JP2005172260A - Air conditioner - Google Patents

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JP2005172260A
JP2005172260A JP2003408624A JP2003408624A JP2005172260A JP 2005172260 A JP2005172260 A JP 2005172260A JP 2003408624 A JP2003408624 A JP 2003408624A JP 2003408624 A JP2003408624 A JP 2003408624A JP 2005172260 A JP2005172260 A JP 2005172260A
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heat exchanger
bacteria
metal plate
air conditioner
plate
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Daisuke Tabata
大輔 田畑
Shiho Furuya
志保 古谷
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Panasonic Holdings Corp
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Matsushita Electric Industrial Co Ltd
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/54Free-cooling systems

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  • Other Air-Conditioning Systems (AREA)
  • Air Humidification (AREA)
  • Drying Of Gases (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To inhibit discomfort such as generation of odor due to deposited bacteria in a staying part of dew condensate formed by condensing moisture in high-temperature high-humidity air released from a hygroscopic body or rot of staying condensate. <P>SOLUTION: The staying part 6 is provided with a metallic plate 7 connected to a heat exchanger 5 in the conducting state, thereby causing a potential difference due to the internal electromotive force because the metallic plate 7 has lower voltage than the heat exchanger 5. In this condition, bacteria mixed in the dew condensate causes electrophoresis to be sequentially collected toward the low-potential metallic plate 7 due to a difference in ionization tendency between the heat exchanger 5 and the metallic plate 7 because the bacterium itself is charged with negative ions to some degree, whereby the bacteria can be restrained from free activity. After that, the bacteria, the metabolism function of which is inactivated, become weak, and the bacteria existing in the staying part 6 die out. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、水分の吸着・脱離能力を有する吸着体より放出される高温高湿空気中の水分を結露させた結露水を貯留する貯留部に空気中の菌が堆積あるいは滞留した結露水が腐敗して運転時に臭気発生の問題となることを防止する機能を備えた空気調和機に関するものである。   In the present invention, condensed water in which bacteria in the air accumulates or stays in a storage part that stores condensed water that is condensed from moisture in high-temperature and high-humidity air released from an adsorbent having moisture adsorption / desorption capability. The present invention relates to an air conditioner having a function of preventing rot and causing a problem of odor generation during operation.

従来、この種の調湿用吸湿体を備えた空気調和機は、送風手段により室内または室外から取り入れられた空気中より水分を吸着した吸湿体をヒータにより加熱し、吸着体に吸着されている水分の脱離を行うことにより、結露水を室内へと搬送している(例えば、特許文献1〜2参照)。   Conventionally, an air conditioner equipped with this type of humidity control absorbent is heated by a heater, which absorbs moisture from the air taken in from the room or outdoors by a blower, and is adsorbed by the adsorber. Condensed water is conveyed indoors by desorbing moisture (see, for example, Patent Documents 1 and 2).

図は、特許文献1に記載された従来の調湿用吸湿体を備えた空気調和機を示すものである。
特開平8−121826号公報 特開2002−317970号公報
FIG. 1 shows an air conditioner provided with a conventional moisture absorbent for humidity adjustment described in Patent Document 1.
JP-A-8-121826 JP 2002-317970 A

しかしながら、前記従来の構成では、貯留部に滴下した結露水が菌の堆積あるいは滞留により腐敗し、その結果室内空間への異臭発生の原因となるという課題を有していた。   However, the conventional configuration has a problem that the condensed water dripped in the storage part is spoiled due to accumulation or retention of bacteria, resulting in generation of a strange odor in the indoor space.

本発明は、前記従来の課題を解決するもので、吸湿体より放出される高温高湿空気中の水分を結露させた結露水を貯留させる雑菌が繁殖し易い貯留部に長期的な寿命を保証できる抗菌機能を設けることで、貯留部に堆積した菌あるいは滞留した結露水の腐敗による臭気発生などの不快感を抑止できる空気調和機を提供することを目的とする。   The present invention solves the above-mentioned conventional problems, and guarantees a long-term life in a storage part in which miscellaneous germs that store condensed water condensed from moisture in high-temperature and high-humidity air released from a hygroscopic body are easy to propagate. An object of the present invention is to provide an air conditioner that can suppress discomfort such as generation of odor due to decay of germs accumulated in a reservoir or accumulated condensed water by providing an antibacterial function that can be performed.

前記従来の課題を解決するために、本発明の空気調和機は、吸着体より放出される高温高湿空気中の水分を結露させた結露水を貯留させる雑菌が繁殖し易い貯留部に長期的な寿命を保証できる抗菌機能を設けたものである。   In order to solve the above-mentioned conventional problems, the air conditioner of the present invention is provided with a long-term storage in a storage part in which miscellaneous bacteria that store condensed water obtained by condensation of moisture in high-temperature and high-humidity air released from an adsorbent are easily propagated. Antibacterial function that can guarantee a long life.

