JPH07145963A - Air conditioner - Google Patents

Air conditioner

Info

Publication number
JPH07145963A
JPH07145963A JP31736893A JP31736893A JPH07145963A JP H07145963 A JPH07145963 A JP H07145963A JP 31736893 A JP31736893 A JP 31736893A JP 31736893 A JP31736893 A JP 31736893A JP H07145963 A JPH07145963 A JP H07145963A
Authority
JP
Japan
Prior art keywords
air
reaction tank
room
discharged
zeolite reaction
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP31736893A
Other languages
Japanese (ja)
Other versions
JP3314998B2 (en
Inventor
Masayoshi Usui
正佳 臼井
Nonenman Manfuretsudo
マンフレッド.ノネンマン
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Usui Kokusai Sangyo Kaisha Ltd
Original Assignee
Usui Kokusai Sangyo Kaisha Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Usui Kokusai Sangyo Kaisha Ltd filed Critical Usui Kokusai Sangyo Kaisha Ltd
Priority to JP31736893A priority Critical patent/JP3314998B2/en
Publication of JPH07145963A publication Critical patent/JPH07145963A/en
Application granted granted Critical
Publication of JP3314998B2 publication Critical patent/JP3314998B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To simply manufacture a structure without using refrigerant, to reduce maintaining and operation costs and to eliminate an environmental contamination of refrigerant gas with low noise by providing a zeolite reaction tank for absorbing humidity of, heating and discharging introducing air. CONSTITUTION:At the time of cooling, the air of a room 1 is discharged from a discharge port 01, fed to a zeolite reaction tank 6 through switching valves 2a, 2b, a blower 5a and a partition valve 3, and low humidity, dry high temperature air is discharged from the tank 6. The air is supplied to a heat exchanger 7, heat exchanged with the air supplied to the exchanger 7 by a blower 5b to dry air at a relatively lower temperature, and supplied to a humidifier 8. Vaporization heat for vaporizing the water of the humidifier 8 is discharged, its temperature is further lowered, and air having a low temperature and suitable humidity is fed to the room 1 through a switching valve 2d. Air in the room 1 is discharged out of a discharge port 02 and heat exchanged with the air from the tank 6 by the exchanger 7, and fed.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は室内の空気状態を調整す
る空調装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an air conditioner for adjusting the air condition in a room.

【0002】[0002]

【従来の技術】室内の空気状態を調整する従来の空調装
置では、フロンなどの冷媒を圧縮するコンプレッサ、ガ
ス状の冷媒を凝縮して液状の冷媒にする凝縮器、液状の
冷媒を急激に膨張する膨張器、ガス状の冷媒を蒸発させ
る蒸発器を備えている。そして、冷房動作を行う場合に
は、コンプレッサで生成されたガス状の圧縮された冷媒
が、凝縮器で凝縮されて液体の冷媒となり、膨張器で急
激に膨張され、蒸発器で室内に流入される空気と熱交換
され、該空気から気化熱を奪って該空気の温度を低下さ
せ、温度が低下した空気が室内に流入される。また、暖
房動作を行う場合には、コンプレッサで生成されたガス
状の圧縮された冷媒が、凝縮器で室内に流入される空気
と熱交換され、該空気に凝縮熱を与えて該空気の温度が
上昇し、温度が上昇した空気が室内に流入される。
2. Description of the Related Art In a conventional air conditioner for adjusting the indoor air condition, a compressor for compressing a refrigerant such as CFC, a condenser for condensing a gaseous refrigerant into a liquid refrigerant, and a rapid expansion of the liquid refrigerant. And an evaporator that evaporates a gaseous refrigerant. When performing the cooling operation, the gaseous compressed refrigerant produced by the compressor is condensed by the condenser to become a liquid refrigerant, which is rapidly expanded by the expander and then flowed into the room by the evaporator. Is exchanged with the air to remove heat of vaporization from the air to lower the temperature of the air, and the air having the lowered temperature is flowed into the room. Further, when performing a heating operation, the gaseous compressed refrigerant generated by the compressor is heat-exchanged with the air flowing into the room by the condenser, and the heat of condensation is given to the air to give the temperature of the air. Rises, and the air whose temperature has risen flows into the room.

【0003】[0003]

【発明が解決しようとする課題】前述の従来の空調装置
では、コンプレッサ、凝縮器、膨張器及び蒸発器が必要
であり、また冷媒ガスの漏れを防止する密封構造が必要
で、構成が複雑となり製造コスト上で問題が生じると共
に、運転にかなりの電力が消費し、維持稼働コストの低
減も要望されている。また、コンプレッサの駆動に際し
ての騒音や振動が大きく、冷媒ガスの地球環境の汚染の
問題も抱えている。
The above-mentioned conventional air conditioner requires a compressor, a condenser, an expander and an evaporator, and a sealing structure for preventing refrigerant gas from leaking, resulting in a complicated structure. In addition to problems in manufacturing cost, considerable power consumption is required for operation, and maintenance and operation costs are required to be reduced. Further, noise and vibration are great when driving the compressor, and there is a problem of pollution of the refrigerant gas to the global environment.

【0004】本発明は、前述したような空調装置の現状
に鑑みてなされたものであり、その目的は、冷媒を使用
せず構造が簡単で製造コスト及び維持運転コストを低減
することができ、低騒音で冷媒ガスによる環境汚染もな
い空調装置を提供することにある。
The present invention has been made in view of the current state of the air conditioner as described above, and its purpose is to reduce the manufacturing cost and the maintenance operation cost without using a refrigerant, which has a simple structure. An object of the present invention is to provide an air conditioner that has low noise and is free from environmental pollution due to refrigerant gas.

【0005】[0005]

【課題を解決するための手段】前記目的を達成するため
に、本発明は、温度を含む室内の空気状態を調整する空
調装置において、流入する空気を吸湿加熱して放出する
ゼオライト反応槽と、該ゼオライト反応槽から放出され
る低湿高温の空気と、前記室内から放出される空気との
熱交換を行う熱交換器と、前記ゼオライト反応槽から放
出され、前記熱交換により温度が低下した低湿の空気が
流入され、該空気を低温の空気にする加湿装置と、冷房
動作時には、前記加湿装置から放出される空気を、暖房
動作時には、前記室内から放出され、前記熱交換により
温度が上昇した空気を、それぞれ選択して前記室内に流
入させる流入空気選択手段と、前記室内から放出される
空気を前記熱交換器に流入させる空気送出手段と、冷房
動作時には、前記室内から放出される空気を、暖房動作
時には、前記加湿装置から放出される空気を、それぞれ
選択して前記ゼオライト反応槽に流入させる返還選択手
段と、前記ゼオライト反応槽を加熱する再生手段とを有
する構成にしてある。
To achieve the above object, the present invention relates to an air conditioner for adjusting an indoor air condition including temperature, and a zeolite reaction tank for absorbing and heating inflowing air to release it. A low-humidity and high-temperature air discharged from the zeolite reaction tank, a heat exchanger for exchanging heat with the air discharged from the room, and a low-humidity air discharged from the zeolite reaction tank and having a temperature lowered by the heat exchange. A humidifying device into which air is introduced to turn the air into low temperature air, and air discharged from the humidifying device during a cooling operation, and air that is discharged from the room during a heating operation and whose temperature has risen due to the heat exchange. Inflow air selection means for selecting each of them to flow into the room, air delivery means for causing the air discharged from the room to flow into the heat exchanger, and during the cooling operation, And a return selecting unit for selecting the air discharged from the inside and the air discharged from the humidifying device to flow into the zeolite reaction tank during the heating operation, and a regeneration unit for heating the zeolite reaction tank. It is configured.

【0006】[0006]

【作用】冷房動作時には、返還選択手段によって、室内
から放出される空気が選択されてゼオライト反応槽に流
入させ、ゼオライト反応槽では流入する空気を吸湿加熱
して放出する。このようにして、ゼオライト反応槽から
放出される低湿高温の空気は、熱交換器において室内か
ら放出される空気或いは外気と熱交換され、温度が低下
した低湿の空気が得られる。この温度が低下した低湿の
空気は、加湿装置に流入されて適度な湿度を得ると共
に、気化熱を奪われて低温空気になり、この低温で適度
に低い湿度の空気が室内に流入され、室内の空気の温度
と湿度とが調整される。
In the cooling operation, the return selection means selects the air released from the room and causes it to flow into the zeolite reaction tank. The zeolite reaction tank absorbs and heats the inflowing air to release it. In this way, the low-humidity and high-temperature air discharged from the zeolite reaction tank is heat-exchanged with the air discharged from the room or the outside air in the heat exchanger, and the low-humidity air with the lowered temperature is obtained. The low-humidity air whose temperature has dropped is admitted to the humidifier to obtain an appropriate humidity, and at the same time, it is deprived of the heat of vaporization to become low-temperature air. The temperature and humidity of the air is adjusted.

【0007】一方、暖房動作時には、返還選択手段によ
って、加湿装置から放出される空気が選択されてゼオラ
イト反応槽に流入され、ゼオライト反応槽では流入する
空気を吸湿加熱して放出する。このようにして、ゼオラ
イト反応槽から放出される低湿高温の空気は、熱交換器
において室内から放出される空気と熱交換され、室内か
ら放出される空気は、その温度が上昇する。このように
して、温度が上昇した空気が室内に流入され、室内の空
気の温度が調整される。この場合、ゼオライト反応槽か
ら放出され、熱交換器での熱交換により温度が低下した
低湿の空気は、加湿装置に流入され気化熱を奪われて低
温空気になり、この低温で低湿度の空気が、前述のよう
に返還選択手段によってゼオライト反応槽に流入され
る。
On the other hand, during the heating operation, the return selection means selects the air discharged from the humidifying device to flow into the zeolite reaction tank, and the zeolite reaction tank absorbs and heats the inflowing air and discharges it. In this way, the low-humidity and high-temperature air discharged from the zeolite reaction tank is heat-exchanged with the air discharged from the room in the heat exchanger, and the temperature of the air discharged from the room rises. In this way, the air whose temperature has risen flows into the room, and the temperature of the air in the room is adjusted. In this case, the low-humidity air that is discharged from the zeolite reaction tank and whose temperature has decreased due to heat exchange in the heat exchanger flows into the humidifier and is deprived of the heat of vaporization to become low-temperature air. Are flowed into the zeolite reaction tank by the return selection means as described above.

【0008】また、ゼオライト反応槽が過吸湿状態にな
ると、再生手段によりゼオライト反応槽が加熱されその
再生動作が行われる。
When the zeolite reaction tank is in a state of excessive moisture absorption, the zeolite reaction tank is heated by the regenerating means and the regenerating operation is performed.

【0009】[0009]

【実施例】【Example】

[第1の実施例]以下、本発明の実施例を図1乃至図6
を参照して説明するが、先ず図1乃至図4を参照して第
1の実施例を説明する。ここで、図1は第1の実施例の
冷房動作を説明するブロック図、図2は第1の実施例の
暖房動作を説明するブロック図、図3はゼオライトの再
生動作を説明するブロック図、図4は第1の実施例の待
機状態を説明するブロック図である。
[First Embodiment] Hereinafter, an embodiment of the present invention will be described with reference to FIGS.
First, a first embodiment will be described with reference to FIGS. 1 to 4. Here, FIG. 1 is a block diagram illustrating a cooling operation of the first embodiment, FIG. 2 is a block diagram illustrating a heating operation of the first embodiment, and FIG. 3 is a block diagram illustrating a zeolite regeneration operation. FIG. 4 is a block diagram for explaining the standby state of the first embodiment.

【0010】図4に示すように、空気調整が行われる部
屋1には、空気が流入される流入口S1、S2と空気が
放出される放出口O1、O2とが設けてあり、流入口S
1は切換弁2dを介して加湿装置8の出力側に接続して
あり、流入口S2は切換弁2fを介して熱交換器7の第
2の出力側に接続してある。同様に、放出口O1は切換
弁2aを介して切換弁2bに接続してあり、切換弁2
a、2d間が互いに接続してある。切換弁2bにはブロ
ワ5aの入力側が接続してあり、ブロワ5aの出力側
は、仕切弁3を介して吸湿発熱動作を行うゼオライト反
応槽6の入力側に接続してあり、ゼオライト反応槽6に
は間接加熱を行う加熱装置10が設けてあり、ゼオライ
ト反応槽6の出力側には切換弁2cを介して熱交換器7
の第1の入力側が接続してある。そして、熱交換器7の
第2の入力側には、切換弁2eに接続されたブロワ5b
が接続してあり、熱交換器7の第1の出力側には加湿装
置8の入力側が接続してある。図4は部屋1の空気調整
を行う前の待機状態を示しており、この状態では仕切弁
3を閉成し、切換弁2cはゼオライト反応槽6側には閉
成し、熱交換器7の入力側を大気側に開成し、ゼオライ
ト反応槽6は乾燥状態を保っている。
As shown in FIG. 4, the room 1 in which air is adjusted is provided with inlets S1 and S2 into which air is introduced and outlets O1 and O2 from which air is released.
1 is connected to the output side of the humidifying device 8 via the switching valve 2d, and the inflow port S2 is connected to the second output side of the heat exchanger 7 via the switching valve 2f. Similarly, the discharge port O1 is connected to the switching valve 2b via the switching valve 2a.
A and 2d are connected to each other. The input side of the blower 5a is connected to the switching valve 2b, and the output side of the blower 5a is connected to the input side of the zeolite reaction tank 6 which performs a heat absorption and heat generation operation via the sluice valve 3, and the zeolite reaction tank 6 Is provided with a heating device 10 for performing indirect heating, and the output side of the zeolite reaction tank 6 is provided with a heat exchanger 7 via a switching valve 2c.
The first input side of is connected. The blower 5b connected to the switching valve 2e is provided on the second input side of the heat exchanger 7.
Is connected, and the input side of the humidifier 8 is connected to the first output side of the heat exchanger 7. FIG. 4 shows a standby state before performing air conditioning in the room 1. In this state, the sluice valve 3 is closed, the switching valve 2c is closed on the zeolite reaction tank 6 side, and the heat exchanger 7 The input side is opened to the atmosphere side, and the zeolite reaction tank 6 is kept dry.

【0011】次に、このような構成の第1の実施例の冷
房動作を説明する。
Next, the cooling operation of the first embodiment having such a structure will be described.

【0012】図4の状態から部屋1の冷房動作を行うに
は、図1に示すように、加熱装置10をOFFにし、仕
切弁3を開成し、切換弁2cを切り換えてゼオライト反
応槽6の出力側を熱交換器7の入力側に開成し、切換弁
2eを切り換えてブロワ5bの入力側を大気側に開成
し、切換弁2fを切り換えて熱交換器7の第2の出力側
を大気側に開成する。そして、切換弁2dを切り換えて
加湿装置8の出力側を流入口S1に開成し、切換弁2a
と切換弁2bを切り換えて、放出口O1をブロワ5aの
入力側に開成する。
In order to perform the cooling operation of the room 1 from the state shown in FIG. 4, as shown in FIG. 1, the heating device 10 is turned off, the sluice valve 3 is opened, and the switching valve 2c is switched to switch the zeolite reaction tank 6 The output side is opened to the input side of the heat exchanger 7, the switching valve 2e is switched to open the input side of the blower 5b to the atmosphere side, and the switching valve 2f is switched to open the second output side of the heat exchanger 7 to the atmosphere. Open to the side. Then, the switching valve 2d is switched to open the output side of the humidifying device 8 to the inlet S1, and the switching valve 2a is opened.
And the switching valve 2b is switched to open the discharge port O1 to the input side of the blower 5a.

【0013】このようにすると、部屋1の空気は放出口
O1から放出され、切換弁2a、2b、ブロワ5a、仕
切弁3を介してゼオライト反応槽6に流れ込み、ゼオラ
イト反応槽6内のゼオライトの吸湿作用によって乾操さ
れ、吸湿時のゼオライト反応槽6からの発熱によって、
ゼオライト反応槽6からは低湿度で乾燥し且つ温度の高
い空気が放出される。この、低湿度で乾燥し且つ温度の
高い空気は、熱交換器7の第1の入力側に供給されて、
ブロワ5bによって熱交換器7の第2の入力側から供給
される外気と熱交換され、熱交換器7の第1の出力側か
らは温度がやや低下した乾燥空気が放出される。この温
度がやや低下した乾燥空気は、加湿装置8に供給され、
加湿装置8の水を気化するための気化熱を放出してさら
に温度が低下し、低温度で適当な湿度を有する空気が切
換弁2dを介し、流入口S1から部屋1内に流入され、
部屋1の快適な冷房が行われる。
In this way, the air in the room 1 is discharged from the discharge port O1, flows into the zeolite reaction tank 6 through the switching valves 2a, 2b, the blower 5a, and the sluice valve 3 to remove the zeolite in the zeolite reaction tank 6. The zeolite reaction tank 6 is dry-processed by the moisture absorption action, and the heat generated from the zeolite reaction tank 6 during the moisture absorption causes
From the zeolite reaction tank 6, air that is dry at low humidity and has a high temperature is discharged. This low-humidity, dry and high-temperature air is supplied to the first input side of the heat exchanger 7,
The blower 5b exchanges heat with the outside air supplied from the second input side of the heat exchanger 7, and the first output side of the heat exchanger 7 releases dry air having a slightly lowered temperature. The dry air whose temperature is slightly lowered is supplied to the humidifier 8.
The heat of vaporization for vaporizing the water of the humidifying device 8 is released to further lower the temperature, and air having a low temperature and an appropriate humidity is introduced into the room 1 from the inlet S1 through the switching valve 2d,
Comfortable cooling of room 1 is performed.

【0014】次に、第1の実施例の暖房動作を説明す
る。
Next, the heating operation of the first embodiment will be described.

【0015】図4の状態から部屋1の暖房動作を行うに
は、図2に示すように、加熱装置10をOFFにし、仕
切弁3を開成し、切換弁2cを切り換えてゼオライト反
応槽6の出力側を熱交換器7の入力側に開成し、切換弁
2eを切り換えてブロワ5bの入力側を放出口O2側に
開成し、切換弁2fを切り換えて熱交換器7の第2の出
力側を流入口S2側に開成する。そして、切換弁2d、
2aを切り換えて加湿装置8の出力側を切換弁2d、2
a、2bを介してブロワ5aの入力側に開成する。
In order to perform the heating operation of the room 1 from the state of FIG. 4, as shown in FIG. 2, the heating device 10 is turned off, the sluice valve 3 is opened, and the switching valve 2c is switched to switch the zeolite reaction tank 6 from the state. The output side is opened to the input side of the heat exchanger 7, the switching valve 2e is switched to open the input side of the blower 5b to the discharge port O2 side, and the switching valve 2f is switched to the second output side of the heat exchanger 7. Is opened on the inlet S2 side. Then, the switching valve 2d,
2a to switch the output side of the humidifier 8 to the switching valves 2d, 2
Open to the input side of the blower 5a via a and 2b.

【0016】このようにすると、部屋1の空気は放出口
O2から放出され、切換器2e及びブロワ5bを介して
熱交換器7の第2の入力側に供給され、熱交換器7でゼ
オライト反応槽6の出力側から供給される乾燥した高温
度の空気と熱交換され、温度が上昇して熱交換器7の第
2の出力側から、切換器2fを介してこの温度が上昇し
た暖かい空気が流入口S2から部屋1内に流入され、部
屋1に程よい暖房が施される。一方、熱交換器7の第1
の出力側から放出される温度が低下した暖かく乾燥した
空気は、加湿装置8に供給されて、加湿装置8の水に気
化熱を与えて温度が低下すると共に、適度に加湿され、
切換弁2d、2a、2b、ブロワ5a及び仕切弁3を介
して再びゼオライト反応槽6に供給される。
In this way, the air in the room 1 is discharged from the discharge port O2, is supplied to the second input side of the heat exchanger 7 via the switch 2e and the blower 5b, and the zeolite reaction is carried out in the heat exchanger 7. Warm air that has been heat-exchanged with the dry high-temperature air supplied from the output side of the tank 6 and has risen in temperature from the second output side of the heat exchanger 7 via the switching device 2f. Is introduced into the room 1 through the inflow port S2, and the room 1 is appropriately heated. On the other hand, the first of the heat exchanger 7
The warm and dry air whose temperature is released from the output side of is supplied to the humidifying device 8 to give heat of vaporization to the water of the humidifying device 8 to lower the temperature, and to be appropriately humidified,
It is again supplied to the zeolite reaction tank 6 via the switching valves 2d, 2a, 2b, the blower 5a and the sluice valve 3.

【0017】そして、部屋1の冷房動作或いは暖房動作
が行われ、ゼオライト反応槽6の吸湿動作が継続され、
ゼオライト反応槽6が過度の吸湿状態になると、図3に
示すように、切換弁2bが大気側に開成され、仕切弁3
が開成されて切換弁2cが大気側に開成された状態に設
定される。そして、加熱装置10がONにされ、ゼオラ
イト反応槽6が間接的に加熱再生される。第1の実施例
では、ゼオライト反応槽6が一個設けられているが、ゼ
オライト反応槽6を複数設け、現在冷房動作或いは暖房
動作を行っていないゼオライト反応槽を再生動作し、現
在使用中のゼオライト反応槽6が過度の吸湿状態になっ
た場合に、再生動作を完了しているゼオライト反応槽に
切り換えて使用することも可能である。
Then, the cooling operation or the heating operation of the room 1 is performed, the moisture absorption operation of the zeolite reaction tank 6 is continued,
When the zeolite reaction tank 6 becomes excessively hygroscopic, the switching valve 2b is opened to the atmosphere side as shown in FIG.
Is opened and the switching valve 2c is set to the state of being opened to the atmosphere side. Then, the heating device 10 is turned on, and the zeolite reaction tank 6 is indirectly heated and regenerated. In the first embodiment, one zeolite reaction tank 6 is provided, but a plurality of zeolite reaction tanks 6 are provided to regenerate a zeolite reaction tank that is not currently being cooled or heated, and the zeolite currently in use When the reaction tank 6 becomes excessively hygroscopic, it is possible to switch to the zeolite reaction tank in which the regeneration operation has been completed and used.

【0018】このように、第1の実施例によると、冷媒
を使用しないために装置に高度の気密性が要求されず、
コストの高いコンプレッサ、凝縮器、膨張器、蒸発器が
不要であり、加湿装置8は水分が乾燥空気に自然に蒸発
するだけでよく、全体の構造が簡単になると共に、冷房
動作時及び暖房動作時には、ブロワ5a、5bの駆動と
切換弁2a〜2fの切換だけに電力を使用すればよいの
で、稼働コストを大幅に削減することが可能である。ま
た、コンプレッサがないので、コンプレッサ駆動時に発
生する振動、騒音公害が生じることがなく、装置廃棄時
等に冷媒の環境汚染の問題も発生しない空調装置が提供
される。第1の実施例は住宅、オフィス、クリーンルー
ム等の各方面で広く使用可能であるが、精密作業時や就
寝時に騒音のない快適な空調動作を行うことができる。
As described above, according to the first embodiment, since no refrigerant is used, the apparatus is not required to have a high degree of airtightness.
There is no need for costly compressors, condensers, expanders, and evaporators, and the humidifier 8 only needs to naturally evaporate water into dry air, which simplifies the overall structure and also during cooling and heating operations. Occasionally, electric power may be used only for driving the blowers 5a and 5b and switching the switching valves 2a to 2f, so that the operating cost can be significantly reduced. Further, since there is no compressor, there is provided no vibration or noise pollution that occurs when the compressor is driven, and an air conditioner that does not cause the problem of environmental pollution of the refrigerant when the device is discarded. The first embodiment can be widely used in various fields such as a house, an office, and a clean room, but it is possible to perform a comfortable air conditioning operation without noise during precision work or sleeping.

【0019】[第2の実施例]次に、本発明の第2の実
施例を図5及び図6を参照して説明する。ここで、図5
は第2の実施例の冷房動作を説明するブロック図、図6
は実施例の暖房動作を説明するブロック図である。
[Second Embodiment] Next, a second embodiment of the present invention will be described with reference to FIGS. Here, FIG.
6 is a block diagram for explaining the cooling operation of the second embodiment, FIG.
[Fig. 3] is a block diagram illustrating a heating operation of the embodiment.

【0020】この第2の実施例は、すでに説明した第1
の実施例に対して、熱交換器7と加湿装置8との間に、
新たに補助熱交換器12を挿入し、この補助熱交換器1
2の入力側に切換弁2aを接続し、補助熱交換器12の
出力側を切換弁2bに接続してあり、またゼオライト反
応槽6には直接加熱を行う加熱装置10が内設されてい
る。第2の実施例のその他の部分の構成は、すでに説明
した第1の実施例と同一である。
This second embodiment is based on the first embodiment already described.
For the embodiment of the above, between the heat exchanger 7 and the humidifying device 8,
The auxiliary heat exchanger 12 is newly inserted, and this auxiliary heat exchanger 1
The switching valve 2a is connected to the input side of 2, the output side of the auxiliary heat exchanger 12 is connected to the switching valve 2b, and the zeolite reaction tank 6 is internally provided with a heating device 10 for performing heating. . The configuration of the other parts of the second embodiment is the same as that of the first embodiment already described.

【0021】この第2の実施例では、冷房動作時には、
放出口O1から放出される空気は、補助熱交換器12で
熱交換器7の第1の出力側の空気とも熱交換されるの
で、熱交換の効率が向上し、加湿装置8からより低温度
の空気を流入口S1から部屋1内に流入することが可能
になる。また、暖房動作時には、補助熱交換器12にお
いて、熱交換器7の第1の出力側の空気を、加湿装置8
の出力の低温空気と熱交換することにより、ゼオライト
反応槽6の負荷を減少し、ゼオライト反応槽6の動作寿
命を延長することが可能になる。
In the second embodiment, during the cooling operation,
The air discharged from the discharge port O1 is also heat-exchanged with the air on the first output side of the heat exchanger 7 by the auxiliary heat exchanger 12, so that the efficiency of heat exchange is improved and the temperature of the humidifier 8 becomes lower. It becomes possible to flow the air of the above into the room 1 from the inflow port S1. Further, during the heating operation, in the auxiliary heat exchanger 12, the air on the first output side of the heat exchanger 7 is supplied to the humidifier 8
By exchanging heat with the low temperature air having the output of 1, the load on the zeolite reaction tank 6 can be reduced and the operating life of the zeolite reaction tank 6 can be extended.

【0022】また、各実施例において、ゼオライト反応
槽6の再生動作時に得られた水蒸気を凝縮水として回収
し、加湿装置8に戻すことも可能である。
In each embodiment, it is also possible to recover the steam obtained during the regenerating operation of the zeolite reaction tank 6 as condensed water and return it to the humidifier 8.

【0023】[0023]

【発明の効果】本発明によると、ゼオライト反応槽から
放出される低湿高温の空気が、熱交換器において室内か
ら放出される空気と熱交換され、さらに加湿装置8で気
化熱が奪われた低温空気とされ、一方、室内から放出さ
れる空気は前記熱交換で高温空気とされ、前記低温空気
により冷房動作が行われ、前記高温空気により暖房動作
が行われるので、冷媒を使用せず、コンプレッサ、凝縮
器、膨張器、蒸発器が不要となり、構造が簡単になり製
造コストが低減すると共に、冷房動作時及び暖房動作時
の電力消費が大幅に削減され、稼働コストが削減され、
コンプレッサからの騒音公害が生じることがなく、冷媒
の環境汚染の問題も発生しない空調装置が提供される。
According to the present invention, the low-humidity and high-temperature air discharged from the zeolite reaction tank is heat-exchanged with the air discharged from the room in the heat exchanger, and the heat of vaporization is removed by the humidifier 8 at low temperature. On the other hand, the air discharged from the room is turned into high temperature air by the heat exchange, the cooling operation is performed by the low temperature air, and the heating operation is performed by the high temperature air, so that the refrigerant is not used and the compressor is used. , No condenser, expander and evaporator are required, the structure is simple and the manufacturing cost is reduced, the power consumption during the cooling operation and the heating operation is significantly reduced, and the operating cost is reduced.
Provided is an air conditioner that does not cause noise pollution from a compressor and does not cause a problem of refrigerant environmental pollution.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の第1の実施例の冷房動作を説明するブ
ロック図である。
FIG. 1 is a block diagram illustrating a cooling operation according to a first embodiment of the present invention.

【図2】第1の実施例の暖房動作を説明するブロック図
である。
FIG. 2 is a block diagram illustrating a heating operation according to the first embodiment.

【図3】第1の実施例のゼオライトの再生動作を説明す
るブロック図である。
FIG. 3 is a block diagram illustrating a regenerating operation of the zeolite of the first embodiment.

【図4】第1の実施例の待機状態を説明するブロック図
である。
FIG. 4 is a block diagram illustrating a standby state of the first embodiment.

【図5】本発明の第2の実施例の冷房動作を説明するブ
ロック図である。
FIG. 5 is a block diagram illustrating a cooling operation according to a second embodiment of the present invention.

【図6】第2の実施例の暖房動作を説明するブロック図
である。
FIG. 6 is a block diagram illustrating a heating operation according to a second embodiment.

【符号の説明】[Explanation of symbols]

1 部屋 2a〜2f 切換弁 3 仕切弁 5a、5b ブロワ 6 ゼオライト反応槽 7 熱交換器 8 加湿装置 10 加熱装置 12 補助熱交換器 1 room 2a-2f switching valve 3 sluice valve 5a, 5b blower 6 zeolite reaction tank 7 heat exchanger 8 humidifier 10 heating device 12 auxiliary heat exchanger

─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成6年2月1日[Submission date] February 1, 1994

【手続補正1】[Procedure Amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0010[Correction target item name] 0010

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0010】図4に示すように、空気調整が行われる部
屋1には、空気が流入される流入口S1、S2と空気が
放出される放出口O1、O2とが設けてあり、流入口S
1は切換弁2dを介して加湿装置8の出力側に接続して
あり、流入口S2は切換弁2fを介して熱交換器7の第
2の出力側に接続してある。同様に、放出口O1は切換
弁2aを介して切換弁2bに接続してあり、切換弁2
a、2d間が互いに接続してある。切換弁2bにはブロ
ワ5aの入力側が接続してあり、ブロワ5aの出力側
は、仕切弁3を介して吸湿発熱動作を行うゼオライト反
応槽6の入力側に接続してあり、ゼオライト反応槽6に
は間接加熱を行う加熱装置10が設けてあり、ゼオライ
ト反応槽6の出力側には切換弁2cを介して熱交換器7
の第1の入力側が接続してある。そして、熱交換器7の
第2の入力側には、切換弁2eに接続されたブロワ5b
が接続してあり、熱交換器7の第1の出力側には加湿装
置8の入力側が接続してある。なお、ゼオライト反応槽
6に内装されるゼオライトは最大の多孔質開口と吸水性
を有するXタイプのゼオライトで球形のペレット又は棒
状体として使用することが好ましい。図4は部屋1の空
気調整を行う前の待機状態を示しており、この状態では
仕切弁3を閉成し、切換弁2cはゼオライト反応槽6側
には閉成し、熱交換器7の入力側を大気側に開成し、ゼ
オライト反応槽6は乾燥状態を保っている。
As shown in FIG. 4, the room 1 in which air is adjusted is provided with inlets S1 and S2 into which air is introduced and outlets O1 and O2 from which air is released.
1 is connected to the output side of the humidifying device 8 via the switching valve 2d, and the inflow port S2 is connected to the second output side of the heat exchanger 7 via the switching valve 2f. Similarly, the discharge port O1 is connected to the switching valve 2b via the switching valve 2a.
A and 2d are connected to each other. The input side of the blower 5a is connected to the switching valve 2b, and the output side of the blower 5a is connected to the input side of the zeolite reaction tank 6 that performs a heat absorption and heat generation operation via the sluice valve 3, and the zeolite reaction tank 6 Is provided with a heating device 10 for performing indirect heating. The output side of the zeolite reaction tank 6 is provided with a heat exchanger 7 via a switching valve 2c.
The first input side of is connected. The blower 5b connected to the switching valve 2e is provided on the second input side of the heat exchanger 7.
Is connected, and the input side of the humidifier 8 is connected to the first output side of the heat exchanger 7. The zeolite contained in the zeolite reaction tank 6 is an X type zeolite having the maximum porous opening and water absorption, and it is preferable to use it as a spherical pellet or rod-shaped body. FIG. 4 shows a standby state before performing air conditioning in the room 1. In this state, the sluice valve 3 is closed, the switching valve 2c is closed on the zeolite reaction tank 6 side, and the heat exchanger 7 The input side is opened to the atmosphere side, and the zeolite reaction tank 6 is kept dry.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 温度を含む室内の空気状態を調整する空
調装置において、 流入する空気を吸湿加熱して放出するゼオライト反応槽
と、 該ゼオライト反応槽から放出される低湿高温の空気と、
前記室内から放出される空気との熱交換を行う熱交換器
と、 前記ゼオライト反応槽から放出され、前記熱交換により
温度が低下した低湿の空気が流入され、該空気を低温の
空気にする加湿装置と、 冷房動作時には、前記加湿装置から放出される空気を、
暖房動作時には、前記室内から放出され、前記熱交換に
より温度が上昇した空気を、それぞれ選択して前記室内
に流入させる流入空気選択手段と、 前記室内から放出される空気を前記熱交換器に流入させ
る空気送出手段と、 冷房動作時には、前記室内から放出される空気を、暖房
動作時には、前記加湿装置から放出される空気を、それ
ぞれ選択して前記ゼオライト反応槽に流入させる返還選
択手段と、 前記ゼオライト反応槽を加熱する再生手段とを有するこ
とを特徴とする空調装置。
1. In an air conditioner for adjusting an indoor air condition including temperature, a zeolite reaction tank for absorbing and heating inflowing air to release it, and low-humidity and high-temperature air discharged from the zeolite reaction tank.
A heat exchanger that exchanges heat with the air discharged from the room, and low-humidity air that has been discharged from the zeolite reaction tank and whose temperature has decreased due to the heat exchange is introduced to humidify the air into low-temperature air. Device, the air discharged from the humidifier during cooling operation,
During the heating operation, the inflow air selection means for selecting the air released from the room and having the temperature raised by the heat exchange to flow into the room, and the air released from the room to the heat exchanger. An air delivery means for causing the air to be discharged from the room during the cooling operation, and a return selecting means for selecting the air discharged from the humidifying device during the heating operation to flow into the zeolite reaction tank, respectively. An air conditioner having a regenerating means for heating a zeolite reaction tank.
【請求項2】 前記熱交換器の後段に補助熱交換器がさ
らに設けてあり、前記返還選択手段が、前記室内から放
出される空気または前記加湿装置から放出される空気
を、前記補助熱交換器において、前記熱交換器の出力と
の間で熱交換して、前記ゼオライト反応槽に流入させる
ことを特徴とする請求項1記載の空調装置。
2. An auxiliary heat exchanger is further provided at a stage subsequent to the heat exchanger, and the return selection means transfers the air discharged from the room or the air discharged from the humidifying device to the auxiliary heat exchange. 2. The air conditioner according to claim 1, wherein heat is exchanged with the output of the heat exchanger in the vessel and the heat is allowed to flow into the zeolite reaction tank.
【請求項3】 前記ゼオライト反応槽を複数個設け、空
気調整動作に使用しないゼオライト反応槽に前記再生手
段により再生処理が施されることを特徴とする請求項1
または請求項2記載の空調装置。
3. The zeolite reaction tank is provided in a plurality, and the zeolite reaction tank not used for air conditioning operation is regenerated by the regenerating means.
Alternatively, the air conditioner according to claim 2.
【請求項4】 前記加湿装置が一定の水量を維持するよ
うに給水を行う給水手段をさらに有することを特徴とす
る請求項1乃至請求項3の何れかに記載の空調装置。
4. The air conditioner according to claim 1, further comprising water supply means for supplying water so that the humidifying device maintains a constant amount of water.
JP31736893A 1993-11-24 1993-11-24 Air conditioner Expired - Fee Related JP3314998B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31736893A JP3314998B2 (en) 1993-11-24 1993-11-24 Air conditioner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31736893A JP3314998B2 (en) 1993-11-24 1993-11-24 Air conditioner

Publications (2)

Publication Number Publication Date
JPH07145963A true JPH07145963A (en) 1995-06-06
JP3314998B2 JP3314998B2 (en) 2002-08-19

Family

ID=18087472

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31736893A Expired - Fee Related JP3314998B2 (en) 1993-11-24 1993-11-24 Air conditioner

Country Status (1)

Country Link
JP (1) JP3314998B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2155417A1 (en) * 1999-09-08 2001-05-01 Samsung Electronics Co Ltd Humidifier and air conditioner with humidifier

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2155417A1 (en) * 1999-09-08 2001-05-01 Samsung Electronics Co Ltd Humidifier and air conditioner with humidifier

Also Published As

Publication number Publication date
JP3314998B2 (en) 2002-08-19

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