射された網は、表面の光触媒が剥離等しやすく耐久性が低い。溶射された光触媒がなくなると、光触媒としての作用がなくなり、その部分を交換しなければならないという問題があった。
【0008】
この発明は、上記従来の技術の問題点に鑑みてなされたもので、光触媒による殺菌作用を恒久的に維持することができ、殺菌作用も高い水処理装置および水処理方法を提供することを目的とする。
【0009】
【課題を解決するための手段】
この発明は、被処理水が流れる配管の途中に設けられる反応容器内にチタンまたはチタン合金製の網や線状集合体の大表面積材料を設け、この大表面積材料の表面に酸化チタンから成る光触媒を形成し、この大表面積材料の上流側で上記被処理水中にオゾンを注入し、上記大表面積材料に紫外線を照射して、オゾンにより上記被処理水を殺菌するとともに上記光触媒により殺菌を行ない、さらに上記オゾンにより、上記チタンまたはチタン合金表面に酸化チタンを常時形成可能とする水処理方法である。
【0010】
またこの発明は、被処理水を流すポンプと、被処理水が流れる配管の途中に設けられる反応容器と、この反応容器の中に設けられたチタンまたはチタン合金製の大表面積材料と、この大表面積材料の上流側で上記被処理水中にオゾンを注入するオゾン発生器等のオゾン注入手段と、上記大表面積材料に紫外線を照射する紫外線光源とを備えた水処理装置である。上記反応容器は、へーキャッチャー等の処理槽を兼用しても良い。
【0011】
【発明の実施の形態】
以下、この発明の実施の形態について図面に基づいて説明する。図1は、この発明の水処理装置の第一実施形態を示す概略図で、この実施形態の水処理装置10は、被処理水12として温泉や健康施設等において循環するお風呂の湯を処理するものである。この実施形態の水処理装置10は、大浴槽14の被処理水12が流れ込み循環させる循環用配管16に、髪の毛を回収するヘアーキャッチャー18と、ヘアーキャッチャー18の下流に設けられた循環ポンプ20とを有している。循環ポンプ20の下流側には、濾過タンク22が設けられ、濾過タンク22の下流に熱交換器24が設けられ、被処理水12の温度を所定温度に昇温し、循環用配管16を介して大浴槽14に被処理水12を戻している。
【0012】
循環用配管16の大浴槽14の取水口16aとヘアーキャッチャー18との間には、オゾン発生器26に接続されたオゾン配管28が接続されている。オゾン発生器26は、放電により空気中にオゾンを発生させ、所定濃度のオゾンガスを送るものである。発生したオゾンは、オゾン配管28から循環用配管16の被処理水12中に混入され、被処理水12中に溶解する。
【0013】
ヘアーキャッチャー18と循環ポンプ20との間の循環用配管16には、図2に示すように、内部にチタンまたはチタン合金製の、網やチタン線、繊維状チタン材料の集合体、その他多孔質チタン材料等の大表面積材料30を収容した反応容器32が取り付けられている。大表面積材料30は、チタンまたはチタン合金の表面に予め二酸化チタンの光触媒が形成されていても良く、後述するように、オゾンにより、使用中に二酸化チタンの光触媒を形成するものでも良い。
【0014】
反応容器32は少なくとも一部が透明で、透明部分は紫外線を通しやすい材料で形成されている。反応容器32の透明部分に面して、紫外線を照射する蛍光灯等の紫外線光源34が配置されている。紫外線光源34は、二酸化チタンの光触媒が正孔および電子を効率良く生じさせる紫外光(波長が410nm以下)を多く含むことが望ましく、紫外線ランプや低圧または高圧水銀ランプ、または300〜400nmの波長をもつ蛍光ランプなどであってよい。さらに、紫外光を出すLEDを複数個並べたものでも良い。
【0015】
次に、この実施形態の動作作用について説明する。被処理水12は循環ポンプ20により加圧されて、水処理装置10の濾過タンク22内に圧送され、異物等がある程度除去され、熱交換器24を介して一定の温度に温められて大浴槽14内に戻される。また、循環ポンプ20の上流側では、大浴槽14からの被処理水12が、循環用配管16によりヘアーキャッチャー18で髪の毛等を除去され、反応容器32を経て循環ポンプ20に吸引される。このとき、反応容器32の上流側の循環用配管16では、オゾン発生器26からのオゾン含有空気が被処理水12に混合され、このオゾンを有する被処理水12が反応容器32内の大表面積材料30間を通過する。大表面積材料32の表面では、二酸化チタンによる光触媒が形成され、この光触媒32の周囲では、紫外線照射によりOHラジカルによる殺菌や有機物の分解が行われる。この殺菌メカニズムは上述の通りである。同時に、オゾンによる殺菌も行われる。また、チタンまたはチタン合金製の大表面積材料30は、その表面の光触媒が剥離した場合、露出したチタン原子に対して被処理液12中のオゾンが反応し、容易に表面に二酸化チタンの光触媒が形成される。
【0016】
この実施形態の水処理方法と装置によれば、被処理水12に殺菌及び有機物の分解処理を光触媒により高効率で確実に行うことができ、さらに、オゾンによる殺菌も行われ、レジオラ菌等による浴槽水の汚染を確実に防止することができ、大量の被処理水12の処理が可能となる。さらに、反応容器32内の大表面積材料30の二酸化チタンによる光触媒が、長期間の使用により剥離しても、オゾン発生器26からのオゾンにより、チタンまたはチタン合金製の大表面積材料30の表面には、常時二酸化チタンが生成され、光触媒がなくなることはない。
【0017】
また、紫外光照射時に光触媒では、正孔と同時に生成した電子が酸素と迅速に反応してスーパーオキサイド(O )が生成する。このとき、酸素が不足すると未反応の電子が正孔と再結合し、正孔の酸化反応を阻害することになるが、この発明では、オゾンを含む十分な酸素含有気体が光触媒表面に供給されるので、上記の電子と正孔の再結合を防止することができ、その結果、被処理水12と二酸化チタンの光触媒との酸化反応効率を高めることができる。
【0018】
さらに、この実施形態によれば、反応容器32における被処理水12の混合攪拌効果により、被処理水12を光触媒表面に効率良く接触させることができるとともに、十分な酸素が供給され、二酸化チタン等の光触媒と被処理水12との反応効率を飛躍的に高めることができる。
【0019】
次にこの発明の第二実施形態について図3〜図5に基づいて説明する。ここで、上記実施の形態と同様の部材は同一符号を付して説明を省略する。この実施形態の水処理装置40は、熱交換器24の下流側に、大浴槽14へ送る被処理水12をバイパス配管42によりバイパスして加圧する二次側加圧ポンプ44を備えたもので、このバイパス配管42に、オゾン発生器26が接続されたものである。そして、反応容器32は、バイパス配管42が循環用配管16に接続された部位の下流側の循環用配管16に設けられている。
【0020】
オゾン発生器26からのオゾンは、オゾン配管28を経てバイパス配管42を流れる被処理水12に混合され溶解する。バイパス配管42とオゾン配管28の連結部は、図4に示すように、二次側加圧ポンプ44の下流に設けられ、この連結部には混合器46が設けられている。混合器46は、内部がベンチュリ管状に形成され、オゾン配管28はベンチュリ管の喉部に接続され、負圧により混合器46内に吸引され効率的に混合溶解が行われる。
【0021】
また、バイパス配管42とオゾン配管28の連結部が、図5に示すように、二次側加圧ポンプ44の上流に設けても良い。この場合、二次側加圧ポンプ44により、オゾンと被処理水12は十分に撹拌されオゾンが被処理水12内に溶解していく。
【0022】
この実施形態の水処理装置40によっても、オゾンが混合した被処理水12が反応容器32内に送られ、反応容器32内でオゾンによる殺菌と二酸化チタンによる光触媒の作用で、殺菌及び有機物の分解が効率的に行われる。さらに、反応容器32内の大表面積材料30は、表面の光触媒が剥離してもオゾンによりチタン原子が次々に二酸化チタンに酸化され、二酸化チタンの光触媒が剥離してなくなることはない。
【0023】
なお、この発明の被図処理方法と装置は、上記実施形態に限定されるものではなく、大表面積材料30は、チタンまたはチタン合金の線状材料を所定形状に形成した集合体や、チタンまたはチタン合金の針状体や粒状体の集合物、または多孔質体を集めたものでも良い。また、紫外線光源34は、図6に示すように、反応容器32の周囲3箇所に設けても良く、適宜複数箇所に配置しても良い。これによりより効率よく光触媒による反応が促進される。
【0024】
また、図7(A)に示すように、反応容器32内に紫外線光源34を配置しても良い。これにより、反応容器32による紫外線の減衰を無くすことができ、より効率的に光触媒の反応を起こさせることができる。さらに、図7(B)に示すように、反応容器32をヘアーキャッチャー18等の処理槽と兼用してもよい。例えば、反応容器13の被処理水12の入り口側にヘアーキャッチャーの籠48を設け、反応容器32内の隔壁50を隔てて、下流側に大表面積材料30を設けたものである。これにより、さらに装置の小型化、省スペース化を図ることができる。
【0025】
この発明の水処理方法と装置の対象とする被処理水は、浴槽の湯以外に生活排水や工業用水その他殺菌処理等を必要とする水全てに利用可能である。
【0026】
【発明の効果】
この発明に係る光触媒を用いた水処理方法と装置によれば、被処理水をオゾンとともに、光触媒により殺菌及び有機物の分解処理を行わせるようにしたので、被処理水に含まれる有害有機物、細菌等の微生物、臭気物質や難分解物質などを効率良く大量に殺菌、分解除去することができる。さらに、光触媒を表面に形成した大表面積材料を、チタンまたはチタン合金により形成したので、二酸化チタンの光触媒が長期使用により剥離しても、オゾンによる強力な酸化作用で、大表面積材料のチタン原子を酸化し、表面に二酸化チタンの光触媒を常に形成する。これにより、大表面積材料は、半永久的に光触媒として機能することができ、使用による光触媒の剥離等の問題を解決することができる。
【図面の簡単な説明】
【図1】この発明の第一実施形態の水処理装置の概略配管図である。
【図2】この実施形態の反応容器の縦断面図である。
【図3】この発明の第二実施形態の水処理装置の概略配管図である。
【図4】この実施形態の反応容器の配管を示す縦断面図である。
【図5】この実施形態の反応容器の他の配管を示す縦断面図である。
【図6】この発明の他の実施形態の紫外線光源の配置を示す概略断面図である。
【図7】この発明の他の実施形態の紫外線光源を配置した反応容器の概略断面図(A)と、ヘアーキャッチャーと兼用した反応容器の概略断面図(B)である。
【符号の説明】
10 水処理装置
12 被処理水
14 大浴槽
16 循環用配管
20 循環ポンプ
22 濾過タンク
24 熱交換器
26 オゾン発生器
30 大表面積材料
32 反応容器
34 紫外線光源
