Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP5310772B2 - Air conditioning equipment - Google Patents
[go: Go Back, main page]

JP5310772B2 - Air conditioning equipment - Google Patents

Air conditioning equipment Download PDF

Info

Publication number
JP5310772B2
JP5310772B2 JP2011085091A JP2011085091A JP5310772B2 JP 5310772 B2 JP5310772 B2 JP 5310772B2 JP 2011085091 A JP2011085091 A JP 2011085091A JP 2011085091 A JP2011085091 A JP 2011085091A JP 5310772 B2 JP5310772 B2 JP 5310772B2
Authority
JP
Japan
Prior art keywords
water
cathode
oxygen species
active oxygen
anode
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.)
Expired - Fee Related
Application number
JP2011085091A
Other languages
Japanese (ja)
Other versions
JP2012217908A (en
Inventor
真理 折戸
史朗 竹内
潤一郎 星崎
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.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric Corp
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 Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP2011085091A priority Critical patent/JP5310772B2/en
Publication of JP2012217908A publication Critical patent/JP2012217908A/en
Application granted granted Critical
Publication of JP5310772B2 publication Critical patent/JP5310772B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Water Treatment By Electricity Or Magnetism (AREA)

Description

この発明は、電極反応によって活性酸素種を生成する活性酸素種生成装置備えた空調機器に関するものである。 The present invention relates to an air conditioner including an active oxygen species generating device that generates active oxygen species by an electrode reaction.

下記特許文献1及び2には、水中の菌の繁殖を抑制するための装置において、浮遊体の下方に電極を設け、浮遊体を水面に浮かべるものが開示されている。具体的に、特許文献1及び2に記載のものでは、水中に配置された電極から、殺菌性の金属イオンを溶出させることにより、その溶出した金属イオンによって殺菌を行っている。   Patent Documents 1 and 2 below disclose an apparatus for suppressing the propagation of bacteria in water, in which an electrode is provided below the floating body and the floating body floats on the water surface. Specifically, in the thing of patent document 1 and 2, sterilization is performed by the eluted metal ion by eluting the bactericidal metal ion from the electrode arrange | positioned in water.

特許第3947180号公報Japanese Patent No. 3947180 特開2000−154570号公報JP 2000-154570 A

特許文献1及び2に記載のものでは、電極から溶出させた金属イオンによって殺菌を行うため、電極基材が通電によって徐々に劣化し、長期間安定して使用することが困難であった。   In the thing of patent document 1 and 2, since it sterilizes with the metal ion eluted from the electrode, the electrode base material deteriorated gradually by electricity supply, and it was difficult to use it stably for a long period of time.

これに対し、水中の菌の繁殖を抑制するための装置として、電極反応によって活性酸素種を生成するものも知られている。かかる生成装置では、水中の溶存酸素との反応によって活性酸素種を生成し、生成した活性酸素種によって菌の繁殖等を抑制する。このため、電極の配置が適切に行われていないと、活性酸素種の生成能が著しく低下するといった問題があった。   On the other hand, an apparatus for generating reactive oxygen species by an electrode reaction is also known as an apparatus for suppressing the propagation of bacteria in water. In such a production | generation apparatus, reactive oxygen species are produced | generated by reaction with the dissolved oxygen in water, and reproduction | regeneration of a microbe etc. are suppressed with the produced | generated active oxygen species. For this reason, there has been a problem in that the ability to generate active oxygen species is significantly reduced if the electrodes are not properly arranged.

この発明は、上述のような課題を解決するためになされたもので、その目的は、活性酸素種生成装置を備えた空調機器において、電極を適切に配置して活性酸素種の生成効率を向上させるとともに、活性酸素種の生成効率が高い状態で長期に渡って使用することができるようにすることである。 The present invention has been made to solve the above-described problems, and its object is to improve the generation efficiency of active oxygen species by appropriately arranging electrodes in an air conditioner equipped with an active oxygen species generation device. In addition, the active oxygen species can be used over a long period of time with high generation efficiency.

この発明に係る空調機器は、電極反応により活性酸素種を生成する活性酸素種生成装置を冷却塔に備えた空調機器であって、冷却塔は、水を循環させるためのポンプと、ポンプによって循環される水の熱交換を行うための熱交換部と、熱交換部から流下した水が貯留される貯水部と、を備え、活性酸素種生成装置は、各一部が、貯水部に貯留された水の水面から突出し、各他部が貯水部に貯留された水に浸漬された陰極及び陽極と、陰極及び陽極の気中露出面積と水中浸漬面積との比を、貯水部内の水位変動に関わらず、一定に保持するための保持手段と、を備えたものである。 An air conditioner according to the present invention is an air conditioner equipped with a reactive oxygen species generating device for generating active oxygen species by an electrode reaction in a cooling tower, and the cooling tower is circulated by a pump for circulating water and a pump. A heat exchange part for performing heat exchange of the water to be generated and a water storage part for storing water flowing down from the heat exchange part, and each part of the active oxygen species generating device is stored in the water storage part The ratio of the cathode exposed to the surface of the water and the other parts immersed in the water stored in the reservoir and the ratio of the exposed area in the air and the area immersed in the water to the water level fluctuation in the reservoir Regardless, it is provided with holding means for holding it constant .

この発明によれば、電極を適切に配置して活性酸素種の生成効率を向上させることができる。また、活性酸素種の生成効率が高い状態で、装置の長期に渡る使用が可能となる。   According to the present invention, it is possible to improve the generation efficiency of active oxygen species by appropriately arranging the electrodes. In addition, the apparatus can be used for a long period of time while the generation efficiency of the active oxygen species is high.

この発明の実施の形態1における活性酸素種生成装置の構成を示す概略図である。It is the schematic which shows the structure of the active oxygen species production | generation apparatus in Embodiment 1 of this invention. 図1に示す活性酸素種生成装置の高水位時の状態と低水位時の状態とを示す概略図である。It is the schematic which shows the state at the time of the high water level of a reactive oxygen species production | generation apparatus shown in FIG. 1, and the state at the time of a low water level. 酸化還元反応によるポリアニリンの構造変化を示す図である。It is a figure which shows the structural change of polyaniline by oxidation-reduction reaction. 過酸化水素濃度の推移を示す図である。It is a figure which shows transition of hydrogen peroxide concentration. この発明の実施の形態2における空調機器の構成を示す概略図である。It is the schematic which shows the structure of the air conditioning apparatus in Embodiment 2 of this invention.

この発明をより詳細に説明するため、添付の図面に従ってこれを説明する。なお、各図中、同一又は相当する部分には同一の符号を付しており、その重複説明は適宜に簡略化ないし省略する。   In order to explain the present invention in more detail, it will be described with reference to the accompanying drawings. In addition, in each figure, the same code | symbol is attached | subjected to the part which is the same or it corresponds, The duplication description is simplified or abbreviate | omitted suitably.

実施の形態1.
図1はこの発明の実施の形態1における活性酸素種生成装置の構成を示す概略図、図2は図1に示す活性酸素種生成装置の高水位時の状態と低水位時の状態とを示す概略図である。
Embodiment 1 FIG.
FIG. 1 is a schematic diagram showing a configuration of an active oxygen species generating device according to Embodiment 1 of the present invention, and FIG. 2 shows a high water level state and a low water level state of the active oxygen species generating device shown in FIG. FIG.

図1及び図2において、1は水反応槽、2は水反応槽1に溜められた水、3は本願発明の要部を構成する活性酸素種生成部である。水反応槽1内には、陰極4及び陽極5からなる電極が配置されている。陰極4及び陽極5は、例えば、板状を呈しており、それぞれの一部が水2の水面2aから突出し、他部のみが水2に浸漬されて(浸されて)いる。陰極4及び陽極5は、電圧印加手段6に接続されており、所定の電圧が印加できるように構成されている。   1 and 2, 1 is a water reaction tank, 2 is water stored in the water reaction tank 1, and 3 is an active oxygen species generation unit that constitutes a main part of the present invention. An electrode composed of a cathode 4 and an anode 5 is disposed in the water reaction tank 1. The cathode 4 and the anode 5 have, for example, a plate shape, part of which protrudes from the water surface 2 a of the water 2 and only the other part is immersed (immersed) in the water 2. The cathode 4 and the anode 5 are connected to a voltage applying means 6 and configured to apply a predetermined voltage.

活性酸素種生成部3は、電圧印加手段6によって陰極4及び陽極5に所定の電圧が印加されることにより、電極反応によって水2中に活性酸素種を生成する。なお、電極(陰極4及び陽極5)は、水反応槽1に貯留された水2を殺菌処理するために必要な量の活性酸素種を生成することができるように、水2への浸漬量(面積)が設定されている。生成された活性酸素種は、濃度勾配による自然拡散により、電極の表面から水2全体に拡散する。また、水反応槽1内にポンプ等の水流発生手段(図示せず)を設置したり、水反応槽1に配管を介してポンプ等の水流発生手段を接続したりして電極の近傍に水流を強制的に発生させても、生成された活性酸素種を水2全体に拡散させることができる。   The active oxygen species generator 3 generates active oxygen species in the water 2 by an electrode reaction when a predetermined voltage is applied to the cathode 4 and the anode 5 by the voltage application means 6. The electrodes (cathode 4 and anode 5) are immersed in water 2 so that the amount of active oxygen species necessary for sterilizing the water 2 stored in the water reaction tank 1 can be generated. (Area) is set. The generated active oxygen species diffuses from the surface of the electrode to the entire water 2 by natural diffusion due to the concentration gradient. Further, a water flow generating means (not shown) such as a pump is installed in the water reaction tank 1 or a water flow generating means such as a pump is connected to the water reaction tank 1 through a pipe so that the water flow is in the vicinity of the electrode. Even if this is forcibly generated, the generated active oxygen species can be diffused throughout the water 2.

7は電極(陰極4及び陽極5)に設けられた浮遊手段(保持手段)である。浮遊手段7は、電極の表面積のうち、空気中に露出している面積(水2に浸されていない面積の意:以下、「気中露出面積」という)と、水2に浸されている面積(以下、「水中浸漬面積」という)との比率(図1におけるA:B)を一定に保持するためのものである。即ち、浮遊手段7により、電極が水面2aに対して常に同じ位置に保持される。   7 is a floating means (holding means) provided on the electrodes (cathode 4 and anode 5). The floating means 7 is immersed in the surface of the electrode surface area exposed in the air (meaning the area not immersed in the water 2, hereinafter referred to as “air exposed area”) and the water 2. The ratio (A: B in FIG. 1) to the area (hereinafter referred to as “submerged area in water”) is kept constant. That is, the electrode is always held at the same position with respect to the water surface 2a by the floating means 7.

活性酸素種は、水2中の溶存酸素により生成される物質である。このため、電極と水面2aとの位置関係、即ち、電極の気中露出面積と水中浸漬面積との比は、一定であることが望ましい。浮遊手段7は、このような機能を実現するための手段を構成するが、電極の気中露出面積と水中浸漬面積との比を、常に厳密に一定に保持できなくても構わない。例えば、ポンプ等の水流発生手段が備えられている場合は、水面2aに微小な揺れが発生する。かかる場合、電極の水面2aに対する位置は、水面2aの微小な揺れの全てに一致していなくても良い。但し、本実施の形態のような電極に固定した浮遊手段7であれば、電極の位置を水面2aの微小な揺れにも追従させることは可能である。   The reactive oxygen species is a substance generated by dissolved oxygen in the water 2. For this reason, it is desirable that the positional relationship between the electrode and the water surface 2a, that is, the ratio of the exposed area of the electrode in the air to the submerged area is constant. The floating means 7 constitutes a means for realizing such a function. However, the ratio of the air exposure area of the electrode to the water immersion area may not always be kept strictly constant. For example, in the case where water flow generating means such as a pump is provided, minute fluctuations occur on the water surface 2a. In such a case, the position of the electrode with respect to the water surface 2a may not coincide with all the minute fluctuations of the water surface 2a. However, if the floating means 7 is fixed to the electrode as in the present embodiment, the position of the electrode can be made to follow even the slight shaking of the water surface 2a.

具体的に、浮遊手段7は、発泡材等、浮力によって電極を水2に浮遊させることができるもので構成される。
また、保持手段として、浮遊以外の他の手段を採用しても良い。例えば、ボールタップ等の水位検出手段によって水反応槽1内の水位を検出し、滑車構造や可動軸により、検出した水位(水面2aの位置)に合わせて、電極の位置(高さ)を調節しても良い。
Specifically, the floating means 7 is composed of a foam material or the like that can float the electrode in the water 2 by buoyancy.
Further, other means other than floating may be employed as the holding means. For example, the water level in the water reaction tank 1 is detected by a water level detection means such as a ball tap, and the position (height) of the electrode is adjusted according to the detected water level (position of the water surface 2a) by means of a pulley structure or a movable shaft. May be.

陰極4は、浮遊手段7が設けられることにより、その一部(所定位置から上方の部分)が水面(喫水線)2aよりも常に上方に配置され、空気中に露出した状態となる。また、陰極4の他部(上記所定位置から下方の部分)は、水面2aよりも常に下方に配置され、水2に浸漬された状態となる。即ち、浮遊手段7は、水反応槽1内の水2の量(水位)に関わらず、陰極4の気中露出面積と水中浸漬面積との比を一定に保持する。例えば、高水位時の陰極4の気中露出面積Aと水中浸漬面積Bとの比は、低水位時の陰極4の気中露出面積Aと水中浸漬面積Bとの比と同じ(A:B=A:B)になる。(図2では、浮遊手段7の記載を省略している。) Since the cathode 4 is provided with the floating means 7, a part thereof (a portion above a predetermined position) is always disposed above the water surface (draft line) 2 a and is exposed to the air. The other part of the cathode 4 (the part below the predetermined position) is always disposed below the water surface 2 a and is immersed in the water 2. That is, the floating means 7 keeps the ratio of the exposed area of the cathode 4 in the air and the area immersed in water constant regardless of the amount (water level) of the water 2 in the water reaction tank 1. For example, the ratio of the air during the exposure area A 1 and immersed in water area B 1 of the cathode 4 at high water level, the same as the ratio of the air during the exposure area A 2 of the cathode 4 at the time of low water-water immersion area B 2 (A 1 : B 1 = A 2 : B 2 ) (In FIG. 2, description of the floating means 7 is omitted.)

陽極5についても、陰極4と同様である。即ち、陽極5は、浮遊手段7が設けられることにより、その一部(所定位置から上方の部分)が水面2aよりも常に上方に配置され、空気中に露出した状態となる。また、陽極5の他部(上記所定位置から下方の部分)は、水面2aよりも常に下方に配置され、水2に浸漬された状態となる。即ち、浮遊手段7は、水反応槽1内の水2の量(水位)に関わらず、陽極5の気中露出面積と水中浸漬面積との比を一定に保持する。   The anode 5 is the same as the cathode 4. That is, the anode 5 is provided with the floating means 7 so that a part thereof (a portion above a predetermined position) is always disposed above the water surface 2a and is exposed to the air. Further, the other part of the anode 5 (the part below the predetermined position) is always disposed below the water surface 2 a and is immersed in the water 2. That is, the floating means 7 keeps the ratio of the exposed area in the air of the anode 5 and the area immersed in water constant regardless of the amount (water level) of the water 2 in the water reaction tank 1.

また、電極は、広い面積を有する面が水面2aに対して垂直となるように配置される。かかる配置であれば、溶存酸素濃度が高い水面2a近傍の電極の表面積を多くすることができ、活性酸素種の生成効率を向上させることが可能となる。エアバブリングといった水2中の溶存酸素濃度を上げるための手段が特に備えられていない場合、水2中への酸素の供給は、水2と空気とが接する水面2aにおいて行われる。このため、電極の上記配置は、エアバブリング等の酸素供給手段が備えられていない場合に、特に有効である。なお、エアバブリング等の酸素供給手段が備えられている場合は、電極の水2に浸漬されている部分の一部を酸素供給手段(或いは、酸素供給手段から供給される酸素(空気))の近傍に配置すれば良い。   The electrodes are arranged such that a surface having a large area is perpendicular to the water surface 2a. With such an arrangement, the surface area of the electrode in the vicinity of the water surface 2a having a high dissolved oxygen concentration can be increased, and the generation efficiency of active oxygen species can be improved. When a means for increasing the dissolved oxygen concentration in the water 2 such as air bubbling is not particularly provided, the supply of oxygen into the water 2 is performed on the water surface 2a where the water 2 and the air are in contact with each other. For this reason, the above arrangement of the electrodes is particularly effective when oxygen supply means such as air bubbling is not provided. In the case where an oxygen supply means such as air bubbling is provided, a part of the electrode immersed in the water 2 is part of the oxygen supply means (or oxygen (air) supplied from the oxygen supply means). What is necessary is just to arrange | position in the vicinity.

活性酸素種の生成能を向上させる手段の一つに、陰極4の表面に活性酸素種の生成能を有する材料を塗布する方法がある。具体的には、活性酸素種生成能を有する材料として導電性高分子(レドックスポリマー)が採用され、陰極4の表面がレドックスポリマーによって被覆される。なお、レドックスポリマーの具体例としては、例えば、ポリアニリン、ポリチオフェン、ポリピロール、ポリアセン等が挙げられる。   One means for improving the ability to generate active oxygen species is to apply a material having the ability to generate active oxygen species to the surface of the cathode 4. Specifically, a conductive polymer (redox polymer) is employed as a material having the ability to generate active oxygen species, and the surface of the cathode 4 is covered with the redox polymer. Specific examples of the redox polymer include polyaniline, polythiophene, polypyrrole, polyacene, and the like.

レドックスポリマーとは、化学的重合、電気的重合といった重合方法に関わらず生成され、電子の授受により酸化状態或いは還元状態に可逆的に変化する物質のことである。活性酸素を生成するためには、酸素の還元作用に最も優れるポリアニリンを陰極4に担持させる構成が好ましい。図3は酸化還元反応によるポリアニリンの構造変化を示す図である。図3に示すように、ポリアニリンは、還元型から酸化型に構造変化する際に、その触媒的作用によって電子と水2中の酸素とを反応させて、活性酸素の一種であるスーパーオキシド(O )を生成する(式1参照)。他に、過酸化水素やヒドロキシラジカルといった物質も生成される。
+PAn(red)→O +PAn(ox) ・・・(1)
A redox polymer is a substance that is produced regardless of a polymerization method such as chemical polymerization or electrical polymerization, and reversibly changes to an oxidized state or a reduced state by exchange of electrons. In order to generate active oxygen, a configuration in which polyaniline having the best oxygen reducing action is supported on the cathode 4 is preferable. FIG. 3 is a diagram showing a structural change of polyaniline due to an oxidation-reduction reaction. As shown in FIG. 3, when the polyaniline undergoes a structural change from a reduced form to an oxidized form, it reacts with electrons in the water 2 by its catalytic action to produce superoxide (O 2 -) to generate (see equation 1). In addition, substances such as hydrogen peroxide and hydroxy radicals are also generated.
O 2 + PAn (red) → O 2 + PAn (ox) (1)

式1に示す活性酸素種の生成反応によって、ポリアニリンは、酸化型へと構造変化する。しかし、陰極4には、電圧印加手段6から電子が供給されるため、供給される電子によってポリアニリンは元の状態に戻り、継続して活性酸素種を生成することができる。   The structure of polyaniline is changed to an oxidized form by the reaction of generating active oxygen species shown in Formula 1. However, since electrons are supplied to the cathode 4 from the voltage applying means 6, the polyaniline returns to its original state by the supplied electrons, and it is possible to continuously generate active oxygen species.

なお、非ドープポリアニリンを電極の表面に塗布して用いる場合は、表面抵抗値が高くなるため、例えば、電子供給材をポリアニリンの層と電極の基材との間に設ける。これにより、ポリアニリンへの電子の供給を容易に行うことが可能となり、電極の基材全体の導電性を向上させることができる。上記電子供給材は、例えば、アルミニウム、チタン、ステンレス、カーボンといった材料から構成されることが好ましい。また、その形状は、粒子状、ハニカム状等、ポリアニリンと接する表面積が大きいものであることが好ましい。   In the case where undoped polyaniline is applied to the surface of the electrode and used, the surface resistance value becomes high. For example, an electron supply material is provided between the polyaniline layer and the electrode substrate. Thereby, it becomes possible to easily supply electrons to the polyaniline, and the conductivity of the entire substrate of the electrode can be improved. The electron supply material is preferably made of a material such as aluminum, titanium, stainless steel, or carbon. In addition, the shape is preferably a particle, honeycomb or the like having a large surface area in contact with polyaniline.

なお、図1及び図2には、最も簡単な例として、水反応槽1内に陰極4と陽極5とを一つずつ配置したものを示している。陰極4や陽極5を水反応槽1内に複数(積層して)配置する場合は、例えば、陽極5に隣接して配置した陰極4の側面のうち、陽極5に対面しない一面を、他の陰極4の一面に対面するように配置する。即ち、「陰極−陽極−陰極」を一組として、この一組或いは複数組を水反応槽1内に並べて配置する。かかる構成であれば、陰極4と陽極5とを交互に配置した場合よりも、活性酸素種の生成効率を向上させることができる。これは、陰極4の設置数に対して陽極5の設置数が少なくなるため、陽極5での活性酸素種の消失反応を抑制することができるためである。   In FIGS. 1 and 2, as the simplest example, one in which one cathode 4 and one anode 5 are arranged in the water reaction tank 1 is shown. In the case where a plurality of (stacked) cathodes 4 and anodes 5 are arranged in the water reaction tank 1, for example, one side of the cathode 4 arranged adjacent to the anode 5 that does not face the anode 5 It arrange | positions so that one surface of the cathode 4 may be faced. That is, “cathode-anode-cathode” is set as one set, and one set or a plurality of sets are arranged in the water reaction tank 1 side by side. With such a configuration, the generation efficiency of the active oxygen species can be improved as compared with the case where the cathodes 4 and the anodes 5 are alternately arranged. This is because the number of anodes 5 installed is less than the number of cathodes 4 installed, and the disappearance reaction of active oxygen species at the anode 5 can be suppressed.

図4は過酸化水素濃度の推移を示す図である。具体的に、図4は、電極の気中露出面積と水中浸漬面積との比を一定にした場合の過酸化水素濃度の推移と、電極の位置を水反応槽1に対して固定した場合の過酸化水素濃度の推移とを示している。なお、図4に示す結果は、電極2の表面にポリアニリンを塗布するとともに、水反応槽1内への水2の追加を行わず、且つ、水2を強制的に循環させる手段を備えていない試験系で得られたものである。   FIG. 4 is a graph showing the transition of the hydrogen peroxide concentration. Specifically, FIG. 4 shows the transition of the hydrogen peroxide concentration when the ratio between the exposed area of the electrode in the air and the area immersed in water is constant, and the case where the position of the electrode is fixed with respect to the water reaction tank 1. It shows the transition of the hydrogen peroxide concentration. The results shown in FIG. 4 indicate that polyaniline is applied to the surface of the electrode 2, the water 2 is not added to the water reaction tank 1, and no means for forcibly circulating the water 2 is provided. It was obtained in a test system.

上記試験系では、水反応槽1内の水2が少しずつ蒸発していくため、水反応槽1の水位は、時間の経過とともに低下する。このため、電極の位置を水反応槽1に対して固定した場合は、時間の経過とともに、活性酸素種の生成に有効に作用する水中浸漬面積が減少してしまう。その結果、図4に示すように、電極の位置を固定した場合は、電極の気中露出面積と水中浸漬面積との比を一定にした場合よりも活性酸素種生成能が徐々に劣化していき、最終的に到達する濃度にも差が生じてしまう。   In the above test system, since the water 2 in the water reaction tank 1 evaporates little by little, the water level in the water reaction tank 1 decreases with time. For this reason, when the position of an electrode is fixed with respect to the water reaction tank 1, the immersion area in water which acts effectively on the production | generation of an active oxygen seed will reduce with progress of time. As a result, as shown in FIG. 4, when the position of the electrode is fixed, the active oxygen species generating ability is gradually deteriorated as compared with the case where the ratio of the exposed area of the electrode in the air to the immersed area in water is constant. As a result, there is a difference in the final concentration.

このように、活性酸素種生成部3に浮遊手段7(保持手段)を備えることにより、電極と水面2aとの位置関係、即ち、電極の気中露出面積と水中浸漬面積との比を、水反応槽1内の水2の量(水位)に関わらず一定に保持することができ、活性酸素種の生成効率を向上させることができる。また、上記構成の活性酸素種生成装置は、電極から金属イオンを溶出させる従来装置と比較して電極寿命が長く、長期間安定して使用することができる。   Thus, by providing the active oxygen species generating unit 3 with the floating means 7 (holding means), the positional relationship between the electrode and the water surface 2a, that is, the ratio of the exposed area of the electrode in the air to the submerged area of the water, Regardless of the amount of water 2 (water level) in the reaction tank 1, it can be kept constant, and the production efficiency of active oxygen species can be improved. In addition, the active oxygen species generating device having the above-described configuration has a longer electrode life than a conventional device that elutes metal ions from an electrode, and can be used stably for a long period of time.

本装置で生成された活性酸素種水は強い酸化力を持つため、この水及びこの水と接触させた物質の抗菌等を行うことができる。
なお、上記抗菌等とは、滅菌、消毒、殺菌、除菌、抗菌を含む概念であり、カビ、ウィルスを含めた微生物や小型水生生物の発生、生育、増殖を抑制或いは死滅させることをいう。
Since the active oxygen species water generated by this apparatus has a strong oxidizing power, it is possible to perform antibacterial and the like of this water and substances brought into contact with this water.
The antibacterial and the like is a concept including sterilization, disinfection, sterilization, sterilization, and antibacterial, and refers to suppressing or killing the generation, growth, and proliferation of microorganisms and small aquatic organisms including molds and viruses.

また、本願において、活性酸素種とは、スーパーオキシド(O)、ヒドロキシラジカル(・OH)、過酸化水素(H)、一重項酸素()、オゾン(O)等、分子状酸素である三重項酸素(O)より活性化された酸素、及びその関連分子のことをいう。 Further, in the present application, the active oxygen species superoxide (O 2 · -), hydroxy radicals (· OH), hydrogen peroxide (H 2 O 2), singlet oxygen (1 O 2), ozone (O 3 ) And the like, and oxygen related to triplet oxygen (O 2 ), which is molecular oxygen, and related molecules.

実施の形態2.
図5はこの発明の実施の形態2における空調機器の構成を示す概略図である。本実施の形態においては、実施の形態1において説明した活性酸素種生成装置(の活性酸素種生成部3)を空調機器に適用した例について説明する。なお、図5には、冷却塔8を有する空調機器を示している。
Embodiment 2. FIG.
FIG. 5 is a schematic diagram showing the configuration of the air-conditioning apparatus according to Embodiment 2 of the present invention. In the present embodiment, an example will be described in which the active oxygen species generating apparatus (the active oxygen species generating unit 3) described in the first embodiment is applied to an air conditioner. FIG. 5 shows an air conditioner having a cooling tower 8.

図5に示すように、空調機器の冷却塔8には、ポンプ9、配管10、熱交換部11、貯水部12(実施の形態1における水反応槽1に相当)、ファン13が備えられている。   As shown in FIG. 5, the cooling tower 8 of the air conditioner includes a pump 9, a pipe 10, a heat exchange unit 11, a water storage unit 12 (corresponding to the water reaction tank 1 in the first embodiment), and a fan 13. Yes.

ポンプ9によって冷却塔8内を循環する水14は、配管10内を図5に示す矢印の方向に通って、熱交換部11に供給される。熱交換部11は、配管10から供給される水14の熱交換を行う。熱交換部11から流下した水14は、貯水部12に溜まるとともに、その一部は、ポンプ9によって配管10内に取り込まれる。なお、ファン13は、熱交換部11において水14を空冷するため、冷却塔8内に外気を取り込むためのものである。   The water 14 circulated in the cooling tower 8 by the pump 9 is supplied to the heat exchange unit 11 through the pipe 10 in the direction of the arrow shown in FIG. The heat exchange unit 11 performs heat exchange of the water 14 supplied from the pipe 10. The water 14 flowing down from the heat exchange unit 11 is collected in the water storage unit 12, and a part of the water 14 is taken into the pipe 10 by the pump 9. The fan 13 is for taking outside air into the cooling tower 8 in order to air-cool the water 14 in the heat exchanging section 11.

実施の形態1において詳細を説明した活性酸素種生成部3は、貯水部12内に配置され、陰極4及び陽極5の下部側が、貯水部12に貯留された水14に浸漬されている。即ち、活性酸素種生成部3の電極は、浮遊手段7によって水面14aに対して常に同じ位置に保持される。   The active oxygen species generating unit 3 described in detail in the first embodiment is disposed in the water storage unit 12, and the lower side of the cathode 4 and the anode 5 is immersed in water 14 stored in the water storage unit 12. That is, the electrode of the active oxygen species generating unit 3 is always held at the same position with respect to the water surface 14 a by the floating means 7.

上記構成を有する空調機器では、運転中は冷却塔8内で水14が循環し、貯水部12内の水量もある程度一定に保たれる。しかし、夜間等、空調機器の運転が停止されると、冷却塔8内の水14が貯水部12に溜まり、冷却塔8全体の水量が変化していないにも関わらず、貯水部12の水位が上昇する。   In the air conditioner having the above configuration, the water 14 circulates in the cooling tower 8 during operation, and the amount of water in the water storage unit 12 is kept constant to some extent. However, when the operation of the air-conditioning equipment is stopped at night or the like, the water 14 in the cooling tower 8 is accumulated in the water storage section 12, and the water level of the water storage section 12 is not changed although the amount of water in the entire cooling tower 8 has not changed. Rises.

このように、内部で水位変動が生じる機器では、活性酸素種生成装置に浮遊手段7(保持手段)が備えられていない場合、高水位時及び低水位時の双方において菌の繁殖を十分に抑制できるように電極を水14に浸漬させなければならず、電極が大型化するといった問題がある。また、高水位時に電極の給電部が水面14a下に配置されてしまう場合は、給電部の劣化を防止するための防水処理を電極に施す必要があり、コストの上昇や設計の手間が発生してしまう。   As described above, in the device in which the water level fluctuates inside, when the active oxygen species generating device is not equipped with the floating means 7 (holding means), the propagation of bacteria is sufficiently suppressed both at the high water level and at the low water level. There is a problem that the electrode must be immersed in the water 14 so that the electrode can be enlarged. In addition, when the power feeding part of the electrode is disposed below the water surface 14a at a high water level, it is necessary to perform a waterproofing treatment on the electrode to prevent deterioration of the power feeding part, resulting in an increase in cost and time for designing. End up.

本構成の空調機器(活性酸素種生成装置)であれば、このような問題が発生することはなく、実施の形態1と同様の効果を奏することが可能である。
なお、活性酸素種生成装置自体の構成は、実施の形態1と同様である。
If it is an air-conditioning apparatus (active oxygen species production | generation apparatus) of this structure, such a problem will not generate | occur | produce and it can have an effect similar to Embodiment 1. FIG.
The configuration of the active oxygen species generator itself is the same as that of the first embodiment.

実施の形態1に示した活性酸素種生成装置(活性酸素種生成部3)は、空調機器の他、給湯装置や下水等の処理施設においても適用することができる。本活性酸素種生成装置は、水中の菌を抑制する他、カビの繁殖の抑制や水の脱臭を目的とした技術にも応用することができる。   The active oxygen species generator (active oxygen species generator 3) shown in the first embodiment can be applied not only to air conditioners but also to processing facilities such as a hot water supply device and sewage. This active oxygen species generating device can be applied to techniques aimed at suppressing fungal growth and deodorizing water in addition to suppressing fungi in water.

1 水反応槽
2、14 水
2a、14a 水面(喫水線)
3 活性酸素種生成部
4 陰極
5 陽極
6 電圧印加手段
7 浮遊手段
8 冷却塔
9 ポンプ
10 配管
11 熱交換部
12 貯水部
13 ファン
1 Water reaction tank 2, 14 Water 2a, 14a Water surface (draft)
DESCRIPTION OF SYMBOLS 3 Active oxygen seed production | generation part 4 Cathode 5 Anode 6 Voltage application means 7 Floating means 8 Cooling tower 9 Pump 10 Piping 11 Heat exchange part 12 Water storage part 13 Fan

Claims (6)

電極反応により活性酸素種を生成する活性酸素種生成装置を冷却塔に備えた空調機器であって、
前記冷却塔は、
水を循環させるためのポンプと、
前記ポンプによって循環される水の熱交換を行うための熱交換部と、
前記熱交換部から流下した水が貯留される貯水部と、
を備え、
前記活性酸素種生成装置は、
各一部が、前記貯水部に貯留された水の水面から突出し、各他部が前記貯水部に貯留された水に浸漬された陰極及び陽極と、
前記陰極及び前記陽極の気中露出面積と水中浸漬面積との比を、前記貯水部内の水位変動に関わらず、一定に保持するための保持手段と、
を備えた空調機器。
An air conditioner equipped with an active oxygen species generating device for generating active oxygen species by an electrode reaction in a cooling tower,
The cooling tower is
A pump for circulating water,
A heat exchange section for performing heat exchange of water circulated by the pump;
A water storage part in which water flowing down from the heat exchange part is stored;
With
The active oxygen species generator is
Each part protrudes from the surface of the water stored in the water storage part, and each other part is immersed in water stored in the water storage part , a cathode and an anode,
A holding means for holding the cathode and the ratio of the exposed area in the air of the anode and the area immersed in water constant regardless of the water level fluctuation in the water reservoir;
Air conditioning equipment equipped with .
前記保持手段は、前記陰極及び前記陽極を前記貯水部内の水に浮遊させる浮遊手段からなる請求項1に記載の空調機器The air conditioner according to claim 1, wherein the holding unit includes a floating unit that floats the cathode and the anode in the water in the water storage unit . 前記陰極及び前記陽極は、前記貯水部内の水面に対して垂直方向に配置された請求項1又は請求項2に記載の空調機器The air conditioner according to claim 1 or 2, wherein the cathode and the anode are arranged in a direction perpendicular to a water surface in the water storage section . 前記陰極は、その表面が活性酸素種生成能を有する所定の材料で被覆された請求項1から請求項3の何れかに記載の空調機器The air conditioner according to any one of claims 1 to 3, wherein a surface of the cathode is coated with a predetermined material having an active oxygen species generating ability. 前記陰極を被覆する材料は、所定のレドックスポリマーである請求項4に記載の空調機器The air conditioner according to claim 4, wherein the material covering the cathode is a predetermined redox polymer. 前記陰極及び前記陽極は、前記貯水部内にそれぞれ複数配置された請求項1から請求項5の何れかに記載の空調機器The cathode and the anode, air conditioning equipment according to any one of claims 1 to 5, respectively in the reservoir has a plurality of arranged.
JP2011085091A 2011-04-07 2011-04-07 Air conditioning equipment Expired - Fee Related JP5310772B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2011085091A JP5310772B2 (en) 2011-04-07 2011-04-07 Air conditioning equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2011085091A JP5310772B2 (en) 2011-04-07 2011-04-07 Air conditioning equipment

Publications (2)

Publication Number Publication Date
JP2012217908A JP2012217908A (en) 2012-11-12
JP5310772B2 true JP5310772B2 (en) 2013-10-09

Family

ID=47270032

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2011085091A Expired - Fee Related JP5310772B2 (en) 2011-04-07 2011-04-07 Air conditioning equipment

Country Status (1)

Country Link
JP (1) JP5310772B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5444186B2 (en) * 2010-10-20 2014-03-19 株式会社東芝 Hydrogen peroxide water generator and sterilization system

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09310190A (en) * 1996-05-21 1997-12-02 Toyo Tanso Kk Floating electrode for electrochemical reaction and electrolytic cell using the same electrode
JP2002035097A (en) * 2000-07-28 2002-02-05 Kenichi Morita Gas deodorizing and sterilizing device and method
JP4198169B2 (en) * 2006-10-20 2008-12-17 三洋電機株式会社 Descaling system
JP5213793B2 (en) * 2009-05-13 2013-06-19 三菱電機株式会社 Active oxygen generator, humidifier, air purifier

Also Published As

Publication number Publication date
JP2012217908A (en) 2012-11-12

Similar Documents

Publication Publication Date Title
Shapira et al. Side reactions in capacitive deionization (CDI) processes: the role of oxygen reduction
Xu et al. Electrogeneration of hydrogen peroxide using Ti/IrO2–Ta2O5 anode in dual tubular membranes Electro-Fenton reactor for the degradation of tricyclazole without aeration
US20070017801A1 (en) High electric field electrolysis cell
WO2008059331A2 (en) Bioelectrochemical reactor
Chatterjee et al. Design of clayware separator-electrode assembly for treatment of wastewater in microbial fuel cells
KR101163365B1 (en) Floating-type microbial fuel cell
Shin et al. The enhancement of ammonium removal from ethanolamine wastewater using air-cathode microbial fuel cells coupled to ferric reduction
Dinh et al. Lactate and acetate applied in dual‐chamber microbial fuel cells with domestic wastewater
JP5310772B2 (en) Air conditioning equipment
JP5332196B2 (en) Microbial power generation method and microbial power generation apparatus
KR20060007369A (en) High field electrolytic cell
JP5212486B2 (en) Reactive oxygen species generator
JP2002346566A (en) Apparatus and method for water treatment
JP2014188018A (en) Air purifier
JP5355572B2 (en) Sterilization and antibacterial equipment
Wang et al. Flow shear stress applied in self-buffered microbial fuel cells
JP2011162838A (en) Active oxygen species generator
JP5445522B2 (en) Water heater, air conditioner
CN113880196A (en) Bipolar cooperative penetration type electro-Fenton device and method for degrading florfenicol
WO2010050354A1 (en) Microbial power generation method and microbial power generation device
JP2021182552A (en) Fuel cell system comprising antimicrobial patterned surface
JP2016120454A (en) Promotion oxidation water treatment method
JP5093437B2 (en) Bacteria control method for fuel cell system
JP6111417B2 (en) Air sterilization deodorization device
CN217377391U (en) Efficiency increasing mechanism for electrochemical water treatment device

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20130411

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20130416

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20130515

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: 20130604

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20130617

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

Ref document number: 5310772

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees