JP7161650B2 - Dehumidification air conditioner - Google Patents
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- JP7161650B2 JP7161650B2 JP2016177104A JP2016177104A JP7161650B2 JP 7161650 B2 JP7161650 B2 JP 7161650B2 JP 2016177104 A JP2016177104 A JP 2016177104A JP 2016177104 A JP2016177104 A JP 2016177104A JP 7161650 B2 JP7161650 B2 JP 7161650B2
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住居、オフィス、工場、畜舎等を除加湿空調する。
除湿して、夏季の空調を行い、快適な環境を作ることが望まれているが除湿すると、従来の除湿装置では、消費電力が増加する。本件は除加湿して消費電力を減少する空調装置に関する。Dehumidify and air-condition houses, offices, factories, livestock barns, etc.
It is desired to create a comfortable environment by dehumidifying and air-conditioning in summer, but dehumidification increases power consumption in conventional dehumidifiers. The present invention relates to an air conditioner that dehumidifies and reduces power consumption.
除湿方法の主な種類は1.冷却除湿方法 2.乾式除湿方法、3.噴霧除湿方法 4.湿式除湿方法等である。The main types of dehumidification methods are 1. Cooling and dehumidifying
冷却除湿方法はエアコンと称していて、夏期に25℃で運転すると、冷房と同時に同時に除湿も作動する様に工夫されており、相対湿度が60%RHになるようになっている。空気を一旦露点温度以下まで下げなければ除湿しないので、吹き出し温度を空調温度より、10℃以上に下げているため、大きなエネルギーを必要している。
又、除湿モードで、運転すると、熱交換フィンの速度が遅くするため、室温は25℃以上に上昇する。また、25℃の冷房温度運転時より、冷凍機がフル回転になるために消費電力が増大する。
一般的に使用しているエアコンは冷却除湿方式であり、25℃に設定運転をすると相対湿度が、60%RH前後又は以下になるように設計されており、快適環境になる。最近は環境庁より、省エネするために、夏季の空調温度を28℃に上げる様に要請があるが、28℃で運転すると、空気中の絶対水分量が上がり、快適環境にならないから、実行されていない場合が多い。The cooling and dehumidification method is called an air conditioner, and when it is operated at 25°C in the summer, it is devised so that the dehumidification is operated simultaneously with the cooling, and the relative humidity is 60% RH. Since the air cannot be dehumidified unless it is once lowered to below the dew point temperature, the blowing temperature is lowered to 10° C. or higher than the air conditioning temperature, which requires a large amount of energy.
Also, when operating in the dehumidifying mode, the speed of the heat exchange fins slows down, so the room temperature rises above 25°C. In addition, power consumption increases since the refrigerator rotates at full speed from the cooling temperature operation of 25°C.
Generally used air conditioners are of the cooling and dehumidifying type, and are designed to keep the relative humidity around or below 60% RH when set to 25°C, creating a comfortable environment. Recently, the Environment Agency has requested that the air conditioning temperature be raised to 28°C in the summer in order to save energy. often not.
乾式除湿方法はシリカゲルに空気を接触させて、除湿する方法である。
この方法はシリカゲルに付着した水分を除く作業が不可欠であり、120℃以上の熱風でシリカゲルを再生しなければならない。
このためにシリカゲルへの加熱電力と、シリカゲルと接触した空気が加熱されるので、余熱を冷却するための冷却電力が必要となる。
最近、稚内の珪藻土を利用し低温度での再生が報じられているが、除湿量が少ないので、未だ実用化されていない。The dry dehumidification method is a method of dehumidifying silica gel by contacting it with air.
In this method, it is essential to remove the water adhering to the silica gel, and the silica gel must be regenerated with hot air of 120° C. or higher.
For this reason, heating power for the silica gel and cooling power for cooling the residual heat are required because the air in contact with the silica gel is heated.
Recently, it has been reported that diatomaceous earth from Wakkanai can be used for regeneration at low temperatures, but it has not yet been put to practical use because the amount of dehumidification is small.
噴霧除湿方法は露点室の中で露点温度に冷却し水を霧状に噴霧して空気気を冷却する方法であるが、この方法は必ず再熱する必要になるので、環境試験機などの小型環境試験機などの小型空調では有効であるが、住宅などの一般空調には不向きである。 The spray dehumidification method is a method of cooling the air to the dew point temperature in the dew point chamber and spraying water in the form of a mist to cool the air. It is effective for small air conditioners such as environmental test machines, but it is not suitable for general air conditioners such as houses.
湿式除加湿方法にて、塩化リチュームや塩化カルシューム溶液を利用した湿式除加湿であり、25℃~30℃の範囲であれば大量の除湿効果ある省エネが可能あるが、塩化リチュームや塩化カルシューム溶液等の再生装置が必要なため、装置が大型化し高価であり、廃液となった、塩化リチュームや塩化カルシュームの廃液処理が必要であるので、あまり普及していない。 In the wet dehumidification method, it is a wet dehumidification method using lithium chloride or calcium chloride solution, and if it is in the range of 25 ° C to 30 ° C, it is possible to save energy with a large amount of dehumidification effect, but lithium chloride, calcium chloride solution, etc. Since a regenerating device is required, the device is large and expensive, and it is necessary to treat the waste liquid of lithium chloride and calcium chloride, so it is not widely used.
住居、オフィス、工場、畜舎等を空調する(以後一般空調と称する。)場合には温度調節はおこなわれているが湿度調節はほとんど行われていない。
その訳は消費電力が増加するからである。本発明は湿度調節をして空調の省エネを行なう。When air-conditioning houses, offices, factories, livestock barns, etc. (hereinafter referred to as general air-conditioning), temperature control is performed, but humidity control is hardly performed.
The reason is that power consumption increases. The present invention regulates humidity to save energy in air conditioning.
外国の乾燥地帯では、気温30℃でも、相対湿度が低いので、快適に感じる。恒温恒湿室にて体感試験して真意を確認する実験を行った。エアコンの最適冷却温度は25℃運転時と、室温30℃で相対湿度が40%の比較ではエアコン25℃運転とほとんど同じであった。
20年程前に、体感温度が50人中45人は同じであると千葉大学工学部都市環境部の試験結果(論文これからの空調)がある。この時の除湿方法は乾式除湿方法で記載されていた。In arid regions of foreign countries, even with a temperature of 30°C, the relative humidity is low and one feels comfortable. An experiment was conducted to confirm the real intention by performing a sensory test in a constant temperature and humidity room. The optimum cooling temperature of the air conditioner was almost the same as the air conditioner operating at 25°C when the room temperature was 30°C and the relative humidity was 40%.
About 20 years ago, according to the results of a test conducted by the Department of Urban Environment, Faculty of Engineering, Chiba University, 45 out of 50 people had the same sensible temperature. The dehumidification method at this time was described as a dry dehumidification method.
誰でも水で加湿することは知っていますが、水で除湿することはあまり知られていません。その実験を図3の恒温恒湿を使用して、実験をします。
密閉した恒温恒湿室に水槽を作り、水を張りみずを冷却出来る様に冷却コイルを設置して、水の温度が調節冷却出来る様にします。
「実験 1」室温30℃水温30℃(成り行き制御)にすると、相対湿度100%になる
「実験 2」室温30℃水温25℃(冷却制御)にすると、相対湿度65%になる
「実験 3」室温30℃水温20℃(冷却制御)にすると、相対湿度40%になる
以上の実験から、冷却した水が除湿したことになる。また水温が湿球温度と同じであることをも発見した。Everyone knows about humidifying with water, but not many people know about dehumidifying with water. The experiment will be conducted using the constant temperature and humidity shown in Figure 3.
A water tank is created in a sealed constant temperature and humidity chamber, and a cooling coil is installed so that the water can be cooled and the temperature of the water can be adjusted and cooled.
"
本発明の立体水面の説明をします。冷房時はヒートポンプ8を冷房運転に選択し、ヒートポンプフィン6で室内空気冷房すると同時、プレート熱交換器5にも冷媒を送り、水温を室内温度の湿球温度より低い温度以下に冷却水を不織布2の上部から流し、室内空気と接触させて除湿を行い、煖房時はヒートポンプ8を煖房運転に選択し、ヒートポンプフィン6で室内空気を煖房すると同時に、プレート熱交換器5にも冷媒を送り、水温を室内空気の湿球温度より高い温度に加熱した水を不織布2の上部から流し、室内空気と接触させて加湿を行う空調機である。 I will explain the three-dimensional water surface of the present invention. At the time of cooling, the
従来のエアコンでは室温25℃運転の室内相対湿度制御すると、相対湿度が60%になる様設計されているので、相対湿度が60%になる。従って室内空気のエンタルピーは(hb57)となり、吹き出し空気温度は15℃なる、従って、吹き出しエンタルピーは(hc42.7)になる、空調機の負荷はエンタルピー差は13.3である。
本発明の立体水面よる空調負荷は、室内の湿度で30℃、室内の相対湿度40%、であり、室内のエンタルピーは(RM57.9)であり、吹き出し空気の温度23.4相対湿度57%であるが、吹き出しエンタルピーは(RM52.0)であるので、本願のエンタルピー差5.9であるから。
従来のエアコンとの、エンタルピー差は13.3に対して、本願の立体水面によるエンタルピー差は5.9であるので、55.4%の省エネになる。その計算は従来方式の本発明の立体水面よる空調負荷(hb57)-(hc42.7)=13.3であり、
本発明の立体水面よる空調負荷の本発明の立体水面よる空調負荷エンタルピー差は(RM57.9)-(RC52.0)=5.9であるから、
消費エンタルピー差比較は44.6%になり、省エネ率の比較では、55.4%である吹き出し温度は立体水面温度以上(23.4℃)であっても、露点温度15℃に除湿されるので、大幅な省エネが明白である。A conventional air conditioner is designed to have a relative humidity of 60% when the indoor relative humidity is controlled at a room temperature of 25° C., so the relative humidity is 60%. Therefore, the enthalpy of the indoor air is (hb57) , the blowing air temperature is 15°C, the blowing enthalpy is (hc42.7) , and the enthalpy difference of the load of the air conditioner is 13.3.
The air conditioning load due to the three-dimensional water surface of the present invention is an indoor humidity of 30 ° C., an indoor relative humidity of 40%, an indoor enthalpy of (RM57.9) , and a blown air temperature of 23.4 and a relative humidity of 57%. However, since the blowing enthalpy is (RM52.0) , the enthalpy difference in this application is 5.9.
Compared with the conventional air conditioner, the enthalpy difference is 13.3, and the enthalpy difference due to the three-dimensional water surface of the present application is 5.9, resulting in an energy saving of 55.4%. The calculation is the air conditioning load (hb57) - (hc42.7) = 13.3 due to the three-dimensional water surface of the present invention in the conventional method,
Since the enthalpy difference between the air conditioning load due to the three-dimensional water surface of the present invention and the air conditioning load due to the three-dimensional water surface of the present invention is (RM57.9) - (RC52.0) = 5.9 ,
The consumption enthalpy difference is 44.6%, and the energy saving ratio is 55.4%. Even if the blowing temperature is above the water surface temperature (23.4°C), the dew point is dehumidified to 15°C. So significant energy savings are evident .
以下、本発明の実施形態を図1~図5を用いて説明する。
(図1)は本発明の実施形態に関る一般空調に関する温湿度制御の構成する概略的に示す図であり、本発明の立体水面の構造を示すものである。
1.水槽 2.不織布(立体水面) 3.水中ポンプ 4.送水管 5.プレート熱交換器
6.空調ファン 7.循環ファン 8.ヒートポンプ 等で構成する空調機である。
(図2)の冷房時はヒートポンプ8を冷房運転に選択し、ヒートポンプフィン6で室内空気冷房すると同時に、プレート熱交換器5にも冷媒を送り、水温を室内温度の湿球温度より低い温度以下に冷却水を不織布2の上部から流し、室内空気と接触させて除湿を行い、煖房時はヒートポンプ8を煖房運転に選択し、ヒートポンプフィン6で室内空気を煖を煖房すると同時に、プレート熱交換器5にも冷媒を送り、水温を室内空気の湿球温度より高い温度に加熱した水を不織布2の上部から流し、室内空気と接触させて加湿を行う空調機である。
(図3)は従来の技術の恒温恒湿である。水面が除加湿できることを説明するための参考図である。
1.水槽 4.冷却用ガス管 6.空調用フィン 12.循環ファン。
(図4)は従来のエアコンの空気湿り線図であり省エネを比較する為の参考図である。
(図5)は本発明の立体水面による空調を空気湿り線図で説明したものである。省エネを比較するための図である。An embodiment of the present invention will be described below with reference to FIGS. 1 to 5. FIG.
(FIG. 1) is a diagram schematically showing the configuration of temperature and humidity control for general air conditioning according to an embodiment of the present invention, showing the structure of a three-dimensional water surface of the present invention.
1.
During cooling (FIG. 2), the
(FIG. 3) is a conventional technology of constant temperature and humidity. It is a reference diagram for explaining that the water surface can be dehumidified.
1.
(Fig. 4) is an air moisture diagram of a conventional air conditioner and is a reference diagram for comparing energy saving.
FIG. 5 is an air moisture diagram illustrating air conditioning using a three-dimensional water surface according to the present invention. It is a figure for comparing energy saving.
空気湿り線図[図4]に関する
夏期において、外気温度が32℃で、相対湿度50%の時、従来の空調をして室内温度25℃で相対湿度60%の快適な快適環境に制御した場合の消費エネルギーを調べるにはエンタルピー差に風量を乗じる
空気のエンタルピーは空調機入口のエンタルピーは(hb 56.0)空調機出口のエンタルピーは(hc42.7)=エンタルピー差(12.3)×風量を乗じる。In the summer with respect to the air humidity diagram [Fig. 4], when the outside air temperature is 32°C and the relative humidity is 50%, conventional air conditioning is used to control the comfortable environment with the indoor temperature of 25°C and the relative humidity of 60%. The enthalpy of the air is the enthalpy at the air conditioner inlet (hb 56.0), and the enthalpy at the air conditioner outlet is (hc 42.7) = enthalpy difference (12.3) x air volume Multiply by
空気湿り線図[図5]に関する。
夏期において、外気温度が32℃で相対湿度50%RHの時、外気温度が32℃で相対湿度50%RHの時、本発明の立体体水面と付属した空調機で室内温度30℃で相対湿度40%の快適環境で制御した場合の消費エネルギーを調べるにはエンタルピーの差に風量を乗じる。
循環空気のエンタルピー(RM57.9)空調機出口温度のエンタルピー(RC52.0)であり、エンタルピー差(5.9)×風量となる。It relates to the air wetness diagram [Fig. 5].
In summer, when the outside temperature is 32°C and the relative humidity is 50% RH, when the outside temperature is 32°C and the relative humidity is 50% RH, the three-dimensional water surface of the present invention and the attached air conditioner are used at the indoor temperature of 30°C and the relative humidity. In order to investigate the energy consumption when controlling in a comfortable environment of 40%, the difference in enthalpy is multiplied by the air volume.
The enthalpy of the circulating air (RM57.9 ) is the enthalpy of the air conditioner outlet temperature (RC52.0), and the enthalpy difference (5.9) x air volume.
[図1]の符号
1.水槽 2.不織布(立体水面) 3.水中ポンプ 4.送水管
5.プレート熱交換器 6. ヒートポンプフィン 8.ヒートポンプ
[図2]の符号
1.水槽 2.不織布(立体水面) 4.送水管 9.不織布(立体水面)用の固定器具
[図3]の符号
1 水槽 10. 冷暖コイル 11.ヒーター 12.循環ファン
[図4]の符号
A.外気空気 M.室内空気 C.冷却器出口空気
hM.室内エンタルピー hC.冷却器出口エンタルピー
[図5]の符号
A.外気空気 M.室内空気 C.空調機出口空気
RM.室内エンタルピー RC.空調機出口エンタルピーSymbols in FIG. 1 1.
Symbol A. in FIG. Ambient air M.I. Indoor air C. Chiller outlet air hM. Room enthalpy hC. The cooler exit enthalpy [Fig. 5] is labeled A. Ambient air M.I. Indoor air C. air conditioner outlet air
RM. Room enthalpy RC. Air conditioner outlet enthalpy
Claims (1)
煖房時はヒートポンプ8を煖房運転に選択し、ヒートポンプフィン6で室内空気を煖房すると同時に、プレート熱交換器5にも冷媒を送り、水温を室内空気の湿球温度より高い温度以上に加熱した水を不織布2の上部から流し、室内空気と接触させて加湿を行う空調機。A three-dimensional water surface composed of a water tank 1, a nonwoven fabric 2, a submersible pump 3, a water pipe 4, and a plate heat exchanger 5, and is a device capable of continuously circulating water and dehumidifying, and the three-dimensional water surface is vertical. At the time of cooling, the heat pump 8 is selected for cooling operation, and the heat pump fins 6 cool the indoor air, and at the same time, the refrigerant is also sent to the plate heat exchanger 5 to reduce the water temperature to the humidity of the indoor temperature. Cooling water made to a temperature lower than the ball temperature is flowed from the upper part of the nonwoven fabric 2, and the nonwoven fabric 2 is brought into contact with the room air to dehumidify,
At the time of heating, the heat pump 8 is selected for heating operation, the indoor air is heated by the heat pump fins 6, and at the same time, the refrigerant is also sent to the plate heat exchanger 5 to raise the water temperature to a temperature higher than the wet bulb temperature of the indoor air. An air conditioner that humidifies by flowing heated water from above the nonwoven fabric 2 and bringing it into contact with room air.
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