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a water treatment apparatus and a water treatment method for sterilizing water such as bathtub water, domestic wastewater, drinking water, pool water, cooling water, washing water, stored water, aquaculture water, and industrial wastewater.
[0002]
[Prior art]
[Patent Document 1] Japanese Patent Application Laid-Open No. H8-89725 [Patent Document 2] Japanese Patent Application Laid-Open No. H11-262759 Conventionally, for example, bath water in hot springs and health facilities is circulated while temperature control, sterilization, and removal of suspended matter are performed. Is being done. The bathtub water had been cleaned to a certain degree through a filtration tank containing mineral particles and a sterilizer using an ozone injection device, and circulated by a circulation pump.
[0003]
In the above configuration, the amount of ozone required for sterilization in a large-scale bath is large, and it is necessary to use high-concentration ozone. However, high-concentration ozone which was not completely dissolved in the water to be treated with high-concentration ozone was discharged into the air, which was not preferable. Further, in the case of circulating water in a large-scale bath facility, there is a problem that the amount of circulating hot water is large and low-concentration ozone results in a large-sized ozone generator and poor efficiency.
[0004]
On the other hand, as disclosed in Patent Documents 1 and 2, a reaction vessel provided with a photocatalyst is provided in the middle of a path for circulating the water to be treated, and the reaction vessel is irradiated with ultraviolet rays, and the water to be treated is treated by the photocatalyst. Those that render the bacteria harmless have also been proposed. In this water treatment apparatus, a net sprayed with titanium oxide is placed in a reaction vessel and irradiated with an ultraviolet lamp to pass water to be treated and sterilized by the action of a photocatalyst. Further, Patent Document 2 proposes a processing method for supplying a gas containing ozone into the water to be treated by using a similar apparatus.
[0005]
The principle of the sterilization treatment using the photocatalyst is as follows. When a photocatalyst such as titanium oxide, which is a semiconductor substance, is irradiated with ultraviolet light having a wavelength of 400 nm or less, holes are generated in the valence band and electrons are generated in the conduction band. The oxidation potential of these holes is higher than the oxidation potential of fluorine, ozone, hydrogen peroxide, etc., and organic substances are completely oxidized and decomposed by a photocatalyst, and finally are completely oxidized to carbon dioxide gas, water, sulfuric acid, nitric acid, etc. Is done. The mechanism of the oxidation reaction by the photocatalyst is that the oxidation reaction is caused by a hole generated when the photocatalyst is irradiated with ultraviolet light or a highly reactive hydroxyl radical (OH radical) generated by a reaction between the hole and water. It is believed that. At this time, a reduction reaction between electrons generated simultaneously with holes generated when the ultraviolet rays are irradiated and oxygen gas or the like proceeds in parallel. The action of the photocatalyst has a stronger germicidal ability than conventional germicides such as ozone, hydrogen peroxide and chlorine due to such a strong oxidation reaction, and also has a function of decomposing organic substances. In addition, since the lifetime of holes and OH radicals generated by light irradiation is as short as milliseconds or less, there is no residue after treatment such as an oxidizing agent such as ozone or hydrogen peroxide, and a device for treating the residual oxidizing agent is unnecessary. There is an advantage that there is. For this reason, many water treatment apparatuses using a photocatalyst have been proposed.
[0006]
[Problems to be solved by the invention]
However, since the action of the photocatalyst occurs only on the surface of the photocatalyst irradiated with light, it is necessary to increase the surface area of the photocatalyst to increase the contact efficiency with the water to be treated in order to perform the treatment efficiently. In addition, holes or OH radicals generated when the photocatalyst is irradiated with ultraviolet light have a short life, and therefore need to be reacted in a short time. Further, there is a problem that ultraviolet light is easily absorbed by water and is easily attenuated in water.
[0007]
Furthermore, in the case of the above-mentioned conventional technology, the oxidizing and disinfecting actions occur only on the surface of the photocatalyst irradiated with ultraviolet rays, and only a small part of the water to be treated comes into contact with the surface of the net sprayed with the photocatalyst such as titanium oxide on the surface. Only the processing was performed, and the processing capacity was low. In addition, a net on which a photocatalyst such as titanium oxide is sprayed has a low durability because the photocatalyst on the surface is easily separated. When the sprayed photocatalyst disappears, there is a problem that the function as the photocatalyst is lost and that part must be replaced.
[0008]
The present invention has been made in view of the above-mentioned problems of the related art, and has as its object to provide a water treatment apparatus and a water treatment method which can maintain a sterilizing action by a photocatalyst permanently and have a high sterilizing action. And
[0009]
[Means for Solving the Problems]
According to the present invention, a titanium or titanium alloy net or a large surface area material of a linear assembly is provided in a reaction vessel provided in the middle of a pipe through which water to be treated flows, and a photocatalyst comprising titanium oxide on the surface of the large surface area material Is formed, ozone is injected into the water to be treated on the upstream side of the large surface area material, and the large surface area material is irradiated with ultraviolet rays, and the water to be treated is sterilized by ozone and sterilized by the photocatalyst, Further, there is provided a water treatment method in which titanium oxide can be always formed on the surface of the titanium or titanium alloy by the ozone.
[0010]
The present invention also provides a pump for flowing the water to be treated, a reaction vessel provided in the middle of a pipe through which the water to be treated flows, a large surface area material made of titanium or a titanium alloy provided in the reaction vessel, The water treatment apparatus includes an ozone injection means such as an ozone generator for injecting ozone into the water to be treated on the upstream side of the surface area material, and an ultraviolet light source for irradiating the large surface area material with ultraviolet light. The reaction vessel may also serve as a processing tank such as a hair catcher.
[0011]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a schematic view showing a first embodiment of a water treatment apparatus of the present invention. A water treatment apparatus 10 of this embodiment treats bath water circulated in a hot spring or a health facility as treated water 12. Is what you do. The water treatment apparatus 10 of this embodiment includes a hair catcher 18 for collecting hair, a circulation pump 20 provided downstream of the hair catcher 18, a circulation pipe 16 through which the water to be treated 12 in the large bath 14 flows and circulates. have. A filtration tank 22 is provided downstream of the circulation pump 20, a heat exchanger 24 is provided downstream of the filtration tank 22, and the temperature of the water to be treated 12 is raised to a predetermined temperature. The treatment water 12 is returned to the large bath 14.
[0012]
An ozone pipe 28 connected to an ozone generator 26 is connected between the water intake 16 a of the large tub 14 of the circulation pipe 16 and the hair catcher 18. The ozone generator 26 generates ozone in the air by electric discharge and sends ozone gas of a predetermined concentration. The generated ozone is mixed into the water to be treated 12 of the circulation pipe 16 from the ozone pipe 28 and is dissolved in the water to be treated 12.
[0013]
As shown in FIG. 2, the circulation pipe 16 between the hair catcher 18 and the circulation pump 20 has a net or titanium wire, an aggregate of fibrous titanium material, and other porous materials made of titanium or a titanium alloy. A reaction vessel 32 containing a large surface area material 30 such as a titanium material is attached. The high surface area material 30 may have a titanium dioxide photocatalyst formed on the surface of titanium or a titanium alloy in advance, or may use ozone to form a titanium dioxide photocatalyst during use, as described later.
[0014]
At least a part of the reaction vessel 32 is transparent, and the transparent part is formed of a material that easily transmits ultraviolet light. An ultraviolet light source 34 such as a fluorescent lamp for irradiating ultraviolet light is disposed facing the transparent portion of the reaction vessel 32. The ultraviolet light source 34 desirably contains a large amount of ultraviolet light (wavelength of 410 nm or less) in which a photocatalyst of titanium dioxide efficiently generates holes and electrons. An ultraviolet lamp, a low-pressure or high-pressure mercury lamp, or a wavelength of 300 to 400 nm is used. Fluorescent lamp or the like. Further, a plurality of LEDs that emit ultraviolet light may be arranged.
[0015]
