JP2014149134A - Heat exchange device, and cooling device of condenser using the heat exchange device - Google Patents

Heat exchange device, and cooling device of condenser using the heat exchange device Download PDF

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JP2014149134A
JP2014149134A JP2013019076A JP2013019076A JP2014149134A JP 2014149134 A JP2014149134 A JP 2014149134A JP 2013019076 A JP2013019076 A JP 2013019076A JP 2013019076 A JP2013019076 A JP 2013019076A JP 2014149134 A JP2014149134 A JP 2014149134A
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heat exchanger
air
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latent heat
vaporization type
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Ryohei Hamano
良平 浜野
Kosuke Hamano
晃輔 浜野
Takayuki Ikeda
孝幸 池田
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AKUATEKKU KK
Aquatech Corp
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Aquatech Corp
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Abstract

PROBLEM TO BE SOLVED: To lower a temperature of air while keeping a humidity approximately same as that of the outdoor air by using a heat exchange device in which a vaporization type latent heat exchanger and a sensible heat exchanger are combined.SOLUTION: A heat exchange device is provided with a first vaporization type latent heat exchanger 11 for lowering a temperature of intake air by utilizing latent heat in vaporizing water, and a first sensible heat exchanger 33 in which air intake directions are orthogonal to each other to exchange heat between the air taken in the orthogonal directions. The first sensible heat exchanger 33 is disposed at a downstream side of the air of the first vaporization type latent heat exchanger 11. The air having exchanged heat in the vaporization-type latent heat exchanger 11 and the outdoor air, exchange heat by the sensible heat exchanger 33. A temperature of the air from the sensible heat exchanger 33 can be lowered while keeping a humidity approximately same as that of the outdoor air.

Description

本発明は、気化式潜熱交換器と顕熱交換器とを組み合わせた熱交換装置及びこの熱交換装置を用いた凝縮器の冷却装置に関するものである。。   The present invention relates to a heat exchange device in which a vaporization type latent heat exchanger and a sensible heat exchanger are combined, and a condenser cooling device using the heat exchange device. .

従来より、気化式潜熱交換器を用いた空気調和機が提供されている。例えば、下記に示す特許文献1が挙げられる。   Conventionally, an air conditioner using a vaporization type latent heat exchanger has been provided. For example, Patent Document 1 shown below can be cited.

特開2004−309113号公報JP 2004-309113 A

また、顕熱交換器を用いている空気調和機もある。そして、これらの気化式潜熱交換器あるいは顕熱交換器を用いて、夏場でも冷房運転時での空気の温度を下げるようにしている。   There is also an air conditioner that uses a sensible heat exchanger. These vaporization type latent heat exchangers or sensible heat exchangers are used to lower the temperature of air during the cooling operation even in summer.

しかしながら、従来の空気調和機では、気化式潜熱交換器あるいは顕熱交換器を単独で用いており、気化式潜熱交換器では出口側の湿度が高くなると、空気の温度を下げる能力が低下し、それ以上温度を下げることができないという問題を有している。
また、気化式潜熱交換器あるいは顕熱交換器単独での使用は、ある程度は空気の温度を冷却することが可能ではあるものの、気化式潜熱交換器あるいは顕熱交換器の単独での使用は、限界があるのが現状である。
However, in the conventional air conditioner, a vaporization type latent heat exchanger or a sensible heat exchanger is used alone. In the vaporization type latent heat exchanger, when the humidity on the outlet side increases, the ability to lower the temperature of the air decreases, There is a problem that the temperature cannot be lowered any further.
In addition, the use of the vaporization type latent heat exchanger or the sensible heat exchanger alone can cool the temperature of the air to some extent, but the use of the vaporization type latent heat exchanger or the sensible heat exchanger alone, The current situation is limited.

本発明は上述の問題点に鑑みて提供したものであって、気化式潜熱交換器と顕熱交換器を組み合わせた熱交換装置を用いることで、外気と同じ程度の湿度のまま空気の温度を下げるようにし、また、この熱交換器からの空気を空気調和機の凝縮器に当てることで、効率良く冷房運転をできるようにした熱交換装置及びこの熱交換装置を用いた凝縮器の冷却装置を提供することを目的としている。   The present invention has been provided in view of the above-mentioned problems, and by using a heat exchange device that combines a vaporization type latent heat exchanger and a sensible heat exchanger, the temperature of the air is maintained at the same level of humidity as the outside air. And a heat exchanger capable of performing an efficient cooling operation by applying air from the heat exchanger to the condenser of the air conditioner, and a condenser cooling device using the heat exchanger The purpose is to provide.

そこで、本発明の請求項1に記載の熱交換装置では、水が気化する際の潜熱を利用して吸気された空気の温度を低下させる第1の気化式潜熱交換器11と、
空気の吸気方向が互いに直交し、直交方向に吸気された空気間で熱交換を行なう第1の顕熱交換器33とを備え、
前記第1の気化式潜熱交換器11の空気の下流側に前記第1の顕熱交換器33を配置していることを特徴としている。
Therefore, in the heat exchange device according to claim 1 of the present invention, the first vaporization type latent heat exchanger 11 that lowers the temperature of the air taken in by utilizing the latent heat generated when water vaporizes;
A first sensible heat exchanger 33 that exchanges heat between the air sucked in the orthogonal direction and the air intake directions are orthogonal to each other;
The first sensible heat exchanger 33 is arranged on the downstream side of the air of the first vaporization type latent heat exchanger 11.

請求項2に記載の熱交換装置では、前記第1の顕熱交換器33で熱交換され、空気の温度が低下した側の該第1の顕熱交換器33の下流側に、前記第1の気化式潜熱交換器11と同様の構成からなる第2の気化式潜熱交換器11aを配置していることを特徴としている。   In the heat exchange device according to claim 2, heat exchange is performed in the first sensible heat exchanger 33, and the first sensible heat exchanger 33 on the downstream side of the first sensible heat exchanger 33 is disposed on the downstream side. The second vaporization type latent heat exchanger 11a having the same configuration as that of the vaporization type latent heat exchanger 11 is arranged.

請求項3に記載の熱交換装置では、水が気化する際の潜熱を利用して吸気された空気の温度を低下させる第1の気化式潜熱交換器11と、空気の吸気方向が互いに直交し、直交方向に吸気された空気間で熱交換を行ない前記第1の気化式潜熱交換器11の空気の下流側に配置した第1の顕熱交換器33とで第1の熱交換装置を構成し、
前記第1の気化式潜熱交換器11及び第1の顕熱交換器33と同様の構成からなる第2の気化式潜熱交換器11b及び第2の顕熱交換器33bとで第2の熱交換装置を構成し、
前記第1の気化式潜熱交換器11及び第1の顕熱交換器33と同様の構成からなる第3の気化式潜熱交換器11a及び第3の顕熱交換器33aとで第3の熱交換装置を構成し、
前記第1の顕熱交換器33の下流側に前記第3の気化式潜熱交換器11aを配置すると共に、前記第2の顕熱交換器33bの下流側に前記第3の顕熱交換器33aを配置していることを特徴としている。
In the heat exchange device according to claim 3, the first vaporization type latent heat exchanger 11 for lowering the temperature of the sucked air by using latent heat when water is vaporized, and the intake direction of the air are orthogonal to each other. The first sensible heat exchanger 33 is arranged with the first sensible heat exchanger 33 arranged on the downstream side of the air of the first vaporization type latent heat exchanger 11 to exchange heat between the air sucked in the orthogonal direction. And
The second heat exchange is performed between the second vaporization type latent heat exchanger 11b and the second sensible heat exchanger 33b having the same configuration as the first vaporization type latent heat exchanger 11 and the first sensible heat exchanger 33. Configure the device,
A third heat exchange is performed between the third vaporization type latent heat exchanger 11a and the third sensible heat exchanger 33a having the same configuration as the first vaporization type latent heat exchanger 11 and the first sensible heat exchanger 33. Configure the device,
The third vaporization type latent heat exchanger 11a is disposed on the downstream side of the first sensible heat exchanger 33, and the third sensible heat exchanger 33a is disposed on the downstream side of the second sensible heat exchanger 33b. It is characterized by arranging.

請求項4に記載の熱交換装置では、水が気化する際の潜熱を利用して吸気された空気の温度を低下させる第1の気化式潜熱交換器11と、空気の吸気方向が互いに直交し、直交方向に吸気された空気間で熱交換を行ない前記第1の気化式潜熱交換器11の空気の下流側に配置した第1の顕熱交換器33とで第1の熱交換装置を構成し、
前記第1の気化式潜熱交換器11及び第1の顕熱交換器33と同様の構成からなる第2の気化式潜熱交換器11b及び第2の顕熱交換器33bとで第2の熱交換装置を構成し、
前記第1の気化式潜熱交換器11及び第1の顕熱交換器33と同様の構成からなる第3の気化式潜熱交換器11a及び第3の顕熱交換器33aと、前記第3の顕熱交換器33aの下流側に前記第3の気化式潜熱交換器11aを同様の構成からなる第4の気化式潜熱交換器11cとで第3の熱交換装置を構成し、
前記第1の顕熱交換器33の下流側に前記第3の気化式潜熱交換器11aを配置し、前記第2の顕熱交換器33bの下流側に前記第3の顕熱交換器33を配置していることを特徴としている。
In the heat exchange device according to claim 4, the first vaporization type latent heat exchanger 11 that lowers the temperature of the sucked air by using latent heat when water is vaporized, and the air intake direction are orthogonal to each other. The first sensible heat exchanger 33 is arranged with the first sensible heat exchanger 33 arranged on the downstream side of the air of the first vaporization type latent heat exchanger 11 to exchange heat between the air sucked in the orthogonal direction. And
The second heat exchange is performed between the second vaporization type latent heat exchanger 11b and the second sensible heat exchanger 33b having the same configuration as the first vaporization type latent heat exchanger 11 and the first sensible heat exchanger 33. Configure the device,
The third evaporative latent heat exchanger 11a and the third sensible heat exchanger 33a having the same configuration as the first evaporative latent heat exchanger 11 and the first sensible heat exchanger 33, and the third sensible heat exchanger A third heat exchange device is configured with the fourth vaporization type latent heat exchanger 11c having the same configuration as the third vaporization type latent heat exchanger 11a on the downstream side of the heat exchanger 33a,
The third vaporization type latent heat exchanger 11a is disposed on the downstream side of the first sensible heat exchanger 33, and the third sensible heat exchanger 33 is disposed on the downstream side of the second sensible heat exchanger 33b. It is characterized by being arranged.

請求項5に記載の熱交換装置を用いた凝縮器の冷却装置では、空気調和機の室外機1の凝縮器3の空気の吸い込みの上流側に、前記請求項1〜請求項4に記載のいずれかの熱交換装置を配置していることを特徴としている。   In the condenser cooling device using the heat exchange device according to claim 5, the upstream side of the air suction of the condenser 3 of the outdoor unit 1 of the air conditioner is described in the above claims 1 to 4. Any one of the heat exchange devices is arranged.

本発明の請求項1に記載の熱交換装置によれば、水が気化する際の潜熱を利用して吸気された空気の温度を低下させる第1の気化式潜熱交換器11と、
空気の吸気方向が互いに直交し、直交方向に吸気された空気間で熱交換を行なう第1の顕熱交換器33とを備え、
前記第1の気化式潜熱交換器11の空気の下流側に前記第1の顕熱交換器33を配置しているので、第1の顕熱交換器33により外気と同じ程度の湿度のまま温度を下げることができる。
According to the heat exchange device of the first aspect of the present invention, the first vaporization type latent heat exchanger 11 that lowers the temperature of the sucked air using the latent heat generated when water vaporizes;
A first sensible heat exchanger 33 that exchanges heat between the air sucked in the orthogonal direction and the air intake directions are orthogonal to each other;
Since the first sensible heat exchanger 33 is arranged on the downstream side of the air of the first vaporization type latent heat exchanger 11, the first sensible heat exchanger 33 keeps the temperature at the same level as the outside air. Can be lowered.

請求項2に記載の熱交換装置によれば、第1の顕熱交換器33で熱交換され、空気の温度が低下した側の該第1の顕熱交換器33の下流側に、前記第1の気化式潜熱交換器11と同様の構成からなる第2の気化式潜熱交換器11aを配置していることで、第2の気化式潜熱交換器11aにより更に温度を下げることができる。   According to the heat exchange device of claim 2, heat exchange is performed by the first sensible heat exchanger 33, and the first sensible heat exchanger 33 on the downstream side of the first sensible heat exchanger 33 is disposed on the downstream side. By arranging the second vaporization type latent heat exchanger 11a having the same configuration as that of the first vaporization type latent heat exchanger 11, the temperature can be further lowered by the second vaporization type latent heat exchanger 11a.

請求項3に記載の熱交換装置によれば、第1の顕熱交換器33の下流側に前記第3の気化式潜熱交換器11aを配置すると共に、前記第2の顕熱交換器33bの下流側に前記第3の顕熱交換器33aを配置しているので、第3の顕熱交換器33aから出る空気は、第2の顕熱交換器33bからの空気のため、外気と同じ程度の湿度のまま温度を下げることができる。また、複数の熱交器を介しているので、温度を一層下げることができる。   According to the heat exchange device according to claim 3, the third vaporization type latent heat exchanger 11a is disposed on the downstream side of the first sensible heat exchanger 33, and the second sensible heat exchanger 33b Since the third sensible heat exchanger 33a is disposed on the downstream side, the air from the third sensible heat exchanger 33a is the same as the outside air because it is the air from the second sensible heat exchanger 33b. The temperature can be lowered while maintaining the humidity. Moreover, since it passes through the several heat exchanger, temperature can be lowered further.

請求項4に記載の熱交換装置によれば、第1の顕熱交換器33の下流側に前記第3の気化式潜熱交換器11aを配置し、前記第2の顕熱交換器33bの下流側に前記第3の顕熱交換器33aを配置しているので、特に第3の顕熱交換器33aの下流側に第4の気化式潜熱交換器11cを設けおり、そのため、一層温度を下げることができる。   According to the heat exchange device of the fourth aspect, the third vaporization type latent heat exchanger 11a is disposed on the downstream side of the first sensible heat exchanger 33, and the downstream of the second sensible heat exchanger 33b. Since the third sensible heat exchanger 33a is arranged on the side, the fourth vaporization type latent heat exchanger 11c is provided on the downstream side of the third sensible heat exchanger 33a, and therefore the temperature is further lowered. be able to.

請求項5に記載の熱交換装置を用いた凝縮器の冷却装置によれば、空気調和機の室外機1の凝縮器3の空気の吸い込みの上流側に、前記請求項1〜請求項4に記載のいずれかの熱交換装置を配置していることで、凝縮器3に温度が低い空気を当てることができる。これにより夏場の高温時においても凝縮器3を効率良く冷房運転をすることができ、冷却効率を向上させることができる。   According to the condenser cooling device using the heat exchange device according to claim 5, in the upstream side of the air suction of the condenser 3 of the outdoor unit 1 of the air conditioner, By disposing any of the described heat exchange devices, air having a low temperature can be applied to the condenser 3. As a result, the condenser 3 can be efficiently cooled even at high temperatures in summer, and the cooling efficiency can be improved.

本発明の実施の形態における顕熱交換器の斜視図である。It is a perspective view of the sensible heat exchanger in embodiment of this invention. 本発明の実施の形態における顕熱交換器の正面図である。It is a front view of the sensible heat exchanger in embodiment of this invention. 本発明の実施の形態における気化式潜熱交換器の斜視図である。It is a perspective view of the vaporization type latent heat exchanger in an embodiment of the invention. 本発明の実施の形態における気化式潜熱交換器を用いた冷却装置の概略構成である。It is a schematic structure of the cooling device using the vaporization type latent heat exchanger in an embodiment of the invention. 本発明の実施の形態における気化式潜熱交換器を用いた冷却装置の正面図である。It is a front view of the cooling device using the vaporization type latent heat exchanger in an embodiment of the invention. 本発明の実施の形態における保水材を製作する場合の説明図である。It is explanatory drawing in the case of manufacturing the water retention material in embodiment of this invention. 本発明の実施の形態における保水材を製作する場合の説明図である。It is explanatory drawing in the case of manufacturing the water retention material in embodiment of this invention. 本発明の実施の形態における保水材を製作する場合の説明図である。It is explanatory drawing in the case of manufacturing the water retention material in embodiment of this invention. 本発明の実施の形態における保水材を製作する場合の説明図である。It is explanatory drawing in the case of manufacturing the water retention material in embodiment of this invention. 本発明の実施の形態における保水材の要部拡大断面図である。It is a principal part expanded sectional view of the water retention material in embodiment of this invention. 本発明の実施の形態における気化式潜熱交換器と顕熱交換器とを組み合わせた熱交換装置の構成図である。It is a block diagram of the heat exchange apparatus which combined the vaporization type latent heat exchanger and sensible heat exchanger in embodiment of this invention. 本発明の実施の形態における気化式潜熱交換器と顕熱交換器とを組み合わせた熱交換装置の概略構成図である。It is a schematic block diagram of the heat exchange apparatus which combined the vaporization type latent heat exchanger and sensible heat exchanger in embodiment of this invention. 本発明の実施の形態における図11に示す構成に気化式潜熱交換器を組み合わせた熱交換装置の構成図である。It is a block diagram of the heat exchange apparatus which combined the vaporization type latent heat exchanger with the structure shown in FIG. 11 in embodiment of this invention. 本発明の実施の形態における複数の気化式潜熱交換器と顕熱交換器を組み合わせた熱交換装置の構成図である。It is a block diagram of the heat exchange apparatus which combined the some vaporization type latent heat exchanger and sensible heat exchanger in embodiment of this invention. 本発明の実施の形態における複数の気化式潜熱交換器と顕熱交換器を組み合わせた熱交換装置の構成図である。It is a block diagram of the heat exchange apparatus which combined the some vaporization type latent heat exchanger and sensible heat exchanger in embodiment of this invention. 本発明の実施の形態における空気調和機の凝縮器の上流側に熱交換装置を配置した場合の構成図である。It is a block diagram at the time of arrange | positioning a heat exchange apparatus in the upstream of the condenser of the air conditioner in embodiment of this invention. 本発明の実施の形態における空気調和機の凝縮器の上流側に熱交換装置を配置した場合の概略構成図である。It is a schematic block diagram at the time of arrange | positioning a heat exchange apparatus in the upstream of the condenser of the air conditioner in embodiment of this invention. 本発明の実施の形態における空気調和機の冷凍サイクルを示す図である。It is a figure which shows the refrigerating cycle of the air conditioner in embodiment of this invention.

以下、本発明の実施の形態を図面を参照して詳細に説明する。図1は従来より知られている周知な顕熱交換器33の斜視図を、図2は顕熱交換器33の正面図をそれぞれ示している。顕熱交換器33の材料は、樹脂やアルミ材などの金属製が用いられる。   Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings. FIG. 1 is a perspective view of a well-known sensible heat exchanger 33 known in the art, and FIG. 2 is a front view of the sensible heat exchanger 33. The material of the sensible heat exchanger 33 is made of metal such as resin or aluminum.

顕熱交換器33の構成は周知なので詳細な説明は省略するが、上下方向に所定の間隔にて隔壁34が配設されていて、上下の隔壁34の間には例えばジグザク状に折曲した熱伝導板35が配設されている。上下の熱伝導板35の向きは互いに直交方向となっていて、図中の矢印に示すように、外部からの空気の流通が直交するようになっている。
また、空気の流通方向と同方向の端部には側板36がそれぞれ配設されている。また、隔壁34の面と熱伝導板35の各折曲した頂点の部分とは固着されており、隔壁34と熱伝導板35とは熱伝導が容易となっている。
Since the configuration of the sensible heat exchanger 33 is well known, detailed description will be omitted, but partition walls 34 are arranged at predetermined intervals in the vertical direction, and the upper and lower partition walls 34 are bent in a zigzag shape, for example. A heat conductive plate 35 is provided. The directions of the upper and lower heat conducting plates 35 are orthogonal to each other, and the air flow from the outside is orthogonal as shown by the arrows in the figure.
Further, side plates 36 are disposed at the end portions in the same direction as the air flow direction. Further, the surface of the partition wall 34 and the bent apex portion of the heat conduction plate 35 are fixed, and the heat conduction between the partition wall 34 and the heat conduction plate 35 is facilitated.

この顕熱交換器33は、図1の矢印Aに示す方向から流入する空気と、矢印B方向から流入する空気とが流通し、両者の空気の温度に違いにより熱交換が行なわれ、例えば、矢印Aの空気が、矢印Bの空気より高いと、矢印Aの空気は顕熱交換器33から排出した箇所で流入した温度より低い温度となる。
ここで、顕熱交換器33は周知のように、熱だけを交換するものであり、樹脂など湿気を通さない素材でできているので、湿度は交換されない。
In the sensible heat exchanger 33, air flowing in from the direction indicated by the arrow A in FIG. 1 and air flowing in from the direction of the arrow B circulate, and heat exchange is performed due to a difference in the temperature of both the air. If the air indicated by the arrow A is higher than the air indicated by the arrow B, the air indicated by the arrow A has a temperature lower than the temperature flowing in at the portion discharged from the sensible heat exchanger 33.
Here, as is well known, the sensible heat exchanger 33 exchanges only heat and is made of a material that does not allow moisture to pass through, such as a resin, so the humidity is not exchanged.

次に、気化式潜熱交換器11について説明する。図3は気化式潜熱交換器11の斜視図を示し、図4は気化式潜熱交換器11を用いた全体の冷却装置10の概略構成図を示している。また、図5は、図4のA方向から見た概略正面図を示している。   Next, the vaporization type latent heat exchanger 11 will be described. FIG. 3 is a perspective view of the vaporization type latent heat exchanger 11, and FIG. 4 is a schematic configuration diagram of the entire cooling device 10 using the vaporization type latent heat exchanger 11. FIG. 5 shows a schematic front view seen from the direction A in FIG.

冷却装置10は、詳しくは後述する気化式潜熱交換器11と、この気化式潜熱交換器11から排水管12を介して排水される水を回収する水回収装置13と、この水回収装置13に貯溜している水をポンプ14を介して前記気化式潜熱交換器11側に送る給水管15と、この給水管15からの水を気化式潜熱交換器11の上面に給水する給水装置16と、気化式潜熱交換器11へ外部の空気を吸引させるためのファン17等で構成されている。   The cooling device 10 includes a vaporization type latent heat exchanger 11, which will be described in detail later, a water recovery device 13 that collects water drained from the vaporization type latent heat exchanger 11 through the drain pipe 12, and a water recovery device 13. A water supply pipe 15 for sending the stored water to the vaporization type latent heat exchanger 11 side through the pump 14; a water supply device 16 for supplying water from the water supply pipe 15 to the upper surface of the vaporization type latent heat exchanger 11; It comprises a fan 17 or the like for sucking outside air to the vaporization type latent heat exchanger 11.

本実施形態では、水回収装置13内の水をポンプ14、給水管15を介して気化式潜熱交換器11へ循環させ、気化式潜熱交換器11内では水が気化する際の潜熱を利用して気化式潜熱交換器11内で吸気された空気の温度を低下させるものである。
気化式潜熱交換器11内を流下した水は排水管12を介して水回収装置13に回収される。
In this embodiment, the water in the water recovery apparatus 13 is circulated to the vaporizing latent heat exchanger 11 via the pump 14 and the water supply pipe 15, and the latent heat generated when water is vaporized is used in the vaporizing latent heat exchanger 11. Thus, the temperature of the air taken in the vaporizing latent heat exchanger 11 is lowered.
The water flowing down in the vaporization type latent heat exchanger 11 is recovered by the water recovery device 13 through the drain pipe 12.

水回収装置13へは、水道水等の補給水が補給水管20から供給されるようになっており、補給水管20にはフロート弁21が介装されている。このフロート弁21は、液面に浮かぶフロート22が液面の高さに応じて上下方向に移動することにより開閉する弁である。
水回収装置13の液面が所定の高さ以下になると、フロート22が下降してフロート弁21が開いて補給水管20から水が供給される。また、補給水が供給されていって液面が所定の高さ以上になると、フロート22が上昇してフロート弁21が閉じられ、補給水管20からの水の供給が停止される。
The water recovery device 13 is supplied with makeup water such as tap water from a makeup water pipe 20, and a float valve 21 is interposed in the makeup water pipe 20. The float valve 21 is a valve that opens and closes when the float 22 floating on the liquid surface moves in the vertical direction according to the height of the liquid surface.
When the liquid level of the water recovery device 13 becomes a predetermined height or less, the float 22 descends, the float valve 21 opens, and water is supplied from the makeup water pipe 20. Further, when makeup water is supplied and the liquid level reaches a predetermined height or more, the float 22 rises, the float valve 21 is closed, and the supply of water from the makeup water pipe 20 is stopped.

気化式潜熱交換器11へ水回収装置13からの水を循環させて給水する給水装置16は、気化式潜熱交換器11の幅方向と略同じ長さとし、例えばパイプに複数の穴を穿孔しておき、これらの穴から水を気化式潜熱交換器11の上面に滴下ないし散水するものである。   The water supply device 16 that circulates water from the water recovery device 13 to the vaporization type latent heat exchanger 11 to supply water has substantially the same length as the width direction of the vaporization type latent heat exchanger 11, for example, by drilling a plurality of holes in a pipe. In addition, water is dropped or sprinkled on the upper surface of the vaporizing latent heat exchanger 11 from these holes.

なお、図5に示すように気化式潜熱交換器11の下部には排水樋25が設けられており、この排水樋25の端部に排水管12が接続されて、気化式潜熱交換器11から流下した水は水回収装置13へ回収されるようになっている。   As shown in FIG. 5, a drainage basin 25 is provided at the lower part of the vaporization type latent heat exchanger 11, and a drainage pipe 12 is connected to the end of the drainage basin 25 so that the vaporization type latent heat exchanger 11 The water that has flowed down is recovered by the water recovery device 13.

次に、気化式潜熱交換器11の構成について説明する。気化式潜熱交換器11は、図4に示すように、外気が矢印に示すように吸い込まれて吐出される保水材30にて構成されている。なお、この保水材30は、一般に通称クーリングパッド( Cooling Pad )と呼ばれ、湿気を含む素材である紙材で構成されている。
また、このクーリングパッドは、主に畜舎並びに園芸用施設の温度を下げるために用いられるものであり、日本では、無窓畜舎、施設園芸用温室で広く使用されているものである。
Next, the configuration of the vaporization type latent heat exchanger 11 will be described. As shown in FIG. 4, the vaporization type latent heat exchanger 11 is composed of a water retaining material 30 that is sucked and discharged from outside air as indicated by an arrow. The water retaining material 30 is generally called a “cooling pad” and is made of a paper material that is a material containing moisture.
Moreover, this cooling pad is mainly used for lowering the temperature of barns and horticultural facilities, and in Japan, it is widely used in windowless barns and greenhouses for horticulture.

図6〜図9は保水材30の作り方を示しており、保水材30の構造を理解し易いように、この保水材30の構造について説明する。図6に示すように、波形形状をした波板材51を多層に積層して形成するものであり、それぞれの波板材51は、強固に加工された紙で出来ている。なお、波板材51の波形形状で形成されて連続して形成される溝52が、空気の流通路となる。
上下の波板材51を吸気方向に対して互い違いに任意の角度、例えば、30°前後に組み合わせ、上の波板材51の波の下側の頂点と、下の波板材51の波の上側の頂点とは交差する点、つまり、図7に示す黒丸(●)の部分を接着剤にて接着し、上下の波板材51を接着固定する。
6 to 9 show how to make the water retaining material 30, and the structure of the water retaining material 30 will be described so that the structure of the water retaining material 30 can be easily understood. As shown in FIG. 6, corrugated corrugated sheets 51 are formed by laminating multiple layers, and each corrugated sheet 51 is made of strongly processed paper. In addition, the groove | channel 52 formed in the waveform shape of the corrugated board material 51 and formed continuously becomes an air flow path.
The upper and lower corrugated sheets 51 are alternately combined at an arbitrary angle, for example, around 30 °, with respect to the intake direction, and the lower corrugation of the upper corrugated sheet 51 and the upper apex of the wave of the lower corrugated sheet 51 are combined. The crossing points, that is, the black circles (●) shown in FIG.

このようにして波板材51を多数積層したのが図8に示す保水材体55であり、この保水材体55を図中矢印のイ方向にカッター等にて切断することで、任意の厚みの保水材片56を得る。そして、図9に示すように、縦方向、横方向の矢印ロ、ハに示すようにカッター等にて切断することで、任意の大きさの保水材30を形成することができる。   A plurality of corrugated sheet materials 51 are laminated in the water retaining material body 55 shown in FIG. 8, and the water retaining material body 55 is cut with a cutter or the like in the direction indicated by the arrow in the drawing, so that an arbitrary thickness can be obtained. A water retaining material piece 56 is obtained. And as shown in FIG. 9, the water-retaining material 30 of arbitrary magnitude | sizes can be formed by cut | disconnecting with a cutter etc. as shown to the arrow B of the vertical direction and a horizontal direction.

なお、保水材30は、任意の厚みや大きさを容易に製作することができ、また、波板材51を上下に積層する際に、波板材51を任意の角度で傾斜して積層することで、外気の吸気方向に対する波板材51の各溝52の傾斜角度も任意に形成することができる。また、図6に示すように、溝52の幅寸法Lや高さ寸法Hを任意に製作することができる。   In addition, the water retaining material 30 can be easily manufactured in any thickness and size, and when the corrugated sheet material 51 is laminated up and down, the corrugated sheet material 51 is inclined and laminated at an arbitrary angle. The inclination angle of each groove 52 of the corrugated sheet material 51 with respect to the intake direction of outside air can also be arbitrarily formed. Moreover, as shown in FIG. 6, the width dimension L and the height dimension H of the groove | channel 52 can be manufactured arbitrarily.

図10は上記のようにして製作された保水材30の要部拡大断面図を示し、左方から矢印に示すように空気が保水材30の溝52(以後、この溝を「空気流通路」と称する。)を通過する。
この実線で示している空気流通路52は例えば、30°の傾きで上昇し、この実線で示されている空気流通路52と幅方向で隣接し、破線で示している空気流通路52は、例えば、30°の傾きで下降している構成となっている。これらの空気流通路52が保水材30の上下方向及び左右方向に連続して形成されている。
FIG. 10 shows an enlarged cross-sectional view of the main part of the water-retaining material 30 manufactured as described above. From the left, as shown by an arrow, the air is a groove 52 of the water-retaining material 30 (hereinafter, this groove is referred to as “air flow passage”). Pass through).
For example, the air flow passage 52 shown by the solid line rises with an inclination of 30 °, is adjacent to the air flow passage 52 shown by the solid line in the width direction, and the air flow passage 52 shown by the broken line is For example, it is configured to descend with an inclination of 30 °. These air flow passages 52 are formed continuously in the vertical direction and the horizontal direction of the water retaining material 30.

この保水材30に給水装置16からの水が滴下され、保水材30自体に水が吸水されて湿潤状態となり、同時に保水材30の表面、つまり各空気流通路52の表裏の面を水が流下していき、保水材30に吸収されなかった水は保水材30の表面を伝って水回収装置13へと流れて回収される。   Water from the water supply device 16 is dripped onto the water retaining material 30 and the water retaining material 30 itself absorbs water to become wet. At the same time, water flows down the surface of the water retaining material 30, that is, the front and back surfaces of each air flow passage 52. Then, the water that has not been absorbed by the water retention material 30 flows along the surface of the water retention material 30 to the water recovery device 13 and is recovered.

このように、気化式潜熱交換器11(保水材30)内では、水が気化する際の潜熱を利用して気化式潜熱交換器11内で吸気された空気の温度を低下させることができるようになっている。   Thus, in the vaporization type latent heat exchanger 11 (water retaining material 30), the temperature of the air sucked in the vaporization type latent heat exchanger 11 can be lowered using the latent heat generated when water is vaporized. It has become.

図11は、気化式潜熱交換器11と顕熱交換器33とを並設した状態を示し、矢印Aは気化式潜熱交換器11と顕熱交換器33とに流入して流れる空気の流れを示している。また、矢印Bは、矢印Aとは直交する方向で顕熱交換器33のみに流れる空気の流れを示している。ファン41は、矢印Aの方向に空気を吸引するためのものであり、また、ファン42は、、矢印Bの方向に空気を吸引するために設けている。
図12は、図11の構成の概略構成図を示している。
FIG. 11 shows a state in which the vaporization type latent heat exchanger 11 and the sensible heat exchanger 33 are arranged side by side, and an arrow A indicates the flow of air flowing into and flowing into the vaporization type latent heat exchanger 11 and the sensible heat exchanger 33. Show. An arrow B indicates a flow of air flowing only in the sensible heat exchanger 33 in a direction orthogonal to the arrow A. The fan 41 is for sucking air in the direction of arrow A, and the fan 42 is provided for sucking air in the direction of arrow B.
FIG. 12 shows a schematic configuration diagram of the configuration of FIG.

図11において、アとウは、上流側の外気である。気化式潜熱交換器11を通過したイでは、温度はアの部分より低く、湿度は高い状態となっている。また、顕熱交換器33で気化式潜熱交換器11からの空気とで熱交換が行なわれ、そのため、顕熱交換器33を通過した部分でのエは、外気のウより温度が低くなるが、湿度は外気と同じである。
これにより、外気と同じ程度の湿度のまま温度を下げることができる。
In FIG. 11, A and C are the outside air on the upstream side. In B which passed through the vaporization type latent heat exchanger 11, the temperature is lower than that of A and the humidity is high. Further, heat exchange is performed with the air from the vaporization type latent heat exchanger 11 in the sensible heat exchanger 33. Therefore, the temperature at the portion that has passed through the sensible heat exchanger 33 is lower than that of the outside air. The humidity is the same as the outside air.
Thereby, temperature can be lowered | hung with the humidity comparable as external air.

ここで、気化式潜熱交換器11を通過したイでの温度より、顕熱交換器33を通過したエでの温度は高いが、湿度が外気と同じなので、後述するようにエの温度をさらに低下させることができる。なお、イでは湿度が高いので、それ以上温度を低下させることが難しくなる。   Here, although the temperature in D that has passed through the sensible heat exchanger 33 is higher than the temperature in B that has passed through the vaporization type latent heat exchanger 11, the humidity is the same as that of the outside air. Can be reduced. Since the humidity is high in a, it is difficult to lower the temperature further.

図11に示す顕熱交換器33の下流側に気化式潜熱交換器11aを配置した状態を図13に示す。なお、新たに配置した気化式潜熱交換器11aの構成は、気化式潜熱交換器11と同じである。顕熱交換器33の下流側に配置した気化式潜熱交換器11aを通過したオでの空気の温度は、顕熱交換器33を通過したエの温度より低く、また湿度はエよりも高い状態となる。   FIG. 13 shows a state in which the vaporization type latent heat exchanger 11a is arranged on the downstream side of the sensible heat exchanger 33 shown in FIG. In addition, the structure of the newly arrange | positioned vaporization type latent heat exchanger 11a is the same as the vaporization type latent heat exchanger 11. The temperature of the air at E that has passed through the vaporization type latent heat exchanger 11a disposed downstream of the sensible heat exchanger 33 is lower than the temperature of D that has passed through the sensible heat exchanger 33, and the humidity is higher than that of D. It becomes.

気化式潜熱交換器11における上流のアと、下流のイとの温度の低下と、他方の気化式潜熱交換器11aにおける上流のエと、下流のオとの温度の低下の割合はほぼ同じである。そのため、イの温度よりエの温度の方が高いが、気化式潜熱交換器11aを通過することで、オでの温度をイでの温度よりかなり低くすることができる。このように、顕熱交換器33からの空気を気化式潜熱交換器11aにより更に温度を下げることができる。   The rate of decrease in the temperature of the upstream a in the vaporization type latent heat exchanger 11 and the downstream of the b, and the rate of decrease in the temperature of the upstream d in the other vaporization type latent heat exchanger 11a and that of the downstream e are almost the same. is there. Therefore, although the temperature of D is higher than the temperature of A, the temperature at O can be made considerably lower than the temperature at A by passing through the vaporization type latent heat exchanger 11a. In this way, the temperature of the air from the sensible heat exchanger 33 can be further lowered by the vaporization type latent heat exchanger 11a.

図14は、気化式潜熱交換器11と顕熱交換器33とを組み合わせものを3組配置した場合を示している。なお、説明の便宜上それぞれ離した状態で描いているが、実際は各熱交換器は隣接した状態である。   FIG. 14 shows a case where three combinations of the vaporization type latent heat exchanger 11 and the sensible heat exchanger 33 are arranged. In addition, although drawn in the state which each separated for convenience of explanation, in fact, each heat exchanger is in the adjacent state.

気化式潜熱交換器11で通過した空気の温度はT2であり、顕熱交換器33により熱交換された空気の温度T3は、温度T2よりは高い。また、気化式潜熱交換器11bと顕熱交換器33bとで熱交換された空気の温度T3は上記と同様である。気化式潜熱交換器11aで熱交換された空気の温度T4は、温度T3より低く、顕熱交換器33aにて熱交換された空気の温度はT5となる。   The temperature of the air that has passed through the vaporizing latent heat exchanger 11 is T2, and the temperature T3 of the air that has been heat-exchanged by the sensible heat exchanger 33 is higher than the temperature T2. Moreover, the temperature T3 of the air heat-exchanged with the vaporization type latent heat exchanger 11b and the sensible heat exchanger 33b is the same as the above. The temperature T4 of the air heat-exchanged by the vaporization type latent heat exchanger 11a is lower than the temperature T3, and the temperature of the air heat-exchanged by the sensible heat exchanger 33a is T5.

気化式潜熱交換器11a及び顕熱交換器33aとで熱交換を行なう場合に、気化式潜熱交換器11aに流入される空気を、その前段で気化式潜熱交換器11及び顕熱交換器33aとで熱交換された空気とし、また、顕熱交換器33aに流入される空気を、その前段で気化式潜熱交換器11b及び顕熱交換器33bとで熱交換された空気としていることで、顕熱交換器33aより通過した空気の温度T5を一層低下させることができる。なお、顕熱交換器33aより通過した空気の湿度は外気と同じである。
このように、図14の構成では、外気と同じ程度の湿度のまま温度を下げることができる。また、複数の熱交換器を介しているので、温度を一層下げることができる。
When heat exchange is performed between the vaporization type latent heat exchanger 11a and the sensible heat exchanger 33a, the air flowing into the vaporization type latent heat exchanger 11a is exchanged with the vaporization type latent heat exchanger 11 and the sensible heat exchanger 33a in the preceding stage. And the air flowing into the sensible heat exchanger 33a is the air that has been heat-exchanged between the vaporizing latent heat exchanger 11b and the sensible heat exchanger 33b in the preceding stage. The temperature T5 of the air that has passed through the heat exchanger 33a can be further reduced. The humidity of the air that has passed through the sensible heat exchanger 33a is the same as that of the outside air.
Thus, in the configuration of FIG. 14, the temperature can be lowered with the same degree of humidity as the outside air. Moreover, since it passes through the plurality of heat exchangers, the temperature can be further lowered.

図15は、図14の熱交換器の構成に対して顕熱交換器33aの下流側に気化式潜熱交換器11cを設けた場合を示している。この組み合わせでは、最後段に気化式潜熱交換器11cを設けていることで、気化式潜熱交換器11cからの空気の温度T6(<T5)を一層低下させることができる。なお、気化式潜熱交換器11cからの空気の湿度は外気より高くなっている。   FIG. 15 shows a case where a vaporizing latent heat exchanger 11c is provided on the downstream side of the sensible heat exchanger 33a with respect to the configuration of the heat exchanger of FIG. In this combination, the vaporization type latent heat exchanger 11c is provided at the last stage, so that the temperature T6 (<T5) of the air from the vaporization type latent heat exchanger 11c can be further reduced. In addition, the humidity of the air from the vaporization type latent heat exchanger 11c is higher than the outside air.

図16及び図17は、空気調和機の室外機1の凝縮器3の吸い込み空気の上流側に気化式潜熱交換器11、顕熱交換器33及び気化式潜熱交換器11aからなる熱交換装置44を設置した場合の概略構成図を示している。この熱交換装置44は、図13に示す構成と同じである。
また、図17及び図18は、理解し易いように、気化式潜熱交換器11、顕熱交換器33及び気化式潜熱交換器11aを直列的に描いているが、実際は、図16に示す配置構成となっている。
FIGS. 16 and 17 show a heat exchange device 44 comprising a vaporization type latent heat exchanger 11, a sensible heat exchanger 33, and a vaporization type latent heat exchanger 11a on the upstream side of the intake air of the condenser 3 of the outdoor unit 1 of the air conditioner. The schematic block diagram at the time of installing is shown. This heat exchange device 44 has the same configuration as shown in FIG.
17 and 18 depict the vaporization-type latent heat exchanger 11, the sensible heat exchanger 33, and the vaporization-type latent heat exchanger 11a in series for easy understanding, but in actuality, the arrangement shown in FIG. It has a configuration.

室外機1は、周知の構成であるため、詳細な説明は省略するが、室外機1のケース2の一方には凝縮器3が配置され、ケース2の上部には冷却ファン4が設けられている。なお、本実施形態では冷却ファン4をケース2の上部に設けているが、凝縮器3に対向した位置に冷却ファン4が設けられている場合もある。   Since the outdoor unit 1 has a well-known configuration, a detailed description is omitted, but a condenser 3 is disposed on one side of the case 2 of the outdoor unit 1, and a cooling fan 4 is provided on the upper side of the case 2. Yes. In the present embodiment, the cooling fan 4 is provided on the upper portion of the case 2, but the cooling fan 4 may be provided at a position facing the condenser 3.

熱交換装置44の顕熱交換器33は、図16及び図17に示すように、凝縮器3の大きさとほぼ同じか、若干大きめの大きさとしており、顕熱交換器33にて凝縮器3の空気の吸い込み面を覆う大きさである。   As shown in FIGS. 16 and 17, the sensible heat exchanger 33 of the heat exchange device 44 is approximately the same as or slightly larger than the size of the condenser 3. It is a size that covers the air suction surface.

図18は、周知な冷凍サイクルを示し、冷凍サイクルは、凝縮器3、圧縮器5、室内に設置される室内機内の蒸発器6、膨張弁7等で構成されており、それぞれ冷媒管8にて接続されている。
冷房運転時では、圧縮器5で冷媒管8内の冷媒が圧縮されて、冷媒は高温ガスになり、凝縮器3内を冷却ファン4にて気化する際の水の潜熱にて一定の温度に下げられ冷媒ガスは液化する。膨張弁7にて冷媒の圧力は急激に下げられ、冷媒ガスの潜熱で冷たくなり、蒸発器6で部屋の温度を熱交換を行ない、室内機から冷風が部屋内に送られて冷房が行なわれる。
FIG. 18 shows a well-known refrigeration cycle. The refrigeration cycle includes a condenser 3, a compressor 5, an evaporator 6 in an indoor unit installed indoors, an expansion valve 7, and the like. Connected.
During the cooling operation, the refrigerant in the refrigerant pipe 8 is compressed by the compressor 5, and the refrigerant becomes a high-temperature gas. The refrigerant 3 is kept at a constant temperature by the latent heat of water when the condenser 3 is vaporized by the cooling fan 4. The refrigerant gas is liquefied by being lowered. The refrigerant pressure is suddenly lowered by the expansion valve 7 and is cooled by the latent heat of the refrigerant gas. The temperature of the room is exchanged by the evaporator 6, and the cool air is sent from the indoor unit to the room for cooling. .

なお、図18では、気化式潜熱交換器11、11aの上方にはそれぞれ給水装置16を配設することから、給水管15を分岐したパイプ15a、15aにより給水装置16へ水を供給するようにしている。   In FIG. 18, since the water supply device 16 is disposed above the vaporization type latent heat exchangers 11 and 11a, water is supplied to the water supply device 16 through the pipes 15a and 15a branched from the water supply pipe 15. ing.

図16及び図17では、熱交換装置44の構成を図13の場合のものを用いているが、図11、図14、図15のいずれかの熱交換装置44を用いるようにしてもよいものである。   16 and 17, the configuration of the heat exchange device 44 in the case of FIG. 13 is used, but the heat exchange device 44 in any of FIGS. 11, 14, and 15 may be used. It is.

このように、室外機1の凝縮器3の上流側に気化式潜熱交換器11及び顕熱交換器33からなる熱交換装置44を配置していることで、凝縮器3に温度が低い空気を当てることができる。これにより、夏場の高温時においても凝縮器3を効率良く冷房運転することができ、冷却効率を向上させることができる。   As described above, by arranging the heat exchange device 44 including the vaporization type latent heat exchanger 11 and the sensible heat exchanger 33 on the upstream side of the condenser 3 of the outdoor unit 1, air having a low temperature is supplied to the condenser 3. You can guess. Thereby, the condenser 3 can be efficiently cooled even at high temperatures in summer, and the cooling efficiency can be improved.

1 室外機
3 凝縮器
11 第1の気化式潜熱交換器
11b 第2の気化式潜熱交換器
11a 第3の気化式潜熱交換器
11c 第4の気化式潜熱交換器
33 第1の顕熱交換器
33b 第2の顕熱交換器
33a 第3の顕熱交換器
44 熱交換装置
DESCRIPTION OF SYMBOLS 1 Outdoor unit 3 Condenser 11 1st vaporization type latent heat exchanger 11b 2nd vaporization type latent heat exchanger 11a 3rd vaporization type latent heat exchanger 11c 4th vaporization type latent heat exchanger 33 1st sensible heat exchanger 33b 2nd sensible heat exchanger 33a 3rd sensible heat exchanger 44 Heat exchange apparatus

Claims (5)

水が気化する際の潜熱を利用して吸気された空気の温度を低下させる第1の気化式潜熱交換器(11)と、
空気の吸気方向が互いに直交し、直交方向に吸気された空気間で熱交換を行なう第1の顕熱交換器(33)とを備え、
前記第1の気化式潜熱交換器(11)の空気の下流側に前記第1の顕熱交換器(33)を配置していることを特徴とする熱交換装置。
A first vaporization-type latent heat exchanger (11) for lowering the temperature of the sucked air using latent heat generated when water vaporizes;
A first sensible heat exchanger (33) for performing heat exchange between the air sucked in the orthogonal direction, the air intake directions being orthogonal to each other;
The heat exchange apparatus, wherein the first sensible heat exchanger (33) is disposed downstream of the air of the first vaporization type latent heat exchanger (11).
前記第1の顕熱交換器(33)で熱交換され、空気の温度が低下した側の該第1の顕熱交換器(33)の下流側に、前記第1の気化式潜熱交換器(11)と同様の構成からなる第2の気化式潜熱交換器(11a)を配置していることを特徴とする請求項1に記載の熱交換装置。   Heat is exchanged in the first sensible heat exchanger (33), and on the downstream side of the first sensible heat exchanger (33) on the side where the temperature of the air is reduced, the first vaporization type latent heat exchanger ( The heat exchange apparatus according to claim 1, wherein a second vaporization type latent heat exchanger (11a) having the same configuration as in 11) is arranged. 水が気化する際の潜熱を利用して吸気された空気の温度を低下させる第1の気化式潜熱交換器(11)と、空気の吸気方向が互いに直交し、直交方向に吸気された空気間で熱交換を行ない前記第1の気化式潜熱交換器(11)の空気の下流側に配置した第1の顕熱交換器(33)とで第1の熱交換装置を構成し、
前記第1の気化式潜熱交換器(11)及び第1の顕熱交換器(33)と同様の構成からなる第2の気化式潜熱交換器(11b)及び第2の顕熱交換器(33b)とで第2の熱交換装置を構成し、
前記第1の気化式潜熱交換器(11)及び第1の顕熱交換器(33)と同様の構成からなる第3の気化式潜熱交換器(11a)及び第3の顕熱交換器(33a)とで第3の熱交換装置を構成し、
前記第1の顕熱交換器(33)の下流側に前記第3の気化式潜熱交換器(11a)を配置すると共に、前記第2の顕熱交換器(33b)の下流側に前記第3の顕熱交換器(33a)を配置していることを特徴とする熱交換装置。
Between the first vaporization-type latent heat exchanger (11) that lowers the temperature of the sucked air using the latent heat when water is vaporized, and the air sucked in the orthogonal direction. The first heat exchange device is configured with the first sensible heat exchanger (33) disposed on the downstream side of the air of the first vaporization type latent heat exchanger (11) that performs heat exchange at
The second vaporization type latent heat exchanger (11b) and the second sensible heat exchanger (33b) having the same configuration as the first vaporization type latent heat exchanger (11) and the first sensible heat exchanger (33). ) And the second heat exchange device,
The third vaporization type latent heat exchanger (11a) and the third sensible heat exchanger (33a) having the same configuration as the first vaporization type latent heat exchanger (11) and the first sensible heat exchanger (33). ) And the third heat exchange device,
The third vaporization type latent heat exchanger (11a) is disposed downstream of the first sensible heat exchanger (33), and the third sensible heat exchanger (33b) is disposed downstream of the third sensible heat exchanger (33b). A sensible heat exchanger (33a) is arranged.
水が気化する際の潜熱を利用して吸気された空気の温度を低下させる第1の気化式潜熱交換器(11)と、空気の吸気方向が互いに直交し、直交方向に吸気された空気間で熱交換を行ない前記第1の気化式潜熱交換器(11)の空気の下流側に配置した第1の顕熱交換器(33)とで第1の熱交換装置を構成し、
前記第1の気化式潜熱交換器(11)及び第1の顕熱交換器(33)と同様の構成からなる第2の気化式潜熱交換器(11b)及び第2の顕熱交換器(33b)とで第2の熱交換装置を構成し、
前記第1の気化式潜熱交換器(11)及び第1の顕熱交換器(33)と同様の構成からなる第3の気化式潜熱交換器(11a)及び第3の顕熱交換器(33a)と、前記第3の顕熱交換器(33a)の下流側に前記第3の気化式潜熱交換器(11a)を同様の構成からなる第4の気化式潜熱交換器(11c)とで第3の熱交換装置を構成し、
前記第1の顕熱交換器(33)の下流側に前記第3の気化式潜熱交換器(11a)を配置し、前記第2の顕熱交換器(33b)の下流側に前記第3の顕熱交換器(33a)を配置していることを特徴とする熱交換装置。
Between the first vaporization-type latent heat exchanger (11) that lowers the temperature of the sucked air using the latent heat when water is vaporized, and the air sucked in the orthogonal direction. The first heat exchange device is configured with the first sensible heat exchanger (33) disposed on the downstream side of the air of the first vaporization type latent heat exchanger (11) that performs heat exchange at
The second vaporization type latent heat exchanger (11b) and the second sensible heat exchanger (33b) having the same configuration as the first vaporization type latent heat exchanger (11) and the first sensible heat exchanger (33). ) And the second heat exchange device,
The third vaporization type latent heat exchanger (11a) and the third sensible heat exchanger (33a) having the same configuration as the first vaporization type latent heat exchanger (11) and the first sensible heat exchanger (33). ) And the fourth vaporization type latent heat exchanger (11c) having the same configuration as the third vaporization type latent heat exchanger (11a) on the downstream side of the third sensible heat exchanger (33a). 3 heat exchange device,
The third vaporization type latent heat exchanger (11a) is disposed downstream of the first sensible heat exchanger (33), and the third sensible heat exchanger (33b) is downstream of the third sensible heat exchanger (33b). The heat exchange apparatus characterized by arrange | positioning the sensible heat exchanger (33a).
空気調和機の室外機(1)の凝縮器(3)の空気の吸い込みの上流側に、前記請求項1〜請求項4に記載のいずれかの熱交換装置を配置していることを特徴とする熱交換装置を用いた凝縮器の冷却装置。   The heat exchange device according to any one of claims 1 to 4 is arranged upstream of the air suction of the condenser (3) of the outdoor unit (1) of the air conditioner. A condenser cooling device using a heat exchange device.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018025359A (en) * 2016-08-10 2018-02-15 富士電機株式会社 Air conditioning device and air conditioning system
JP2021113676A (en) * 2020-01-20 2021-08-05 ブラザー工業株式会社 air conditioner
JP2021181882A (en) * 2019-07-18 2021-11-25 ブラザー工業株式会社 air conditioner

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JPH06294590A (en) * 1993-04-07 1994-10-21 Abb Gadelius Kk Enthalpy exchanging device
JP2003139350A (en) * 2001-10-31 2003-05-14 Seibu Giken Co Ltd Dehumidifying air conditioner

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JP2003139350A (en) * 2001-10-31 2003-05-14 Seibu Giken Co Ltd Dehumidifying air conditioner

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Publication number Priority date Publication date Assignee Title
JP2018025359A (en) * 2016-08-10 2018-02-15 富士電機株式会社 Air conditioning device and air conditioning system
JP2021181882A (en) * 2019-07-18 2021-11-25 ブラザー工業株式会社 air conditioner
JP7388413B2 (en) 2019-07-18 2023-11-29 ブラザー工業株式会社 air conditioner
JP2021113676A (en) * 2020-01-20 2021-08-05 ブラザー工業株式会社 air conditioner

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