これによって、空気中に浮遊している菌は熱交換器に結露水と一緒に付着して貯留部に滴下する。結露水中に混入した菌は菌自体がある程度マイナスの電荷を帯びているため、熱交換器と金属板のイオン化傾向の差により、菌は電気泳動して低電位な金属板側へと次々と集められて菌の自由な活動を抑制すると考えられる。その後新陳代謝機能を不活化された菌は弱り、やがて死んでしまうことになるので、貯留部に存在する菌を死滅化できる。   As a result, the germs floating in the air adhere to the heat exchanger together with the dew condensation water and are dripped into the reservoir. Bacteria mixed in condensed water have a negative charge to some extent, so the bacteria migrate to the low potential metal plate side by side due to the difference in ionization tendency between the heat exchanger and the metal plate. It is thought that it suppresses the free activity of bacteria. Then, the bacteria whose metabolic function is inactivated weaken and eventually die, so that the bacteria present in the reservoir can be killed.

本発明の空気調和機は、加湿用結露水中の菌を長期的に死滅化することができる。   The air conditioner of the present invention can kill bacteria in the condensed water for humidification over a long period of time.

第1の発明は、雑菌が繁殖し易い結露水の貯留部に長期的な寿命を保証できる抗菌機能を設けることにより、空気中に浮遊している菌は熱交換器に結露水と一緒に付着して貯留部に滴下し、結露水中に混入した菌は菌自体がある程度マイナスの電荷を帯びているため、熱交換器と金属板のイオン化傾向の差により、菌は電気泳動して低電位な金属板側へと
次々と集められて菌の自由な活動を抑制し、その後新陳代謝機能を不活化された菌は弱り、やがて死んでしまうことになるので、貯留部に存在する菌を死滅化することができる。
According to the first aspect of the present invention, an antibacterial function capable of guaranteeing a long-term life is provided in a dew condensation water storage portion in which miscellaneous bacteria easily propagate, so that bacteria floating in the air adhere to the heat exchanger together with the dew condensation water. Since the bacteria that are dripped into the reservoir and mixed in the dew condensation water have a negative charge to some extent, the bacteria are electrophoresed and have a low potential due to the difference in ionization tendency between the heat exchanger and the metal plate. Bacteria that are gathered one after another to the metal plate side and suppress free activity of bacteria, and then inactivated metabolic function will weaken and eventually die, so kill the bacteria present in the reservoir be able to.

第2の発明は、特に、第1の発明の金属板と熱交換器の結線する部分を常に結露水と導通状態とならない場所に設けることにより、結線端子部の接点腐食による導通不良に至るという課題を解決でき、長期的な信頼性を保証することができる。   According to the second aspect of the invention, in particular, by providing the portion where the metal plate of the first aspect of the invention and the heat exchanger are connected in a place where the dew condensation water is not always in a conductive state, it leads to poor conduction due to contact corrosion of the connection terminal portion. The problem can be solved and long-term reliability can be guaranteed.

第3の発明は、特に、第1または第2の発明の金属板とアルミニウムフィンとの間の内部起電力による電位差を0.3〜1.0Vとすることにより、菌は電気泳動して低電位な金属板側へと次々と集められて菌の自由な活動を抑制し、充分な死滅化性能が得られるとともに、その起電力をある一定のレベルに抑えることにより、結露水の電気伝導度が高い場合にも結露水中を電流が流れすぎて低電位側の金属板が腐食に至るということがなくなり、十分な耐久性を保証することができる。   In the third invention, in particular, the potential difference due to the internal electromotive force between the metal plate of the first or second invention and the aluminum fin is set to 0.3 to 1.0 V, so that the bacteria are electrophoresed and reduced. It is collected one after another to the potential metal plate side to suppress the free activity of bacteria, and sufficient killing performance is obtained, and the electromotive force of condensed water is suppressed by suppressing the electromotive force to a certain level. Even when the value is high, the current does not flow too much in the condensed water and the metal plate on the low potential side is not corroded, and sufficient durability can be ensured.

第4の発明は、特に、第1〜3のいずれか1つの発明の金属板と熱交換器との間隔に部分的あるいは全体に絶縁物を介在させることにより、短絡を防止することができ、貯留部に結露水が存在する時にはたえず金属板と熱交換器との間に内部起電力による電位差を確保することができる。   In particular, the fourth invention can prevent a short circuit by interposing an insulator partially or entirely in the interval between the metal plate of any one of the first to third inventions and the heat exchanger, When condensed water is present in the reservoir, a potential difference due to internal electromotive force can be ensured between the metal plate and the heat exchanger.

第5の発明は、特に、第4の発明の金属板と熱交換器先端との間隔を5mm以下とすることにより、結露水に与える電位差の最大値である1.0Vにおいても十分な電解強度が維持でき、菌は電気泳動して低電位な金属板側へと次々と集められて菌の自由な活動を抑制し、死滅化効果を発揮することができる。   In the fifth invention, in particular, by setting the distance between the metal plate of the fourth invention and the tip of the heat exchanger to 5 mm or less, sufficient electrolytic strength can be obtained even at 1.0 V which is the maximum potential difference given to the dew condensation water. The bacteria can be electrophoresed and collected one after another toward the low-potential metal plate to suppress the free activity of the bacteria and exert a killing effect.

第6の発明は、特に、第4または第5の発明の絶縁物を樹脂の不織布あるいはメッシュとすることにより、狭い間隔に対しても絶縁状態を確保できるとともに、結露水を絶縁物自体が長時間にわたって保持でき、少ない結露水量の状態でも内部起電力による電位差を持続し、菌は電気泳動して低電位な金属板側へと次々と集められて菌の自由な活動を抑制し、死滅化効果を発揮することができる。   In the sixth invention, in particular, the insulating material of the fourth or fifth invention is made of a resin nonwoven fabric or mesh, so that an insulating state can be secured even for a narrow interval, and the condensed water itself is long. It can be maintained for a long time, and the potential difference due to the internal electromotive force is maintained even when the amount of condensed water is small, and the bacteria are electrophoresed and gathered one after another to the low potential metal plate side to suppress the free activity of the bacteria and die. The effect can be demonstrated.

第7の発明は、特に、第1〜6のいずれか1つの発明の金属板を亜鉛板、亜鉛メッキ鋼鈑、または亜鉛合金とすることにより、汎用性があり低コスト化を図ることができる。   In the seventh invention, in particular, the metal plate according to any one of the first to sixth inventions is made of a zinc plate, a galvanized steel plate, or a zinc alloy, so that it is versatile and can be reduced in cost. .

以下、本発明の実施の形態について、図面を参照しながら説明する。なお、この実施の形態によって本発明が限定されるものではない。   Hereinafter, embodiments of the present invention will be described with reference to the drawings. Note that the present invention is not limited to the embodiments.

(実施の形態1)
図1は、本発明の第1の実施の形態における空気調和機の室外機加湿装置の断面構成図を示すものである。
(Embodiment 1)
FIG. 1 shows a cross-sectional configuration diagram of an outdoor unit humidifier for an air conditioner according to a first embodiment of the present invention.

図1において、室外機加湿装置は、吸気口と吹出口および除湿水排水口を設けた本体1と、この本体1内に配置される送風機2と、吸湿体3と、その吸湿体3の風上側に設けたヒータ4と、本体1出口に設けられた熱交換器5と、熱交換器5下部に設けた貯留部6と、その貯留部6には熱交換器5と結線された金属板7と、貯留部6に溜まった結露水を室内機へ搬送するポンプ8とで構成されている。   In FIG. 1, the outdoor unit humidifier includes a main body 1 provided with an intake port, a blow-out port, and a dehumidified water drain port, a blower 2 disposed in the main body 1, a moisture absorber 3, and a wind of the moisture absorber 3. The heater 4 provided on the upper side, the heat exchanger 5 provided at the outlet of the main body 1, the storage unit 6 provided at the lower part of the heat exchanger 5, and the metal plate connected to the heat exchanger 5 in the storage unit 6 7 and a pump 8 for conveying the condensed water accumulated in the storage unit 6 to the indoor unit.

以上のように構成された空気調和機の室外機加湿装置について、以下その動作、作用を説明する。   About the outdoor unit humidification apparatus of the air conditioner comprised as mentioned above, the operation | movement and an effect | action are demonstrated below.

図1において、室外機加湿装置は水分吸着時にはヒータ4の通電は停止されており、吸
気口を通じて吸い込まれた空気に含まれる水分は吸湿体3において吸着される。脱離時には、ヒータ4へ通電されており、吸気口を通じて吸い込まれた空気は吸湿体3の風上側に設けられたヒータ4によって加熱され、その加熱空気が吸湿体3を通過することで吸湿体3に吸着された水分が脱離される。その脱離によって生じた高温高湿空気は、金属で構成された熱交換器5を通過することで熱交換器5表面に結露する。結露水はやがて熱交換器5下部に設けられた貯留部6へと滞留される。貯留部6に配置され、熱交換器5と導通状態に結線された金属板7との間に金属板7の方が熱交換器5よりも低電圧である内部起電力による電位差が生じる。このことにより、空気中に浮遊している菌は熱交換器5に結露水と一緒に付着して貯留部6に滴下し、結露水中に混入した菌は菌自体がある程度マイナスの電荷を帯びているため、熱交換器5と金属板7のイオン化傾向の差により、菌は電気泳動して低電位な金属板7側へと次々と集められて菌の自由な活動を抑制し、その後新陳代謝機能を不活化された菌は弱り、やがて死んでしまうことになるので、貯留部6に存在する菌を死滅化することができる。すなわち、雑菌が繁殖し易い結露水の貯留部6に長期的な寿命を保証できる抗菌機能を付加することができる。
In FIG. 1, in the outdoor unit humidifier, energization of the heater 4 is stopped at the time of moisture adsorption, and moisture contained in the air sucked through the intake port is adsorbed by the moisture absorber 3. At the time of detachment, the heater 4 is energized, and the air sucked through the intake port is heated by the heater 4 provided on the windward side of the hygroscopic body 3, and the heated air passes through the hygroscopic body 3 to thereby absorb the hygroscopic body. The water adsorbed on 3 is desorbed. The high-temperature and high-humidity air generated by the desorption is condensed on the surface of the heat exchanger 5 by passing through the heat exchanger 5 made of metal. Condensed water is eventually retained in the reservoir 6 provided at the lower part of the heat exchanger 5. A potential difference is generated between the heat exchanger 5 and the metal plate 7 connected to the conductive state, which is disposed in the storage unit 6, due to an internal electromotive force in which the metal plate 7 has a lower voltage than the heat exchanger 5. As a result, the germs floating in the air adhere to the heat exchanger 5 together with the dew condensation water and are dripped onto the storage unit 6, and the germs mixed in the dew condensation water have a negative charge to some extent. Therefore, due to the difference in ionization tendency between the heat exchanger 5 and the metal plate 7, the bacteria are electrophoresed and gathered one after another to the low potential metal plate 7 side to suppress the free activity of the bacteria, and then the metabolic function Since the inactivated bacteria are weak and will eventually die, the bacteria present in the reservoir 6 can be killed. That is, an antibacterial function capable of guaranteeing a long-term life can be added to the dew condensation water storage unit 6 in which germs easily propagate.

(実施の形態2)
図2は本実施の形態を説明するために空気調和機の室外加湿装置の熱交換器5と亜鉛板9との結線構成を示す正面構成図である。図2において亜鉛板9は熱交換器5から滴下する結露水の通り道が全域にわたってカバーできるように貯留部6に設けられている。したがって全長は熱交換器5よりも長く、幅はアルミニウムフィンの奥行きよりも長くしている。また亜鉛板9の向かって右側には2段の折り曲げ加工をして結線をするための端子取りだし部分を設け、ドレン水中に漬からないように設計した。また亜鉛板9と熱交換器5のアルミニウムフィンとが短絡しないように発泡EPDM10もほぼ全域に設けられている。熱交換器5と亜鉛板9との結線は、塩化ビニル樹脂で絶縁保護カバーされた銅線11を使用して、一方は熱交換器5の端板12にビス止めして固定し、もう一方は亜鉛板9を加湿装置本体とともにビス止めして固定されている。これによって貯留部6に結露水が溜まったときには熱交換器5のアルミニウムフィンと亜鉛板9との間には内部起電力が約0.4V生じるような構成となる。その結果、空気中に漂っていた雑菌はまず熱交換器5によってトラップされ、その後結露水とともに貯留部6に移動するが、その時マイナスの電荷を帯びた菌は亜鉛板9に次々と引きつけられて、身動きがとれない状態となる。その結果自由を失った菌は新陳代謝も抑制され、徐々に弱っていき、やがては死滅してしまう。
(Embodiment 2)
FIG. 2 is a front configuration diagram showing a connection configuration between the heat exchanger 5 and the zinc plate 9 of the outdoor humidifier of the air conditioner in order to explain the present embodiment. In FIG. 2, the zinc plate 9 is provided in the storage portion 6 so that the path of the condensed water dripping from the heat exchanger 5 can be covered over the entire area. Therefore, the total length is longer than that of the heat exchanger 5, and the width is longer than the depth of the aluminum fins. In addition, the right side of the zinc plate 9 is provided with a terminal lead-out portion for two-stage bending to make a connection so that it is not immersed in the drain water. Further, the foamed EPDM 10 is also provided in almost the entire region so that the zinc plate 9 and the aluminum fins of the heat exchanger 5 are not short-circuited. For the connection between the heat exchanger 5 and the zinc plate 9, a copper wire 11 covered with an insulation protection cover with vinyl chloride resin is used, and one is screwed to the end plate 12 of the heat exchanger 5 and fixed. Is fixed by screwing the zinc plate 9 together with the humidifier body. As a result, when condensed water accumulates in the reservoir 6, an internal electromotive force of about 0.4 V is generated between the aluminum fins of the heat exchanger 5 and the zinc plate 9. As a result, the germs floating in the air are first trapped by the heat exchanger 5 and then moved to the reservoir 6 together with the dew condensation water. At that time, the negatively charged germs are attracted to the zinc plate 9 one after another. , You can't move. As a result, bacteria that have lost their freedom are also suppressed in metabolism, gradually weaken, and eventually die.

このような集菌、死滅化機能を有する空気調和機の実証的な評価として下記のような試験を行った。   As an empirical evaluation of such an air conditioner having a function of collecting and killing bacteria, the following tests were conducted.

実証評価試験1としては、NB培地組成(ペプトン 10g、塩化ナトリウム 5g、肉エキス 3g、純水 1L)を1000倍に希釈し、グラム陰性の大腸菌を濃度30個/L程度で含んだ調製水を用意して熱交換器5の10cm幅に対して均一に1ml/minの速度で調製水をマイクロポンプで送液し、排出された水を時間経過とともに0.2mlずつ採取して、平板混釈法に準じて寒天培地にて24時間培養して水中の菌数を調べて亜鉛板9による集菌の効果を評価した。その結果、貯留部6に従来方式のなにもしていないものと比較して、大腸菌が明らかに集菌できていることを確認できた。   As the demonstration evaluation test 1, NB medium composition (10 g of peptone, 5 g of sodium chloride, 3 g of meat extract, 1 L of pure water) was diluted 1000 times and prepared water containing gram-negative Escherichia coli at a concentration of about 30 / L. Prepared water is uniformly pumped at a rate of 1 ml / min for the 10 cm width of the heat exchanger 5, and the discharged water is sampled by 0.2 ml over time, and mixed with a plate. According to the method, the cells were cultured on an agar medium for 24 hours, and the number of bacteria in water was examined to evaluate the effect of collecting bacteria by the zinc plate 9. As a result, it was confirmed that E. coli was clearly collected in comparison with the storage unit 6 that did not do anything in the conventional system.

実証評価試験2として、貯留部6からポンプ8への経路を塞いでNB培地組成(ペプトン 10g、塩化ナトリウム 5g、肉エキス 3g、純水 1L)を1000倍に希釈し、グラム陰性の大腸菌を濃度30個/L程度で含んだ調製水200mlを貯留部6内に投入して12、24、48時間経過後の状態を確認した。投入した調製水を再度滅菌したビーカーに戻してその中から0.2mlの調製水をサンプリングして平板混釈法に準じて寒天培地にて24時間培養し、ブランクとの比較で集菌の効果を調べた。その結果、大腸菌が明らかに集菌できていることを確認できた。   As a demonstration evaluation test 2, the route from the reservoir 6 to the pump 8 is blocked, the NB medium composition (10 g of peptone, 5 g of sodium chloride, 3 g of meat extract, 1 L of pure water) is diluted 1000 times, and the concentration of gram-negative Escherichia coli is increased. 200 ml of prepared water contained at about 30 / L was introduced into the reservoir 6 and the state after 12, 24 and 48 hours had been confirmed. Put the prepared water again into a sterilized beaker, sample 0.2 ml of the prepared water, and culture it in an agar medium for 24 hours according to the plate pour method. I investigated. As a result, it was confirmed that E. coli was clearly collected.

本実施の形態では、発泡EPDMを使用したが、この限りではない。絶縁性に優れたものであれば熱交換器5のアルミニウムフィンと金属板7との間のスペーサーとして使用できる。また弾性を有するものであればさらに都合がよく、その他に発泡PE、発泡PS、発泡PP、発泡PVA、ウレタンフォームなどが使用できる。   In the present embodiment, foamed EPDM is used, but the present invention is not limited to this. Any one having excellent insulation can be used as a spacer between the aluminum fins of the heat exchanger 5 and the metal plate 7. Further, it is more convenient if it has elasticity, and foamed PE, foamed PS, foamed PP, foamed PVA, urethane foam and the like can be used in addition.

(実施の形態3)
図3は本実施の形態を説明するために空気調和機の室外加湿装置の熱交換器5と亜鉛板9との結線構成を示す正面構成図である。室外加湿装置の中で実施の形態2と説明が重複する部分は省略する。図3において、本実施の形態でも亜鉛板9は熱交換器5から滴下する結露水の全域にわたってカバーできるように設けられ、全長は熱交換器5よりも長く、幅はアルミニウムフィンの奥行きよりも長くしている。ここでは亜鉛板9からの端子取り出し方法が実施の形態2と異なっている。すなわち亜鉛板9は平板状態のままとして貯留部6に配置し、結露水中に漬かる部分は銅線13に亜鉛メッキを施して樹脂ネジによってビス止めを行った。この結果、熱交換器5のアルミニウムフィンと亜鉛板9との間には内部起電力が約0.4V生じるようになり、空気中に漂っていた雑菌はまず熱交換器5によってトラップされ、その後結露水とともに貯留部6へ移動し、マイナスの電荷を帯びた菌は亜鉛板9に集菌され、やがては死滅する。また亜鉛板9と結線する銅線も結露水に漬かる部分は亜鉛メッキ処理を施すことによって水中で異種金属の接合による局部腐食を防止することができる。
(Embodiment 3)
FIG. 3 is a front configuration diagram showing a connection configuration between the heat exchanger 5 and the zinc plate 9 of the outdoor humidifier of the air conditioner for explaining the present embodiment. Parts of the outdoor humidifier that overlap with the description of the second embodiment are omitted. In FIG. 3, the zinc plate 9 is also provided in this embodiment so as to cover the entire area of the condensed water dripping from the heat exchanger 5, the overall length is longer than the heat exchanger 5, and the width is greater than the depth of the aluminum fins. It is long. Here, the method of taking out terminals from the zinc plate 9 is different from that of the second embodiment. That is, the zinc plate 9 was placed in the storage portion 6 as it was in a flat state, and the portion immersed in the dewed water was galvanized on the copper wire 13 and screwed with a resin screw. As a result, an internal electromotive force of about 0.4 V is generated between the aluminum fins of the heat exchanger 5 and the zinc plate 9, and the germs floating in the air are first trapped by the heat exchanger 5, and thereafter The bacteria that move to the storage unit 6 together with the dew condensation water and are negatively charged are collected on the zinc plate 9 and eventually die. In addition, a portion where the copper wire connected to the zinc plate 9 is also immersed in the dewed water can be subjected to galvanizing treatment to prevent local corrosion due to joining of different metals in water.

(実施の形態4)
図4は本実施の形態を示す空気調和機の室外加湿装置の断面構成図である。構成の中で実施の形態2と説明が重複する部分は省略する。図4において、本実施の形態では亜鉛板9と熱交換器5のアルミニウムフィンとが短絡しないように厚さ1mmのPP不織布13をほぼ全域に設けている。PP不織布は水分を保持する能力が優れているため亜鉛板9と熱交換器5との電位差を長時間にわたって維持できるので、貯留部6に結露水が存在している間は十分な集菌、死滅化機能を持続できる。具体的には実施の形態2の実証評価試験1で比較して、実施の形態2の場合には熱交換器5に滴下させる水量が減ってくると、ある時点から集菌機能が急激に減衰するが、本実施の形態では滴下水量がおよび熱交換器5が保持している水量がかなり少なくなっても、PP不織布の保水能力によって集菌効果を持続できた。
(Embodiment 4)
FIG. 4 is a cross-sectional configuration diagram of the outdoor humidifier of the air conditioner showing the present embodiment. Portions of the configuration that overlap with those of the second embodiment are omitted. In FIG. 4, in this embodiment, a PP nonwoven fabric 13 having a thickness of 1 mm is provided in almost the entire region so that the zinc plate 9 and the aluminum fins of the heat exchanger 5 are not short-circuited. Since the PP nonwoven fabric has an excellent ability to retain moisture, the potential difference between the zinc plate 9 and the heat exchanger 5 can be maintained over a long period of time, so that sufficient collection of bacteria is possible while dew condensation water is present in the reservoir 6, Sustained extinction function. Specifically, as compared with the demonstration evaluation test 1 of the second embodiment, in the case of the second embodiment, when the amount of water dripped in the heat exchanger 5 decreases, the bacteria collection function attenuates rapidly from a certain point in time. However, in this embodiment, even if the amount of dripped water and the amount of water held by the heat exchanger 5 are considerably reduced, the bacteria collection effect can be maintained by the water retention ability of the PP nonwoven fabric.

本実施の形態では、PPの不織布を使用したが、この限りではない。絶縁性に優れた樹脂の不織布またはメッシュであれば同様な効果が期待できる。PET、PEN、PE、ナイロン等の樹脂も使用できる。不織布は毛細管現象によって、またはメッシュは表面張力によって水を十分保持できるので、長時間にわたって熱交換器5のアルミニウムフィンと金属板7とで内部起電力による電位差を確保でき、その間は亜鉛板側への集菌を持続できる。   In the present embodiment, a PP nonwoven fabric is used, but this is not restrictive. The same effect can be expected if the nonwoven fabric or mesh is a resin excellent in insulation. Resins such as PET, PEN, PE, and nylon can also be used. The nonwoven fabric can hold water sufficiently by capillary action or the mesh by surface tension, so that the potential difference due to the internal electromotive force can be secured between the aluminum fins of the heat exchanger 5 and the metal plate 7 for a long time. Can sustain the collection of bacteria.

(実施の形態5)
本実施の形態では貯留部と熱交換器の間に亜鉛鉄板を配置し、亜鉛鉄板の構造は実施の形態2と同様にした。この時亜鉛鉄板の切断端面はエポキシ系の樹脂によってコーティングして腐食への対策を行った。これによって熱交換器5のアルミニウムフィンと亜鉛鉄板との間には内部起電力が約0.4V生じるようになり、亜鉛鉄板でも十分な集菌、死滅化機能を発揮できた。
(Embodiment 5)
In the present embodiment, a zinc iron plate is disposed between the storage unit and the heat exchanger, and the structure of the zinc iron plate is the same as that of the second embodiment. At this time, the cut end face of the galvanized iron plate was coated with an epoxy resin to take measures against corrosion. As a result, an internal electromotive force of about 0.4 V is generated between the aluminum fins of the heat exchanger 5 and the galvanized iron plate, and the galvanized iron plate was able to exhibit sufficient bacteria collection and killing functions.

(実施の形態6)
本実施の形態では貯留部と熱交換器の間にマグネシウム合金(AZ91)板を配置し、マグネシウム合金板の構造は実施の形態2と同様にした。これによって熱交換器5のアル
ミニウムフィンとマグネシウム合金板との間には内部起電力が約0.8V生じるようになり、マグネシウム合金(AZ91)板とすることによって内部起電力による電位差が大きくすることができ集菌能力は向上し、充分な死滅化機能も発揮できた。
(Embodiment 6)
In the present embodiment, a magnesium alloy (AZ91) plate is disposed between the reservoir and the heat exchanger, and the structure of the magnesium alloy plate is the same as that of the second embodiment. As a result, an internal electromotive force of about 0.8 V is generated between the aluminum fins of the heat exchanger 5 and the magnesium alloy plate, and the potential difference due to the internal electromotive force is increased by using the magnesium alloy (AZ91) plate. The ability to collect bacteria was improved, and a sufficient killing function was achieved.

上記各実施の形態では絶縁物を金属板7の全体にわたって配置したが、絶縁物を部分的に配置することも可能である。   In each said embodiment, although the insulator was arrange | positioned over the whole metal plate 7, it is also possible to arrange | position an insulator partially.

亜鉛板または亜鉛鉄板を使用した実施例では電位差0.4Vを確保でき、マグネシウム合金(AZ91)板を使用したときには電位差0.8Vを確保できた。本発明で菌の電気泳動による集菌に必要な電位差は少なくとも0.3V以上であった。また、1.0Vを越えると熱交換器5からの結露水の電気伝導度にもよるが漏れ電流が無視できなくなり、金属板7自体の溶解が徐々に起こり始める場合もあるため、長期的な信頼性を保証できなくなる。したがって、熱交換器5のアルミニウムフィンとの望ましい電位差は0.3〜1.0Vであり、この範囲の電位差を確保できるものであればいろいろな金属板7が使用できる。   In an example using a zinc plate or a zinc iron plate, a potential difference of 0.4 V could be secured, and when a magnesium alloy (AZ91) plate was used, a potential difference of 0.8 V could be secured. In the present invention, the potential difference required for collecting bacteria by electrophoresis was at least 0.3 V or more. Further, if it exceeds 1.0 V, the leakage current cannot be ignored depending on the electric conductivity of the dew condensation water from the heat exchanger 5, and the melting of the metal plate 7 itself may start gradually. Reliability cannot be guaranteed. Therefore, a desirable potential difference with the aluminum fin of the heat exchanger 5 is 0.3 to 1.0 V, and various metal plates 7 can be used as long as the potential difference within this range can be secured.

また、上記実施の形態では、厚み3mmの発泡EPDMと厚さ1mmのPP不織布を使用した場合について説明したが、熱交換器5のアルミニウムフィンと金属板7との間隔は狭いほど電解強度を大きく保てるので望ましい。しかし両者が貯留部6の水中で短絡してしまっては意味がないのである程度安全率を見込んで設定するほうがよい。また両者を離せる最大の間隔距離としては結露水に影響を与えない電位差の最大値1.0Vにおいても十分な集菌、死滅化能力を発揮できる距離であり、実験により約5mmと判断した。したがって熱交換器5アルミニウムフィンと金属板7との間隔は5mm以下で絶縁状態が確保できていれば、下限は特に制約されない。   Moreover, although the case where the foam EPDM having a thickness of 3 mm and the PP nonwoven fabric having a thickness of 1 mm are used has been described in the above embodiment, the electrolytic strength increases as the distance between the aluminum fin of the heat exchanger 5 and the metal plate 7 decreases. This is desirable because it can be maintained. However, since it is meaningless if both of them are short-circuited in the water of the storage unit 6, it is better to set with a certain safety factor. Further, the maximum distance that can separate the two is a distance that can exhibit sufficient collection and killing ability even at the maximum potential difference of 1.0 V that does not affect the dew condensation water, and was determined to be about 5 mm by experiments. Accordingly, the lower limit is not particularly limited as long as the distance between the heat exchanger 5 aluminum fin and the metal plate 7 is 5 mm or less and an insulating state can be secured.

本発明の空気調和機は、加湿用結露水中の菌を長期的に死滅化することが可能となるので結露水を貯留する構成を持つ除湿機等の用途にも適用できる。   Since the air conditioner of the present invention can kill bacteria in the condensed water for humidification for a long period of time, it can be applied to a dehumidifier having a configuration for storing the condensed water.

本発明の実施の形態1における室外加湿装置の断面構成図Sectional block diagram of the outdoor humidifier in Embodiment 1 of the present invention 本発明の実施の形態2における室外加湿装置の熱交換器と亜鉛板との結線を示す正面構成図Front structure figure which shows the connection with the heat exchanger and zinc plate of the outdoor humidification apparatus in Embodiment 2 of this invention 本発明の実施の形態3における室外加湿装置の熱交換器と亜鉛板との結線を示す正面構成図Front structure figure which shows the connection with the heat exchanger and zinc plate of the outdoor humidification apparatus in Embodiment 3 of this invention 本発明の実施の形態4における室外加湿装置の熱交換器と亜鉛板との結線を示す正面構成図Front structure figure which shows the connection with the heat exchanger and zinc plate of the outdoor humidifier in Embodiment 4 of this invention 従来の室外加湿装置の断面構成図Cross-sectional configuration diagram of a conventional outdoor humidifier

符号の説明Explanation of symbols

1 室外加湿装置本体
2 送風機
3 吸湿体
4 ヒータ
5 熱交換器
6 貯留部
7 金属板
8 ポンプ
9 亜鉛板
10 発泡EPDM
11 銅線
12 端板
13 PP不織布
DESCRIPTION OF SYMBOLS 1 Outdoor humidifier body 2 Blower 3 Absorbent body 4 Heater 5 Heat exchanger 6 Storage part 7 Metal plate 8 Pump 9 Zinc plate 10 Foaming EPDM
11 Copper wire 12 End plate 13 PP Nonwoven fabric

Claims (7)

少なくとも空気中から水分を吸着する吸湿体と、前記吸湿体を加熱するヒーターと、前記吸湿体に空気を送風する送風手段とを具備した室外機において、前記ヒータ加熱時に前記吸湿体より放出される高温高湿空気中の水分を結露させる金属より構成される熱交換器と、前記熱交換器で発生した結露水を貯留する貯留部と、前記貯留部に貯留された結露水を室内機に搬送する搬送手段とを配設し、前記貯留部に金属板が配置され、前記金属板と前記熱交換器が導通するように結線されて前記貯留部に結露水が滞留した時には、前記金属板と前記熱交換器との間に内部起電力による電位差が生じ、前記金属板のほうが前記熱交換器より低電位となる構成であることを特徴とする空気調和機。 In an outdoor unit including at least a hygroscopic body that adsorbs moisture from the air, a heater that heats the hygroscopic body, and a blower that blows air to the hygroscopic body, the outdoor unit is released from the hygroscopic body when the heater is heated. A heat exchanger made of metal that condenses moisture in high-temperature, high-humidity air, a storage unit that stores the condensed water generated in the heat exchanger, and transports the condensed water stored in the storage unit to the indoor unit A metal plate is disposed in the storage unit, and when the metal plate and the heat exchanger are connected so that condensed water is accumulated in the storage unit, the metal plate and An air conditioner characterized in that a potential difference due to an internal electromotive force occurs between the heat exchanger and the metal plate has a lower potential than the heat exchanger. 前記結線位置が、前記貯留部に結露水が滞留した水面よりも上の位置となることを特徴とする請求項1記載の空気調和機。 2. The air conditioner according to claim 1, wherein the connection position is a position above a water surface where condensed water has accumulated in the storage section. 前記金属板と前記熱交換器との間の内部起電力が0.3〜1.0Vであることを特徴とする請求項1または2記載の空気調和機。 The air conditioner according to claim 1 or 2, wherein an internal electromotive force between the metal plate and the heat exchanger is 0.3 to 1.0V. 前記金属板と前記熱交換器の間に絶縁物が配されていることを特徴とする請求項1〜3いずれかに記載の空気調和機。 The air conditioner according to any one of claims 1 to 3, wherein an insulator is disposed between the metal plate and the heat exchanger. 前記金属板と前記熱交換器先端との間隔が5mm以下であることを特徴とする請求項4記載の空気調和機。 The air conditioner according to claim 4, wherein an interval between the metal plate and the tip of the heat exchanger is 5 mm or less. 前記絶縁物が樹脂の不織布あるいはメッシュであることを特徴とする請求項4または5記載の空気調和機。 6. The air conditioner according to claim 4, wherein the insulator is a resin nonwoven fabric or mesh. 前記金属板が亜鉛板、亜鉛メッキ鋼鈑、または亜鉛合金であることを特徴とする請求項1〜6いずれかに記載の空気調和機。 The air conditioner according to any one of claims 1 to 6, wherein the metal plate is a zinc plate, a galvanized steel plate, or a zinc alloy.
JP2003408624A 2003-12-08 2003-12-08 Air conditioner Pending JP2005172260A (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008207046A (en) * 2007-02-23 2008-09-11 Matsushita Electric Ind Co Ltd Hybrid dehumidifying apparatus
JP2009106925A (en) * 2007-10-10 2009-05-21 Erubu:Kk Water treatment apparatus
JP2010048471A (en) * 2008-08-22 2010-03-04 Hitachi Appliances Inc Indoor embedded type heat source machine
EP2230467A1 (en) * 2007-12-18 2010-09-22 Daikin Industries, Ltd. Humidity control device
JP2018109455A (en) * 2016-12-28 2018-07-12 株式会社前川製作所 Air-cooled type heat exchange unit and cooler unit
CN111829121A (en) * 2020-06-11 2020-10-27 姜玲华 Heating pipe system utilizing steam for humidification

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008207046A (en) * 2007-02-23 2008-09-11 Matsushita Electric Ind Co Ltd Hybrid dehumidifying apparatus
JP2009106925A (en) * 2007-10-10 2009-05-21 Erubu:Kk Water treatment apparatus
EP2230467A1 (en) * 2007-12-18 2010-09-22 Daikin Industries, Ltd. Humidity control device
EP2230467A4 (en) * 2007-12-18 2014-12-10 Daikin Ind Ltd Humidity control device
JP2010048471A (en) * 2008-08-22 2010-03-04 Hitachi Appliances Inc Indoor embedded type heat source machine
JP4734386B2 (en) * 2008-08-22 2011-07-27 日立アプライアンス株式会社 Indoor embedded heat source machine
JP2018109455A (en) * 2016-12-28 2018-07-12 株式会社前川製作所 Air-cooled type heat exchange unit and cooler unit
CN111829121A (en) * 2020-06-11 2020-10-27 姜玲华 Heating pipe system utilizing steam for humidification

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