Next, the operation and operation of this embodiment will be described. The water to be treated 12 is pressurized by a circulation pump 20 and sent to a filtration tank 22 of the water treatment apparatus 10 under pressure to remove foreign substances and the like to some extent, and is heated to a certain temperature via a heat exchanger 24 to form a large bath. Returned to 14. Further, on the upstream side of the circulation pump 20, the water to be treated 12 from the large bath 14 is removed from the hair and the like by the hair catcher 18 by the circulation pipe 16, and is sucked into the circulation pump 20 via the reaction vessel 32. At this time, in the circulation pipe 16 on the upstream side of the reaction vessel 32, the ozone-containing air from the ozone generator 26 is mixed with the water to be treated 12, and the water to be treated 12 having the ozone has a large surface area in the reaction vessel 32. It passes between the materials 30. On the surface of the large surface area material 32, a photocatalyst by titanium dioxide is formed, and around this photocatalyst 32, sterilization by OH radicals and decomposition of organic substances are performed by ultraviolet irradiation. This sterilization mechanism is as described above. At the same time, ozone sterilization is also performed. When the photocatalyst on the surface of the titanium or titanium alloy material 30 is peeled off, the ozone in the liquid to be treated 12 reacts with the exposed titanium atoms, and the photocatalyst of titanium dioxide is easily deposited on the surface. It is formed.
[0016]
According to the water treatment method and apparatus of this embodiment, sterilization and decomposition of organic substances can be performed on the water to be treated 12 with high efficiency using a photocatalyst, and sterilization with ozone is also performed. Bath water can be reliably prevented from being contaminated, and a large amount of water to be treated 12 can be treated. Further, even if the photocatalyst of titanium dioxide of the large surface area material 30 in the reaction vessel 32 is peeled off due to long-term use, the ozone from the ozone generator 26 causes the surface of the large surface area material 30 made of titanium or a titanium alloy to be exposed. In this method, titanium dioxide is always generated and the photocatalyst does not disappear.
[0017]
In addition, in the photocatalyst at the time of ultraviolet light irradiation, electrons generated simultaneously with holes react quickly with oxygen to generate superoxide (O 2 ). At this time, if oxygen is insufficient, unreacted electrons are recombined with holes to inhibit the oxidation reaction of holes. However, in the present invention, a sufficient oxygen-containing gas including ozone is supplied to the photocatalyst surface. Therefore, the recombination of the electrons and holes can be prevented, and as a result, the efficiency of the oxidation reaction between the water to be treated 12 and the photocatalyst of titanium dioxide can be increased.
[0018]
Further, according to this embodiment, due to the mixing and stirring effect of the water to be treated 12 in the reaction vessel 32, the water to be treated 12 can be efficiently brought into contact with the surface of the photocatalyst, and sufficient oxygen is supplied, and titanium dioxide or the like is supplied. The reaction efficiency between the photocatalyst and the water to be treated 12 can be dramatically increased.
[0019]
Next, a second embodiment of the present invention will be described with reference to FIGS. Here, the same members as those in the above embodiment are denoted by the same reference numerals, and the description will be omitted. The water treatment apparatus 40 of this embodiment includes a secondary-side pressurizing pump 44 that is provided downstream of the heat exchanger 24 and pressurizes the water to be treated 12 that is sent to the large bath 14 by bypassing the bypass pipe 42. The ozone generator 26 is connected to the bypass pipe 42. The reaction vessel 32 is provided in the circulation pipe 16 on the downstream side of the portion where the bypass pipe 42 is connected to the circulation pipe 16.
[0020]
Ozone from the ozone generator 26 is mixed and dissolved in the water to be treated 12 flowing through the bypass pipe 42 via the ozone pipe 28. As shown in FIG. 4, a connection between the bypass pipe 42 and the ozone pipe 28 is provided downstream of the secondary-side pressurizing pump 44, and a mixer 46 is provided at this connection. The mixer 46 has a Venturi tube inside, and the ozone pipe 28 is connected to the throat of the Venturi tube. The ozone pipe 28 is sucked into the mixer 46 by a negative pressure to efficiently mix and dissolve.
[0021]
Further, the connection between the bypass pipe 42 and the ozone pipe 28 may be provided upstream of the secondary side pressure pump 44 as shown in FIG. In this case, the ozone and the water to be treated 12 are sufficiently stirred by the secondary side pressure pump 44, and the ozone is dissolved in the water to be treated 12.
[0022]
The water to be treated 12 mixed with ozone is also sent to the reaction vessel 32 by the water treatment apparatus 40 of this embodiment, and sterilization by ozone and photocatalysis by titanium dioxide are performed in the reaction vessel 32 to sterilize and decompose organic substances. Is performed efficiently. Furthermore, even if the photocatalyst on the surface of the high-surface-area material 30 in the reaction vessel 32 is peeled off, titanium atoms are oxidized to titanium dioxide one after another by ozone, and the photocatalyst of titanium dioxide does not peel off.
[0023]
The drawing processing method and apparatus of the present invention are not limited to the above-described embodiment, and the large surface area material 30 may be an aggregate formed by forming a linear material of titanium or a titanium alloy into a predetermined shape, or a titanium or titanium alloy. A collection of needle-like bodies or granular bodies of a titanium alloy or a collection of porous bodies may be used. Further, as shown in FIG. 6, the ultraviolet light sources 34 may be provided at three places around the reaction vessel 32, or may be provided at a plurality of places as appropriate. This promotes the photocatalytic reaction more efficiently.
[0024]
Further, as shown in FIG. 7A, an ultraviolet light source 34 may be arranged in the reaction vessel 32. Thereby, the attenuation of the ultraviolet rays by the reaction vessel 32 can be eliminated, and the reaction of the photocatalyst can be caused more efficiently. Further, as shown in FIG. 7 (B), the reaction vessel 32 may be used also as a processing tank such as the hair catcher 18. For example, a hair catcher basket 48 is provided on the inlet side of the water to be treated 12 of the reaction vessel 13, and the large surface area material 30 is provided downstream on the downstream side of the partition wall 50 in the reaction vessel 32. This can further reduce the size and space of the device.
[0025]
The water to be treated, which is the object of the water treatment method and apparatus of the present invention, can be used for domestic wastewater, industrial water, and all other water that requires sterilization, in addition to hot water in a bathtub.
[0026]
【The invention's effect】
According to the water treatment method and apparatus using a photocatalyst according to the present invention, the water to be treated is subjected to sterilization and decomposition of organic substances by the photocatalyst together with ozone, so that harmful organic substances and bacteria contained in the water to be treated are included. Microorganisms, odorous substances, hardly decomposable substances and the like can be efficiently sterilized, decomposed and removed in large quantities. Furthermore, since the titanium oxide or titanium alloy is used to form the large surface area material with the photocatalyst formed on the surface, even if the titanium dioxide photocatalyst peels off due to long-term use, the strong oxidizing action of ozone will remove the titanium atoms of the large surface area material. Oxidizes and constantly forms a titanium dioxide photocatalyst on the surface. Accordingly, the high surface area material can semipermanently function as a photocatalyst, and can solve problems such as separation of the photocatalyst due to use.
[Brief description of the drawings]
FIG. 1 is a schematic piping diagram of a water treatment device according to a first embodiment of the present invention.
FIG. 2 is a longitudinal sectional view of the reaction vessel of this embodiment.
FIG. 3 is a schematic piping diagram of a water treatment apparatus according to a second embodiment of the present invention.
FIG. 4 is a longitudinal sectional view showing the piping of the reaction vessel of this embodiment.
FIG. 5 is a longitudinal sectional view showing another piping of the reaction vessel of this embodiment.
FIG. 6 is a schematic sectional view showing an arrangement of an ultraviolet light source according to another embodiment of the present invention.
FIG. 7 is a schematic sectional view (A) of a reaction vessel provided with an ultraviolet light source according to another embodiment of the present invention, and a schematic sectional view (B) of a reaction vessel also serving as a hair catcher.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 10 Water treatment apparatus 12 Treated water 14 Large bath 16 Circulation piping 20 Circulation pump 22 Filtration tank 24 Heat exchanger 26 Ozone generator 30 Large surface area material 32 Reaction vessel 34 Ultraviolet light source

Claims (2)

被処理水が流れる配管の途中に設けられる反応容器内にチタンまたはチタン合金製の大表面積材料を設け、この大表面積材料の表面に酸化チタンから成る光触媒を形成し、この大表面積材料の上流側で上記被処理水中にオゾンを注入し、上記大表面積材料に紫外線を照射して、オゾンにより上記被処理水を殺菌するとともに上記光触媒により殺菌を行ない、上記オゾンにより上記チタンまたはチタン合金表面に酸化チタンを形成するようにしたことを特徴とする水処理方法。A large surface area material made of titanium or a titanium alloy is provided in a reaction vessel provided in the middle of a pipe through which water to be treated flows, and a photocatalyst made of titanium oxide is formed on the surface of the large surface area material. Inject ozone into the water to be treated, irradiate the large surface area material with ultraviolet rays, sterilize the water to be treated with ozone, sterilize with the photocatalyst, and oxidize the titanium or titanium alloy surface with the ozone. A water treatment method, wherein titanium is formed. 被処理水を流すポンプと、被処理水が流れる配管の途中に設けられる反応容器と、この反応容器の中に設けられたチタンまたはチタン合金製の大表面積材料と、この大表面積材料の上流側で上記被処理水中にオゾンを注入するオゾン注入手段と、上記大表面積材料に紫外線を照射する紫外線光源とを備えたことを特徴とする水処理装置。A pump for flowing the water to be treated, a reaction vessel provided in the middle of a pipe through which the water to be treated flows, a large surface area material made of titanium or a titanium alloy provided in the reaction vessel, and an upstream side of the large surface area material A water treatment apparatus comprising: an ozone injection means for injecting ozone into the water to be treated; and an ultraviolet light source for irradiating the large surface area material with ultraviolet light.
JP2002325207A 2002-11-08 2002-11-08 Water treatment equipment Expired - Fee Related JP4229363B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002325207A JP4229363B2 (en) 2002-11-08 2002-11-08 Water treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002325207A JP4229363B2 (en) 2002-11-08 2002-11-08 Water treatment equipment

Publications (2)

Publication Number Publication Date
JP2004154742A true JP2004154742A (en) 2004-06-03
JP4229363B2 JP4229363B2 (en) 2009-02-25

Family

ID=32804507

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002325207A Expired - Fee Related JP4229363B2 (en) 2002-11-08 2002-11-08 Water treatment equipment

Country Status (1)

Country Link
JP (1) JP4229363B2 (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE112006003564T5 (en) 2005-12-26 2008-10-30 Toyo Valve Co., Ltd. Fluid purification device and fluid purification method
US20100247390A1 (en) * 2007-09-26 2010-09-30 Kenichiro Tanaka Apparatus for producing water having redox activity
US8398828B1 (en) 2012-01-06 2013-03-19 AquaMost, Inc. Apparatus and method for treating aqueous solutions and contaminants therein
US8658035B2 (en) 2011-12-02 2014-02-25 AquaMost, Inc. Apparatus and method for treating aqueous solutions and contaminants therein
US9045357B2 (en) 2012-01-06 2015-06-02 AquaMost, Inc. System for reducing contaminants from a photoelectrocatalytic oxidization apparatus through polarity reversal and method of operation
US9096450B2 (en) 2013-02-11 2015-08-04 AquaMost, Inc. Apparatus and method for treating aqueous solutions and contaminants therein
JP2016101584A (en) * 2010-06-04 2016-06-02 アクセス ビジネス グループ インターナショナル リミテッド ライアビリティ カンパニー Inductively coupled dielectric barrier discharge lamp
CN113738704A (en) * 2021-10-11 2021-12-03 广州耐雪制冷设备有限公司 Pipeline structure with flow stopping function
JP7411770B2 (en) 2018-09-26 2024-01-11 東洋バルヴ株式会社 water treatment equipment

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105645509A (en) * 2016-01-11 2016-06-08 汤奇岳 Green-energy water, and preparation device and method thereof, and application of green-energy water

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11262759A (en) * 1998-03-18 1999-09-28 Mitsubishi Electric Corp Water-treatment apparatus using photocatalyst and method therefor
JP2000225339A (en) * 1999-02-04 2000-08-15 Kawasaki Heavy Ind Ltd Production of titanium oxide-coated material

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11262759A (en) * 1998-03-18 1999-09-28 Mitsubishi Electric Corp Water-treatment apparatus using photocatalyst and method therefor
JP2000225339A (en) * 1999-02-04 2000-08-15 Kawasaki Heavy Ind Ltd Production of titanium oxide-coated material

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101440406B1 (en) 2005-12-26 2014-09-15 가부시키가이샤 기츠 Fluid depurator and fluid depuration method
US8282879B2 (en) 2005-12-26 2012-10-09 Kitz Corporation Fluid purification device and fluid purification method
DE112006003564T5 (en) 2005-12-26 2008-10-30 Toyo Valve Co., Ltd. Fluid purification device and fluid purification method
US20100247390A1 (en) * 2007-09-26 2010-09-30 Kenichiro Tanaka Apparatus for producing water having redox activity
US8889075B2 (en) * 2007-09-26 2014-11-18 Kitakyushu Foundation For The Advancement Of Industry, Science And Technology Apparatus for producing water having redox activity
JP2016101584A (en) * 2010-06-04 2016-06-02 アクセス ビジネス グループ インターナショナル リミテッド ライアビリティ カンパニー Inductively coupled dielectric barrier discharge lamp
JP2018047461A (en) * 2010-06-04 2018-03-29 アクセス ビジネス グループ インターナショナル リミテッド ライアビリティ カンパニー Inductive coupling dielectric barrier discharge lamp
US10035715B2 (en) 2010-06-04 2018-07-31 Access Business Group International Llc Inductively coupled dielectric barrier discharge lamp
US10160667B2 (en) 2010-06-04 2018-12-25 Access Business Group International Llc Inductively coupled dielectric barrier discharge lamp
US8658046B2 (en) 2011-12-02 2014-02-25 AquaMost, Inc. Apparatus and method for treating aqueous solutions and contaminants therein
US8663471B1 (en) 2011-12-02 2014-03-04 AquaMost, Inc. Apparatus and method for treating aqueous solutions and contaminants therein
US8658035B2 (en) 2011-12-02 2014-02-25 AquaMost, Inc. Apparatus and method for treating aqueous solutions and contaminants therein
US8568573B2 (en) 2012-01-06 2013-10-29 AquaMost, Inc. Apparatus and method for treating aqueous solutions and contaminants therein
US9045357B2 (en) 2012-01-06 2015-06-02 AquaMost, Inc. System for reducing contaminants from a photoelectrocatalytic oxidization apparatus through polarity reversal and method of operation
US8398828B1 (en) 2012-01-06 2013-03-19 AquaMost, Inc. Apparatus and method for treating aqueous solutions and contaminants therein
US9096450B2 (en) 2013-02-11 2015-08-04 AquaMost, Inc. Apparatus and method for treating aqueous solutions and contaminants therein
JP7411770B2 (en) 2018-09-26 2024-01-11 東洋バルヴ株式会社 water treatment equipment
CN113738704A (en) * 2021-10-11 2021-12-03 广州耐雪制冷设备有限公司 Pipeline structure with flow stopping function

Also Published As

Publication number Publication date
JP4229363B2 (en) 2009-02-25

Similar Documents

Publication Publication Date Title
JP4355315B2 (en) Fluid purification device
JP5143387B2 (en) Fluid processing method and fluid processing apparatus
JP5015542B2 (en) Water purification equipment
JP4229363B2 (en) Water treatment equipment
JP2010069353A (en) Cleaning apparatus
JP4093409B2 (en) Fluid purification method and fluid purification device
JP3744454B2 (en) Water treatment equipment
JP3646509B2 (en) Water treatment equipment using photocatalyst
JPH10337579A (en) Method and apparatus for treatment of wastewater
JP3270509B2 (en) Bathtub hot water sterilization and purification equipment
KR20040049470A (en) Water sterilization device
JPH1177031A (en) Method and apparatus for ultraviolet radiation sterilizing purification
KR102589335B1 (en) Water treatment apparatus
KR102138176B1 (en) Wastewater pre-processing system with OH reaction agitation tank
JPH08155445A (en) Water treatment apparatus
JP2000279952A (en) Water purifier
JP2001252652A (en) Water purifying device
CN117658274A (en) Low-power-consumption high-efficiency ultraviolet light catalytic oxidation method
JP2004089935A (en) Water treatment method and water treatment apparatus
JPH05305291A (en) Apparatus for cleaning bath water
JP2007160241A (en) Hypohalous acid decomposing method
JP2001170625A (en) Water treating device
JP2004160384A (en) Non-exhaust type sterilization and purification apparatus using ultraviolet light in combination with ozone
JPH11300376A (en) Water treatment and device therefor
KR20160148256A (en) Radical anion-water manufacturing equipment and manufacturing method thereof

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20051025

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20071221

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20080109

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20080310

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20080402

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20080527

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20081001

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20081002

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20081024

A711 Notification of change in applicant

Free format text: JAPANESE INTERMEDIATE CODE: A711

Effective date: 20081027

RD02 Notification of acceptance of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7422

Effective date: 20081027

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A821

Effective date: 20081027

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20081128

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111212

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20141212

Year of fee payment: 6

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees