JP2009039560A - Air disinfection apparatus - Google Patents
Air disinfection apparatus Download PDFInfo
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- JP2009039560A JP2009039560A JP2008273776A JP2008273776A JP2009039560A JP 2009039560 A JP2009039560 A JP 2009039560A JP 2008273776 A JP2008273776 A JP 2008273776A JP 2008273776 A JP2008273776 A JP 2008273776A JP 2009039560 A JP2009039560 A JP 2009039560A
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- electrolyzed water
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- 238000004659 sterilization and disinfection Methods 0.000 title claims abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 68
- 239000007788 liquid Substances 0.000 claims abstract description 58
- 230000001954 sterilising effect Effects 0.000 claims description 24
- 230000001737 promoting effect Effects 0.000 claims description 21
- 238000011144 upstream manufacturing Methods 0.000 claims description 3
- 235000019645 odor Nutrition 0.000 claims 1
- 230000000249 desinfective effect Effects 0.000 abstract 1
- 239000003507 refrigerant Substances 0.000 description 29
- 238000001816 cooling Methods 0.000 description 17
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical class [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 12
- 239000003595 mist Substances 0.000 description 11
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 10
- QWPPOHNGKGFGJK-UHFFFAOYSA-N hypochlorous acid Chemical compound ClO QWPPOHNGKGFGJK-UHFFFAOYSA-N 0.000 description 10
- 241000700605 Viruses Species 0.000 description 9
- 238000010438 heat treatment Methods 0.000 description 8
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 7
- 239000000460 chlorine Substances 0.000 description 7
- 239000008399 tap water Substances 0.000 description 7
- 235000020679 tap water Nutrition 0.000 description 7
- 229910052760 oxygen Inorganic materials 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 238000005868 electrolysis reaction Methods 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 239000011780 sodium chloride Substances 0.000 description 5
- 238000012546 transfer Methods 0.000 description 5
- 229910052801 chlorine Inorganic materials 0.000 description 4
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000000779 smoke Substances 0.000 description 4
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 3
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Substances [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 3
- 230000002441 reversible effect Effects 0.000 description 3
- 241000712461 unidentified influenza virus Species 0.000 description 3
- 238000004378 air conditioning Methods 0.000 description 2
- 229910010293 ceramic material Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 208000015181 infectious disease Diseases 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 230000000474 nursing effect Effects 0.000 description 2
- 238000011045 prefiltration Methods 0.000 description 2
- 239000003642 reactive oxygen metabolite Substances 0.000 description 2
- 239000010936 titanium Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- -1 Chlorine ions Chemical class 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 102000018697 Membrane Proteins Human genes 0.000 description 1
- 108010052285 Membrane Proteins Proteins 0.000 description 1
- 230000010718 Oxidation Activity Effects 0.000 description 1
- OUUQCZGPVNCOIJ-UHFFFAOYSA-M Superoxide Chemical compound [O-][O] OUUQCZGPVNCOIJ-UHFFFAOYSA-M 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000002528 anti-freeze Effects 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003411 electrode reaction Methods 0.000 description 1
- TUJKJAMUKRIRHC-UHFFFAOYSA-N hydroxyl Chemical compound [OH] TUJKJAMUKRIRHC-UHFFFAOYSA-N 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910052741 iridium Inorganic materials 0.000 description 1
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- LEYNFUIKYCSXFM-UHFFFAOYSA-N platinum tantalum Chemical compound [Ta][Pt][Ta] LEYNFUIKYCSXFM-UHFFFAOYSA-N 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
- Central Air Conditioning (AREA)
Abstract
Description
本発明は、空気除菌装置に係り、特に、空中浮遊微生物ウィルス等の除去が可能な空気除菌装置に関する。 The present invention relates to an air sterilization apparatus, and more particularly to an air sterilization apparatus capable of removing airborne microbial viruses and the like.
一般に、空中浮遊微生物ウィルス等の除去を目的として、空気中に電解水ミストを拡散させて、この電解水ミストを空中浮遊微生物に直接接触させ、ウィルス等を不活化する除菌装置が提案されている(例えば、特許文献1参照)。
しかしながら、上記除菌装置では、微粒子状の電解水ミストが到達しやすい使用環境下、すなわち、比較的小空間では効力を発揮するものの、電解水ミストが到達しにくい使用環境下、すなわち、大空間、例えば幼稚園や小・中・高等学校や、介護保険施設や、病院等では効力を発揮しにくいという問題がある。
そこで、本発明の目的は、上述した従来の技術が有する課題を解消し、たとえば大空間等の室内の空気の除菌が可能な空気除菌装置を提供することにある。
However, in the sterilization apparatus described above, it is effective in a use environment where fine particulate electrolyzed water mist easily reaches, that is, in a use environment where electrolyzed water mist is difficult to reach while being effective in a relatively small space, that is, a large space. For example, there is a problem that it is difficult to exert its effect in kindergartens, elementary / middle / high schools, nursing care insurance facilities, hospitals, and the like.
Accordingly, an object of the present invention is to provide an air sterilization apparatus capable of eliminating the problems of the conventional techniques described above and capable of sterilizing indoor air such as a large space.
本発明は、本体に気液接触促進部材とその上方に位置する散水器とが収納され、空気をこの本体に導いて前記気液接触促進部材を通ってこの本体から室内へと流すようにした空気除菌装置において、前記散水器から前記気液接触促進部材に滴下される水は電解水であることを特徴とする空気除菌装置。 In the present invention, a gas-liquid contact facilitating member and a sprinkler located above the main body are housed in the main body, and air is guided to the main body so as to flow from the main body into the room through the gas-liquid contact facilitating member. In the air sterilization apparatus, water dropped from the sprinkler to the gas-liquid contact promoting member is electrolyzed water.
本発明では、本体に電解水を供給すると共に、この電解水により本体に導入した空気を除菌して、この除菌した空気を室内に導く構成としたため、この除菌した空気を遠くに飛ばすことが可能になり、空気除菌が効率よく達成される。 In the present invention, the electrolyzed water is supplied to the main body, the air introduced into the main body is sterilized by the electrolyzed water, and the sterilized air is guided into the room, so that the sterilized air is blown away. Air sterilization can be achieved efficiently.
さらに、前記気液接触促進部材から滴下した電解水は、本体の下方に溜められて前記散水器を介して再び前記気液接触促進部材に滴下させるようにしてもよい。 Furthermore, the electrolyzed water dropped from the gas-liquid contact promoting member may be stored below the main body and dropped again onto the gas-liquid contact promoting member via the watering device.
前記電解水は前記気液接触促進部材に沿って上から下に向けて流れ落ちると共に、この本体に導かれた空気は気液接触促進部材に沿って下から上に向かって流れるようにしても良い。 The electrolyzed water may flow down from top to bottom along the gas-liquid contact promoting member, and the air guided to the main body may flow from bottom to top along the gas-liquid contact promoting member. .
前記気液接触促進部材から滴下した電解水を再び前記気液接触促進部材に滴下させる流路には電極が配置され、この電極の通電により次亜塩素酸を発生させるようにしてもよい。 An electrode may be disposed in a flow path in which the electrolyzed water dropped from the gas-liquid contact promoting member is dropped again on the gas-liquid contact promoting member, and hypochlorous acid may be generated by energization of the electrode.
前記流路には前記電極の下流側および/又は上流側に循環ポンプが配置されている。 A circulation pump is disposed in the flow path downstream and / or upstream of the electrode.
本体から流出されて室内に導かれる空気は、この本体の上部から流出されその後略直角に折り曲げられた風路を介して室内へと導かれる。 The air that flows out from the main body and is led into the room is led into the room through an air passage that flows out from the upper part of the main body and is bent at a substantially right angle.
本発明によれば、本体を用いて、除菌された空気を室内に戻す構成としたため、除菌した空気を、大空間の遠くに飛ばすことが可能になり、大空間等の室内での空気除菌が効率よく達成される。 According to the present invention, since the sterilized air is returned to the room using the main body, the sterilized air can be blown far away from the large space. Sterilization is achieved efficiently.
以下、図面を参照して本発明の実施の形態について説明する。
図1は、本実施の形態による空気除菌装置を示す。
この空気除菌装置は気液接触塔Cを備え、この気液接触塔Cは本体(以下「気液接触塔本体100」と言う。)を備える。この気液接触塔本体100には、セラミック材料で形成されたプレート状の複数の気液接触促進部材301、302、303…が、縦方向に間隔をあけた状態で、ブロック状に組み合わせて配置される。
Embodiments of the present invention will be described below with reference to the drawings.
FIG. 1 shows an air sterilization apparatus according to this embodiment.
The air sterilization apparatus includes a gas-liquid contact tower C, and the gas-liquid contact tower C includes a main body (hereinafter referred to as “gas-liquid contact tower main body 100”). In this gas-liquid contact tower body 100, a plurality of plate-like gas-liquid contact facilitating members 301, 302, 303... Made of a ceramic material are arranged in combination in a block shape with intervals in the vertical direction. Is done.
この気液接触促進部材301、302、303…の上方には散水器32が配置され、この散水器32には、電解水を供給する供給手段105が接続されている。106は、散水器32から散水された電解水を供給手段105に循環させる循環手段である。供給手段105は、上流側から順に、飽和食塩水タンク61と、第1ポンプ62と、食塩水タンク63と、電解槽64と、第2ポンプ65と、濃度調整槽66とを含んで構成される。飽和食塩水タンク61には飽和食塩水が貯留され、この飽和食塩水は、第1ポンプ62により、食塩水タンク63にくみ出される。 A watering device 32 is disposed above the gas-liquid contact promoting members 301, 302, 303, and the watering device 32 is connected to a supply means 105 for supplying electrolyzed water. 106 is a circulation means for circulating the electrolyzed water sprayed from the water sprinkler 32 to the supply means 105. The supply means 105 includes a saturated saline tank 61, a first pump 62, a saline tank 63, an electrolytic bath 64, a second pump 65, and a concentration adjusting bath 66 in this order from the upstream side. The Saturated saline is stored in the saturated saline tank 61, and this saturated saline is pumped into the saline tank 63 by the first pump 62.
この食塩水タンク63には、水道水貯留タンク(または水道管)67から適宜水道水が供給され、タンク内食塩水濃度が、例えば2〜3%濃度に調整される。この食塩水は電解槽64に供給される。電解槽64には、カソード電極とアノード電極からなる一対の電極71が収容され、この電極71に通電することにより、食塩水が電気分解されて、活性酸素種を含んだ電解水(0.5〜1%)が生成される。なお、72は電極制御装置である。ここで、活性酸素種とは、通常の酸素よりも高い酸化活性を持つ酸素分子と、その関連物質のことであり、スーパーオキシドアニオン、一重項酸素、ヒドロキシルラジカル、或いは過酸化水素といった、いわゆる狭義の活性酸素に、オゾン、次ハロゲン酸等といった、いわゆる広義の活性酸素を含めたものとする。この活性酸素種は、空気中に、例えばインフルエンザウィルスが侵入した場合、その感染に必須の当該ウィルスの表面蛋白(スパイク)を破壊、消失(除去)する機能を持ち、これを破壊すると、インフルエンザウィルスと、当該ウィルスが感染するのに必要な受容体(レセプタ)とが結合しなくなり、これによって感染が阻止される。衛生環境研究所との共同による実証試験の結果、インフルエンザウィルスが侵入した空気を、電解水に接触させた場合、インフルエンザウィルスを99%以上除去できることが判明した。 The saline tank 63 is appropriately supplied with tap water from a tap water storage tank (or water pipe) 67, and the saline concentration in the tank is adjusted to, for example, a 2 to 3% concentration. This saline solution is supplied to the electrolytic cell 64. The electrolytic cell 64 accommodates a pair of electrodes 71 composed of a cathode electrode and an anode electrode, and when the electrode 71 is energized, the saline solution is electrolyzed and electrolyzed water containing active oxygen species (0.5%). ~ 1%) is produced. Reference numeral 72 denotes an electrode control device. Here, the reactive oxygen species are oxygen molecules having an oxidation activity higher than that of normal oxygen and related substances, and so-called narrow definition such as superoxide anion, singlet oxygen, hydroxyl radical, or hydrogen peroxide. These active oxygens include so-called broadly active oxygens such as ozone and hypohalogen acids. This reactive oxygen species has a function of destroying and eliminating (removing) the surface protein (spike) of the virus essential for infection when, for example, influenza virus enters the air. And the receptor (receptor) necessary for the virus to infect, and the infection is thereby blocked. As a result of a joint test with the Institute for Hygiene and Environment, it was found that 99% or more of the influenza virus can be removed when the air in which the influenza virus has entered is brought into contact with electrolyzed water.
一対の電極71は、例えばベースがTi(チタン)で皮膜層がIr(イリジウム)、Pt(白金)から構成された電極板であり、この電極71に印加する電流値は、電流密度で20mA(ミリアンペア)/cm2(平方センチメートル)として、所定の遊離残留塩素
濃度(例えば1mg(ミリグラム)/l(リットル))を発生させる。上記電極71により食塩水に通電すると、カソード電極では、
4H++4e-+(4OH-)→2H2+(4OH-)
の反応が起こり、アノード電極では、
2H2O→4H++O2+4e-
の反応が起こると同時に、
水に含まれる塩素イオン(水道水に予め添加されているもの)が、
2Cl-→Cl2+2e-
のように反応し、さらにこのCl2は水と反応し、
Cl2+H2O→HClO+HCl
となる。
The pair of electrodes 71 are, for example, electrode plates in which the base is made of Ti (titanium) and the coating layer is made of Ir (iridium) or Pt (platinum). The current value applied to the electrodes 71 is 20 mA (current density). A predetermined free residual chlorine concentration (for example, 1 mg (milligram) / l (liter)) is generated as milliampere / cm 2 (square centimeter). When the saline is energized by the electrode 71, the cathode electrode:
4H + + 4e − + (4OH − ) → 2H 2 + (4OH − )
And the anode electrode
2H 2 O → 4H + + O 2 + 4e −
As soon as the reaction of
Chlorine ions contained in water (pre-added to tap water)
2Cl − → Cl 2 + 2e −
In addition, this Cl 2 reacts with water,
Cl 2 + H 2 O → HClO + HCl
It becomes.
この電解水は第2ポンプ65によりくみ出され、濃度調整槽66に送られる。この濃度調整槽66には塩素センサ(図示せず)が配置され、この塩素センサの出力に応じ、水道水貯留タンク67から水が供給され、槽66内が10〜1000ppmの濃度に調整され、散水器32に供給される。 This electrolyzed water is pumped out by the second pump 65 and sent to the concentration adjusting tank 66. A chlorine sensor (not shown) is disposed in the concentration adjustment tank 66, water is supplied from the tap water storage tank 67 according to the output of the chlorine sensor, and the inside of the tank 66 is adjusted to a concentration of 10 to 1000 ppm. It is supplied to the sprinkler 32.
散水器32から散水された電解水は、蒸発式補助熱交換器30の表面(電解水接触部)に接触し、下に流れて、気液接触塔本体100の下部に貯留される。ここには、上述した循環手段106が接続されている。この循環手段106は、フィルタ73および第3ポンプ74を含み、気液接触塔本体100の下部に貯留した電解水は、第3ポンプ74により、電解槽64(供給手段)に環流される。 The electrolyzed water sprayed from the water sprinkler 32 contacts the surface of the evaporative auxiliary heat exchanger 30 (electrolyzed water contact portion), flows downward, and is stored in the lower part of the gas-liquid contact tower body 100. Here, the circulation means 106 described above is connected. The circulation means 106 includes a filter 73 and a third pump 74, and the electrolyzed water stored in the lower part of the gas-liquid contact tower body 100 is circulated to the electrolytic cell 64 (supply means) by the third pump 74.
気液接触塔本体100には、吸気部101を介して室内戻り空気が導入され、その空気は、排気部102を経て再び室内に戻される。そして、吸気部101は、吸気ダクト44を含み、この吸気ダクト44にはプレフィルタ45、送風機46が配置され、また、排気部(導入手段)102は、排気ダクト47を含み、この排気ダクト47にはミストトラップ48が配設されている。 Indoor return air is introduced into the gas-liquid contact tower main body 100 via the intake portion 101, and the air is returned to the room again via the exhaust portion 102. The intake section 101 includes an intake duct 44, a pre-filter 45 and a blower 46 are disposed in the intake duct 44, and the exhaust section (introducing means) 102 includes an exhaust duct 47, and the exhaust duct 47 A mist trap 48 is disposed on the side.
本構成では、電極71に通電することで、殺菌力の大きいHClO(次亜塩素酸)が発生し、この次亜塩素酸は散水器32を経て、気液接触促進部材(電解水接触部)301、302、303…に供給される。この散水器32からの電解水は、気液接触促進部材301、302、303…の間を、プレート(気液接触促進部材)に沿って、上から下にむけて流れ落ちると共に、室内戻り空気は、送風機46により送風されて下から上にむけて、プレートに沿って循環する。 In this configuration, when the electrode 71 is energized, HClO (hypochlorous acid) having a high sterilizing power is generated, and this hypochlorous acid passes through the sprinkler 32 and is a gas-liquid contact promoting member (electrolyzed water contact portion). 301, 302, 303... The electrolyzed water from the water sprinkler 32 flows down from the top to the bottom along the plate (gas-liquid contact promoting member) between the gas-liquid contact promoting members 301, 302, 303. The air is blown by the blower 46 and circulates along the plate from the bottom to the top.
これにより、ここを通過する空気中に浮遊するウィルスを不活化することができ、かつ、気液接触促進部材の表面で雑菌が繁殖することを防止できる。
また、ここを通過する際に、臭気も、電解水中の次亜塩素酸と反応し、イオン化して溶解し、空気中から除去されるため、脱臭される。ここで除菌、および脱臭された空気は、送風機46により送風されて、略直角に折り曲げられた風路(以下「排気ダクト47」と言う。)を通じて、例えばアリーナやドーム等で呼称される多数の人が集まる大空間に戻される。
本構成では、クーリングタワー状の気液接触塔Cを用いて、除菌された空気を室内に戻す構成としたため、除菌した空気を、大空間の遠くに飛ばすことが可能になり、大空間での空気除菌が効率よく達成される。
Thereby, the virus which floats in the air which passes here can be inactivated, and various bacteria can be prevented from breeding on the surface of the gas-liquid contact promoting member.
Further, when passing through here, the odor is also deodorized because it reacts with hypochlorous acid in the electrolytic water, is ionized and dissolved, and is removed from the air. Here, the sterilized and deodorized air is blown by the blower 46 and is passed through an air passage (hereinafter, referred to as “exhaust duct 47”) bent substantially at a right angle, for example, in many arenas and dome. It is returned to the large space where people gather.
In this configuration, the cooling tower-shaped gas-liquid contact tower C is used to return the sterilized air to the room, so that the sterilized air can be blown far away from the large space. Air sterilization can be achieved efficiently.
気液接触塔Cでは、送風機46により取入れた室内戻り空気と、上部の散水器32より滴下される水を接触させる。そのため、気液接触塔内に取入れられた空気は、水の一部が蒸発した水蒸気を含み、高温多湿の空気となって排気部102に至る。
これを放置した場合、高温多湿の空気が大気中で冷却される過程で結露し、多量の霧となり白煙が発生する。本構成では、排気ダクト47にミストトラップ48が配設されたため、空気中のミスト分が除去される。したがって、冷却の過程で結露しなくなり、白煙の発生が抑制される。
In the gas-liquid contact tower C, the indoor return air taken in by the blower 46 is brought into contact with the water dripped from the upper sprinkler 32. Therefore, the air taken into the gas-liquid contact tower contains water vapor in which a part of the water is evaporated, and becomes high-temperature and high-humidity air and reaches the exhaust section 102.
If left unattended, condensation occurs in the process of cooling hot and humid air in the atmosphere, resulting in a large amount of fog and white smoke. In this configuration, since the mist trap 48 is disposed in the exhaust duct 47, the mist in the air is removed. Therefore, condensation does not occur in the cooling process, and generation of white smoke is suppressed.
気液接触促進部材301、302、303…は、スケールが付着しにくいように、セラミック材料により形成されている。
それでも万一スケールが付着した場合、プレート状の複数の気液接触促進部材301、302、303…が、ブロック状に組み合わせて配置されているため、気液接触促進部材をブロック単位で交換することができ、或いは、取り出してからスケールを除去する等、メンテナンスを容易にすることができる。
The gas-liquid contact promoting members 301, 302, 303,... Are made of a ceramic material so that the scale is difficult to adhere.
If the scale still adheres, the plurality of plate-like gas-liquid contact promoting members 301, 302, 303,... Are arranged in a block form, so that the gas-liquid contact promoting members are replaced in units of blocks. Alternatively, maintenance can be facilitated by removing the scale after removal.
図2は、別の実施の形態を示す。 この実施の形態では、気液接触塔Cが冷暖房装置と組み合わせて構成されている。この冷暖房装置は、室外ユニットaと、室内ユニットbと、気液接触塔(クーリングタワーユニット)Cとで構成されている。
11は圧縮機、12は四方弁、13は熱源側熱交換器、13aは送風装置、14は冷房用減圧装置、15は暖房用減圧装置、16は暖房時に冷房用減圧装置14を閉止する逆止弁、17は冷房時に暖房用減圧装置15を閉止する逆止弁、18は第1補助熱交換器であり、これらを環状に連接し、熱源側冷媒サイクルを形成している。19は第2補助熱交換器で、第1補助熱交換器18と熱交換するように一体に形成されている。20は冷媒搬送装置で冷房と暖房で冷媒の流出方向が反対となる可逆特性を持っている。これらは、室外ユニットaに収納されている。
FIG. 2 shows another embodiment. In this embodiment, the gas-liquid contact tower C is configured in combination with a cooling / heating device. This air conditioner is composed of an outdoor unit a, an indoor unit b, and a gas-liquid contact tower (cooling tower unit) C.
11 is a compressor, 12 is a four-way valve, 13 is a heat source side heat exchanger, 13a is a blower, 14 is a cooling decompressor, 15 is a heating decompressor, and 16 is a reverse that closes the cooling decompressor 14 during heating. A check valve, 17 is a check valve for closing the heating pressure reducing device 15 during cooling, and 18 is a first auxiliary heat exchanger, which are connected in an annular shape to form a heat source side refrigerant cycle. Reference numeral 19 denotes a second auxiliary heat exchanger, which is integrally formed so as to exchange heat with the first auxiliary heat exchanger 18. Reference numeral 20 denotes a refrigerant transfer device having reversible characteristics in which the refrigerant outflow direction is opposite between cooling and heating. These are stored in the outdoor unit a.
室内ユニットbには、利用側熱交換器23が収納され、この利用側熱交換器23には接続配管41,42を介して第2補助熱交換器19が環状に連接され、これにより、利用側冷媒サイクルが形成されている。 In the indoor unit b, the use side heat exchanger 23 is accommodated, and the second auxiliary heat exchanger 19 is connected to the use side heat exchanger 23 via connection pipes 41 and 42 in an annular shape. A side refrigerant cycle is formed.
気液接触塔Cの気液接触塔本体100には、利用側冷媒サイクルの熱を放熱する蒸発式補助熱交換器30が配置されている。
この蒸発式補助熱交換器30は複数のプレート型熱交換器からなり、例えばブロック状に配列され、ブロック毎に交換、再生が可能である。この蒸発式補助熱交換器30は、第2補助熱交換器19と直列に設けられ、水の蒸発潜熱で冷媒を冷却するもので、後述するように電解水接触部となっている。34a、34bは蒸発式補助熱交換器30へ利用側冷媒サイクルの冷媒流通を調整する三方流量弁である。
In the gas-liquid contact tower main body 100 of the gas-liquid contact tower C, an evaporative auxiliary heat exchanger 30 that dissipates the heat of the use-side refrigerant cycle is disposed.
The evaporative auxiliary heat exchanger 30 includes a plurality of plate-type heat exchangers, which are arranged in a block shape, for example, and can be exchanged and regenerated for each block. The evaporative auxiliary heat exchanger 30 is provided in series with the second auxiliary heat exchanger 19 and cools the refrigerant with the latent heat of evaporation of water, and serves as an electrolyzed water contact portion as will be described later. Reference numerals 34 a and 34 b denote three-way flow valves that adjust the refrigerant flow of the use-side refrigerant cycle to the evaporative auxiliary heat exchanger 30.
気液接触塔本体100には、吸気部101を介して室内戻り空気が導入され、その空気は、排気部102を経て再び室内に戻される。そして、吸気部101は、吸気ダクト44を含み、この吸気ダクト44にはプレフィルタ45、送風機46が配置される。また、排気部(導入手段)102は、排気ダクト47を含み、この排気ダクト47にはミストトラップ48が配設される。 Indoor return air is introduced into the gas-liquid contact tower main body 100 via the intake portion 101, and the air is returned to the room again via the exhaust portion 102. The intake section 101 includes an intake duct 44, and a prefilter 45 and a blower 46 are disposed in the intake duct 44. The exhaust part (introducing means) 102 includes an exhaust duct 47, and a mist trap 48 is disposed in the exhaust duct 47.
気液接触塔Cでは、送風機46により取入れた室内戻り空気と、上部の散水器32より滴下される水を接触させ、水が蒸発する際の潜熱を利用して、蒸発式補助熱交換器30を冷却する。そのため、気液接触塔内に取入れられた空気は、水の一部が蒸発した水蒸気を含み、高温多湿の空気となって排気部102に至る。
これを放置した場合、高温多湿の空気が大気中で冷却される過程で結露し、多量の霧となり白煙が発生する。本構成では、排気ダクト47にミストトラップ48が配設されたため、空気中のミスト分が除去される。したがって、冷却の過程で結露しなくなり、白煙の発生が抑制される。
In the gas-liquid contact tower C, the indoor return air taken in by the blower 46 is brought into contact with the water dropped from the upper sprinkler 32, and the latent heat generated when the water evaporates is used to evaporate the auxiliary heat exchanger 30. Cool down. Therefore, the air taken into the gas-liquid contact tower contains water vapor in which a part of the water is evaporated, and becomes high-temperature and high-humidity air and reaches the exhaust section 102.
If left unattended, condensation occurs in the process of cooling hot and humid air in the atmosphere, resulting in a large amount of fog and white smoke. In this configuration, since the mist trap 48 is disposed in the exhaust duct 47, the mist in the air is removed. Therefore, condensation does not occur in the cooling process, and generation of white smoke is suppressed.
散水器32に電解水を供給する供給手段105と、電解水を供給手段105に循環させる循環手段106とは、上記実施の形態と同様構成であるため、同一部品に同一符号を付して示し説明を省略する。 The supply means 105 for supplying the electrolyzed water to the sprinkler 32 and the circulation means 106 for circulating the electrolyzed water to the supply means 105 have the same configuration as in the above embodiment, and therefore the same parts are denoted by the same reference numerals. Description is omitted.
この構成では、電極71に通電することで、殺菌力の大きいHClO(次亜塩素酸)が発生し、次亜塩素酸が散水器32を経て蒸発式補助熱交換器30の表面(電解水接触部)に供給される。よって、蒸発式補助熱交換器30の表面で雑菌が繁殖することを防止でき、かつ、ここを通過する空気中に浮遊するウィルスを不活化することができる。また、ここを通過する際に、臭気も、電解水中の次亜塩素酸と反応し、イオン化して溶解することで、空気中から除去され、脱臭される。 In this configuration, when the electrode 71 is energized, HClO (hypochlorous acid) having a high sterilizing power is generated, and the hypochlorous acid passes through the sprinkler 32 to the surface of the evaporative auxiliary heat exchanger 30 (electrolyzed water contact). Part). Therefore, it is possible to prevent germs from growing on the surface of the evaporative auxiliary heat exchanger 30 and to inactivate viruses floating in the air passing therethrough. Moreover, when passing through here, the odor also reacts with hypochlorous acid in the electrolyzed water, and is ionized and dissolved to be removed from the air and deodorized.
散水器32から散水された電解水は、蒸発式補助熱交換器30の表面(電解水接触部)に接触し、下に流れて、気液接触塔本体100の下部に貯留される。ここには、上記循環手段106が接続されている。 The electrolyzed water sprayed from the water sprinkler 32 contacts the surface of the evaporative auxiliary heat exchanger 30 (electrolyzed water contact portion), flows downward, and is stored in the lower part of the gas-liquid contact tower body 100. Here, the circulation means 106 is connected.
次に、冷暖房装置についてその動作を説明する。
外気温度が高い時の通常の冷房運転時は図中実線矢印の冷媒サイクルとなり、熱源側冷媒サイクルでは、圧縮機11からの高温高圧ガスは四方弁12を通り、熱源側熱交換器13で放熱して凝縮液化し、逆止弁16を通って冷房用膨張弁14で減圧され、第1補助熱交換器18で蒸発して四方弁12を通り、圧縮機11へ循環する。
Next, the operation of the air conditioner will be described.
During normal cooling operation when the outside air temperature is high, the refrigerant cycle is indicated by a solid arrow in the figure, and in the heat source side refrigerant cycle, the high-temperature and high-pressure gas from the compressor 11 passes through the four-way valve 12 and is radiated by the heat source side heat exchanger 13. Then, it is condensed and liquefied, reduced in pressure by the cooling expansion valve 14 through the check valve 16, evaporated in the first auxiliary heat exchanger 18, passed through the four-way valve 12, and circulated to the compressor 11.
この時、利用側冷媒サイクルの第2補助熱交換器19と第1補助熱交換器18が熱交換し、利用側冷媒サイクルのガス冷媒が冷却されて液化し、冷媒搬送装置20に送られ、この冷媒搬送装置20によって接続配管を通って利用側熱交換器23へ送られて冷房して吸熱蒸発し、ガス化して接続配管を通って第2補助熱交換器19に循環する。 At this time, the second auxiliary heat exchanger 19 and the first auxiliary heat exchanger 18 of the use side refrigerant cycle exchange heat, the gas refrigerant of the use side refrigerant cycle is cooled and liquefied, and sent to the refrigerant transfer device 20, This refrigerant transfer device 20 is sent to the use-side heat exchanger 23 through the connection pipe, is cooled and evaporates with heat, is gasified, and circulates to the second auxiliary heat exchanger 19 through the connection pipe.
また、外気温度が低い場合(例えば0度)の冷房運転時は、利用側冷媒サイクルの運転とともに必要に応じて三方流量弁34a、34bの開度を調整し、蒸発式補助熱交換器30への冷媒流通を制御させる。
同時に第1、第2、第3ポンプ62,65,74を運転し、供給手段105、並びに循環手段106を駆動させ、散水器32を介して蒸発式補助熱交換器30へ電解水を循環散布して電解水の蒸発潜熱で冷却し、液化した冷媒を冷媒搬送装置20により利用側熱交換器23へ流通し冷房するサイクルを形成する。
Further, during cooling operation when the outside air temperature is low (for example, 0 degrees), the opening degree of the three-way flow valves 34a and 34b is adjusted as necessary along with the operation of the use side refrigerant cycle, and the evaporative auxiliary heat exchanger 30 is supplied. To control the refrigerant flow.
At the same time, the first, second, and third pumps 62, 65, and 74 are operated to drive the supply unit 105 and the circulation unit 106, and circulate and spray electrolytic water to the evaporative auxiliary heat exchanger 30 through the sprinkler 32. Then, cooling is performed with the latent heat of evaporation of the electrolyzed water, and a cycle is formed in which the liquefied refrigerant is circulated to the use side heat exchanger 23 by the refrigerant transfer device 20 and cooled.
この時、冷房能力が不足する場合には、熱源側冷媒サイクルを適切な能力で運転し、三方流量弁34aで調整された冷媒を第2補助熱交換器19で冷却し、三方流量弁34bで合流して冷媒搬送装置20へ送り、冷房する。 At this time, if the cooling capacity is insufficient, the heat source side refrigerant cycle is operated with an appropriate capacity, the refrigerant adjusted by the three-way flow valve 34a is cooled by the second auxiliary heat exchanger 19, and the three-way flow valve 34b is used. Merge and send to the refrigerant transport device 20 to cool.
暖房運転時には、図中破線矢印の冷媒サイクルとなり、熱源側冷媒サイクルでは、圧縮機11からの高温高圧冷媒は、四方弁12から第1補助熱交換器18に送られ、放熱して凝縮液化し、逆止弁17から暖房用減圧装置15で減圧し、熱源側熱交換器13で吸熱蒸発し、四方弁12を通って圧縮機11へ循環する。この時、利用側冷媒サイクルの第2補助熱交換器19と第1補助熱交換器18が熱交換し、利用側冷媒サイクル内の液冷媒が加熱されてガス化し、利用側熱交換器23へ送られ、暖房して放熱液化し、冷媒搬送装置20へ送られ第2補助熱交換器19へ循環する。
以上は、冷暖房装置の一例を示すものであり、これに限定されず、冷暖房装置の構成は、どのようなものであってもよい。
During the heating operation, the refrigerant cycle is indicated by the broken-line arrows in the figure. In the refrigerant cycle on the heat source side, the high-temperature and high-pressure refrigerant from the compressor 11 is sent from the four-way valve 12 to the first auxiliary heat exchanger 18 and dissipates heat to condense and liquefy. Then, the pressure is reduced by the heating pressure reducing device 15 from the check valve 17, the heat absorption is performed by the heat source side heat exchanger 13, and the heat is circulated to the compressor 11 through the four-way valve 12. At this time, the second auxiliary heat exchanger 19 and the first auxiliary heat exchanger 18 of the use side refrigerant cycle exchange heat, and the liquid refrigerant in the use side refrigerant cycle is heated and gasified, and then to the use side heat exchanger 23. It is sent, heated to be liquefied, and sent to the refrigerant transfer device 20 to circulate to the second auxiliary heat exchanger 19.
The above is one example of the air conditioning apparatus, and is not limited to this, and the configuration of the air conditioning apparatus may be any.
本実施形態では、電解水を供給する機構によって、気液接触塔の蒸発式補助熱交換器30へ電解水を循環散布させ、そこに室内戻り空気を循環させ、電解水で除菌した空気を室内に戻すため、例えば幼稚園や小・中・高等学校や、介護保険施設や、病院等、アリーナやドーム等で呼称される多数の人が集まる大空間であっても、除菌された空気を、大空間の遠くに飛ばすことが可能になり、大空間での空気除菌が効率よく達成される。 In this embodiment, the electrolyzed water is circulated and sprayed to the evaporative auxiliary heat exchanger 30 of the gas-liquid contact tower by the mechanism for supplying the electrolyzed water, indoor return air is circulated therein, and the air sterilized with the electrolyzed water is removed. In order to return to the room, sterilized air can be removed even in a large space where a large number of people called arenas or domes gather, such as kindergartens, elementary, junior and senior high schools, nursing care insurance facilities, hospitals, etc. It is possible to fly far away in a large space, and air sterilization in the large space is efficiently achieved.
以上、一実施形態に基づいて本発明を説明したが、本発明は、これに限定されるものではない。例えば、活性酸素種としてオゾン(O3)や過酸化水素(H2O2)を発生させる
構成としても良い。この場合、電極として白金タンタル電極を用いると、イオン種が希薄な水から、電気分解により高効率に安定して活性酸素種を生成できる。
このとき、アノード電極では、
2H2O→4H++O2+4e-
の反応と同時に、
3H2O→O3+6H++6e-
2H2O→O3+4H++4e-
の反応が起こりオゾン(O3)が生成される。またカソード電極では、
4H++4e-+(4OH-)→2H2+(4OH-)
O2 -+e-+2H+→H2O2
のように、電極反応によりO2 -が生成したO2 -と溶液中のH+とが結合して、過酸化水素
(H2O2)が生成される。
As mentioned above, although this invention was demonstrated based on one Embodiment, this invention is not limited to this. For example, ozone (O 3 ) or hydrogen peroxide (H 2 O 2 ) may be generated as the active oxygen species. In this case, when a platinum tantalum electrode is used as an electrode, active oxygen species can be stably generated with high efficiency by electrolysis from water having a small ion species.
At this time, in the anode electrode,
2H 2 O → 4H + + O 2 + 4e −
At the same time as
3H 2 O → O 3 + 6H + + 6e −
2H 2 O → O 3 + 4H + + 4e −
This reaction occurs and ozone (O 3 ) is generated. In the cathode electrode,
4H + + 4e − + (4OH − ) → 2H 2 + (4OH − )
O 2 − + e − + 2H + → H 2 O 2
As in, O 2 by the electrode reaction - O which is produced 2 - and solution H + and are bonded in the hydrogen peroxide (H 2 O 2) is generated.
この構成では、電極に通電することにより、殺菌力の大きいオゾン(O3)や過酸化水
素(H2O2)が発生し、これらオゾン(O3)や過酸化水素(H2O2)を含んだ電解水を
作ることができる。この電解水中におけるオゾンもしくは過酸化水素の濃度を、対象ウィルス等を不活化させる濃度に調整し、この濃度の電解水が供給された部位に空気を通過させることにより、空気中に浮遊する対象ウィルス等を不活化することができる。また、臭気も気液接触塔を通過する際に、オゾンまたは過酸化水素と反応し、イオン化して溶解することで空気中から除去され、脱臭される。
In this construction, by supplying current to the electrodes, a large ozone sterilizing power (O 3) and hydrogen peroxide (H 2 O 2) is generated, these ozone (O 3) and hydrogen peroxide (H 2 O 2) Electrolyzed water containing can be made. The concentration of ozone or hydrogen peroxide in the electrolyzed water is adjusted to a concentration that inactivates the target virus, and the target virus is suspended in the air by passing the air through the site to which the electrolyzed water of this concentration is supplied. Etc. can be inactivated. Further, when the odor passes through the gas-liquid contact tower, it reacts with ozone or hydrogen peroxide, and is ionized and dissolved to be removed from the air and deodorized.
水道水を電気分解することにより、電極上(カソード)にスケールが堆積した場合、電気伝導性が低下し、継続的な電気分解が困難となる。
この場合、電極の極性を反転(電極のプラスとマイナスを切り替える)させることが効果的である。カソード電極をアノード電極として電気分解することで、カソード電極上に堆積したスケールを取り除くことができる。この極性反転制御では、例えばタイマを利用して定期的に反転させてもよいし、運転起動の度に反転させる等、不定期的に反転させてもよい。また、電解抵抗の上昇(電解電流の低下、あるいは電解電圧の上昇)を検出し、この結果に基づいて、極性を反転させてもよい。
When scale is deposited on the electrode (cathode) by electrolyzing tap water, the electrical conductivity is lowered, and continuous electrolysis becomes difficult.
In this case, it is effective to reverse the polarity of the electrode (switch between positive and negative of the electrode). By electrolysis using the cathode electrode as the anode electrode, the scale deposited on the cathode electrode can be removed. In this polarity reversal control, for example, it may be reversed periodically using a timer, or may be reversed irregularly, such as reversed every time the operation is started. Further, an increase in electrolytic resistance (decrease in electrolysis current or increase in electrolysis voltage) may be detected, and the polarity may be reversed based on this result.
上記実施形態では、水道水貯留タンク67による給水方式としたが、この水道水貯留タンク67の代わりに、例えば水道管を接続して、市水を直接導く水配管給水方式としてもよいことは云うまでもない。
また、上記構成では、クーリングタワー(気液接触塔)に限定されるものではなく、例えば、不凍液を混入したブラインを利用してなる、いわゆるヒーティングタワー等にも適用が可能であることは云うまでもない。
In the above embodiment, the water supply system using the tap water storage tank 67 is used. However, instead of the tap water storage tank 67, for example, a water pipe supply system that directly connects city water by connecting a water pipe may be used. Not too long.
Further, the above configuration is not limited to a cooling tower (gas-liquid contact tower), and can be applied to a so-called heating tower using a brine mixed with antifreeze liquid, for example. Nor.
30 蒸発式補助熱交換器
32 散水器
44 吸気ダクト
46 送風機
47 排気ダクト(略直角に折り曲げた風路)
48 ミストトラップ
61 飽和食塩水タンク
62 第1ポンプ
63 食塩水タンク
64 電解槽
65 第2ポンプ
66 濃度調整槽
71 電極
100 気液接触塔本体(本体)
101 吸気部
102 排気部(導入手段)
105 供給手段
106 循環手段
301、302、303… 気液接触促進部材(電解水接触部)
30 Evaporative Auxiliary Heat Exchanger 32 Sprinkler 44 Intake Duct 46 Blower 47 Exhaust Duct (Air Path Bent at Right Angle)
48 Mist Trap 61 Saturated Saline Tank 62 First Pump 63 Saline Tank 64 Electrolyzer 65 Second Pump 66 Concentration Adjusting Tank 71 Electrode 100 Gas-Liquid Contact Tower Body (Main Body)
101 Intake part 102 Exhaust part (introducing means)
105 Supply means 106 Circulation means 301, 302, 303 ... Gas-liquid contact promoting member (electrolyzed water contact portion)
Claims (6)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2008273776A JP2009039560A (en) | 2008-10-24 | 2008-10-24 | Air disinfection apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2008273776A JP2009039560A (en) | 2008-10-24 | 2008-10-24 | Air disinfection apparatus |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2005349658A Division JP4878826B2 (en) | 2005-12-02 | 2005-12-02 | Air sanitizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2009039560A true JP2009039560A (en) | 2009-02-26 |
Family
ID=40440922
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2008273776A Pending JP2009039560A (en) | 2008-10-24 | 2008-10-24 | Air disinfection apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2009039560A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011045564A (en) * | 2009-08-27 | 2011-03-10 | Sanyo Electric Co Ltd | Air disinfecting apparatus |
| JP2011050702A (en) * | 2009-09-04 | 2011-03-17 | Es Technology Kk | Method and device for sterilization and deodorization |
| JP2012065783A (en) * | 2010-09-22 | 2012-04-05 | Nobumasa Okuda | Air cleaning system |
| JP2018169074A (en) * | 2017-03-29 | 2018-11-01 | 村上 輝明 | Structure of a device that enables cooling in a windless state using gas as a refrigerant |
| JP2019051095A (en) * | 2017-09-15 | 2019-04-04 | 集塵装置株式会社 | Gas deodorization device |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06292713A (en) * | 1993-04-09 | 1994-10-21 | T R P:Kk | Cleaning method of air and device therefor |
| JPH0970516A (en) * | 1995-09-05 | 1997-03-18 | Omron Corp | air purifier |
-
2008
- 2008-10-24 JP JP2008273776A patent/JP2009039560A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06292713A (en) * | 1993-04-09 | 1994-10-21 | T R P:Kk | Cleaning method of air and device therefor |
| JPH0970516A (en) * | 1995-09-05 | 1997-03-18 | Omron Corp | air purifier |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011045564A (en) * | 2009-08-27 | 2011-03-10 | Sanyo Electric Co Ltd | Air disinfecting apparatus |
| JP2011050702A (en) * | 2009-09-04 | 2011-03-17 | Es Technology Kk | Method and device for sterilization and deodorization |
| JP2012065783A (en) * | 2010-09-22 | 2012-04-05 | Nobumasa Okuda | Air cleaning system |
| JP2018169074A (en) * | 2017-03-29 | 2018-11-01 | 村上 輝明 | Structure of a device that enables cooling in a windless state using gas as a refrigerant |
| JP2019051095A (en) * | 2017-09-15 | 2019-04-04 | 集塵装置株式会社 | Gas deodorization device |
| JP7016650B2 (en) | 2017-09-15 | 2022-02-07 | 集塵装置株式会社 | Gas deodorizer |
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