JPH06154543A - Dehumidifier of steam-permeable membrane-type - Google Patents

Dehumidifier of steam-permeable membrane-type

Info

Publication number
JPH06154543A
JPH06154543A JP4308612A JP30861292A JPH06154543A JP H06154543 A JPH06154543 A JP H06154543A JP 4308612 A JP4308612 A JP 4308612A JP 30861292 A JP30861292 A JP 30861292A JP H06154543 A JPH06154543 A JP H06154543A
Authority
JP
Japan
Prior art keywords
moisture
tank
module
hygroscopic liquid
tube
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.)
Pending
Application number
JP4308612A
Other languages
Japanese (ja)
Inventor
Kazuyuki Iguchi
和幸 井口
Toshikazu Mitani
俊数 三谷
Kazuyoshi Takeuchi
一喜 竹内
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.)
Daikin Industries Ltd
Original Assignee
Daikin Industries 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 Daikin Industries Ltd filed Critical Daikin Industries Ltd
Priority to JP4308612A priority Critical patent/JPH06154543A/en
Publication of JPH06154543A publication Critical patent/JPH06154543A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
    • F24F3/12Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
    • F24F3/14Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
    • F24F3/1411Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant
    • F24F3/1417Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant with liquid hygroscopic desiccants
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
    • F24F3/12Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
    • F24F3/14Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
    • F24F2003/1435Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification comprising semi-permeable membrane

Abstract

PURPOSE:To provide a dehumidifier of steam-permeable type which is entirely simple and compact, and can be installed easily with space-saving and noise-free operation. CONSTITUTION:A moisture absorption/desorption module 31 which receives and supplies moisture between an internal hygroscopic liquid and an external ventilated air is provided in an air duct 1 with an inlet 1a connected to an interior and outlets 1b, 1c which communicate with the interior and an exterior by switching operation of a damper 2, through the steam permeable membrane of a tube 32. A hygroscopic liquid 36 in a tank 34 is allowed to circulate through tubular paths 38, 39 is equipped with a pump 37 installed in the moisture adsorption and desorption module 31. The circulating hygroscopic liquid is selectively heated or cooled by the Peltier effect of an electronic freezing element 3.

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、室内空気に含まれる水
分を除去する水蒸気透過膜式除湿装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water vapor permeable membrane type dehumidifier for removing water contained in indoor air.

【0002】[0002]

【従来の技術】従来、この種の除湿装置として、例えば
図4に示すようなものが知られている(特開昭64−5
6118号公報)。この除湿装置は、塩化リチウム(Li
Cl)水溶液などの吸湿液体が、これに接触する空気の相
対湿度を、その溶質濃度が高いほど、またその温度が低
いほど低い値に保つという原理を利用している。即ち、
この除湿装置は、室内Rに、主鎖や側鎖に水酸基等をも
つポリエステル系高分子等からなる水蒸気透過膜製の数
本のチューブ32を並列に配設してなる吸湿モジュール
31とファン33を設け、冷却用コイル35を備えたタ
ンク34内に蓄えたLiCl水溶液36を、ポンプ37に
より管路38および絞り弁40をもつ管路39を介して
上記吸湿モジュール31に循環させる。一方、室外に、
ファン42をもつ上記吸湿モジュールと同様の放湿モジ
ュール41とヒータ43を設け、上記管路39から絞り
弁44および熱交換器45を経て分流するLiCl水溶液
を、ポンプ46により管路47を経て上記ヒータ43と
放湿モジュール41に供給し、上記熱交換器45を貫通
する管路48を経てタンク34に戻すようにしている。
2. Description of the Related Art Conventionally, a dehumidifying device of this kind is known, for example, as shown in FIG. 4 (JP-A-64-5).
6118). This dehumidifier uses lithium chloride (Li
Cl) A hygroscopic liquid such as an aqueous solution keeps the relative humidity of air in contact with it at a lower value as the solute concentration is higher and the temperature is lower. That is,
In this dehumidifying device, in a room R, a moisture absorption module 31 and a fan 33 are provided in which several tubes 32 made of a water vapor permeable film made of a polyester polymer having a hydroxyl group or the like in a main chain or a side chain are arranged in parallel. Is provided, and the LiCl aqueous solution 36 stored in the tank 34 having the cooling coil 35 is circulated to the moisture absorption module 31 by the pump 37 via the conduit 38 and the conduit 39 having the throttle valve 40. On the other hand, outdoors
A moisture releasing module 41 similar to the moisture absorbing module having a fan 42 and a heater 43 are provided, and the LiCl aqueous solution branched from the pipe 39 through the throttle valve 44 and the heat exchanger 45 is pumped through the pipe 47 through the pipe 47. It is supplied to the heater 43 and the moisture releasing module 41, and is returned to the tank 34 via a pipe line 48 penetrating the heat exchanger 45.

【0003】そして、室内Rを除湿するには、冷却用コ
イル35で冷却されたタンク34内の高濃度のLiCl水
溶液36を、ポンプ37により室内の吸湿モジュール3
1に送り、ファン33で送られる室内空気に含まれる水
分を、水蒸気透過膜製のチューブ32の膜を透過させて
LiCl水溶液に吸収する。水分を吸収したLiCl水溶液
は、吸水に伴う潜熱で温められると共に低濃度になり、
管路39を経てタンク34に戻るが、その一部は、ポン
プ46により、絞り弁44から予熱用の熱交換器45を
通りヒータ43で加熱され、水蒸気圧を上げて室外の放
湿モジュール41に送られる。放湿モジュール41で
は、水蒸気透過膜内外の蒸気圧差により、LiCl水溶液
中の水分が、ファン42で送られる大気中に膜を透過し
て放出される。水分を放出したLiCl水溶液は、脱水に
伴う潜熱で温められるとともに高濃度になり、熱交換器
45で室内側からの低濃度のLiCl水溶液を温め、自身
は冷えてタンク34に戻る。
In order to dehumidify the room R, the high-concentration LiCl aqueous solution 36 in the tank 34 cooled by the cooling coil 35 is pumped into the room moisture absorption module 3
1, the water contained in the room air sent by the fan 33 is permeated through the membrane of the tube 32 made of a water vapor permeable membrane to be absorbed in the LiCl aqueous solution. The LiCl aqueous solution that has absorbed water is warmed by the latent heat associated with water absorption and becomes low in concentration,
Although it returns to the tank 34 via the pipe 39, a part of it is heated by the pump 43 from the throttle valve 44, the heat exchanger 45 for preheating, and the heater 43 to raise the water vapor pressure and to release the outdoor moisture releasing module 41. Sent to. In the moisture releasing module 41, due to the difference in vapor pressure between the inside and outside of the water vapor permeable membrane, the water contained in the LiCl aqueous solution permeates the membrane into the atmosphere sent by the fan 42 and is released. The released LiCl aqueous solution is warmed by latent heat accompanying dehydration and becomes high in concentration, and the heat exchanger 45 warms the low-concentration LiCl aqueous solution from the indoor side, and then returns to the tank 34 by cooling.

【0004】[0004]

【発明が解決しようとする課題】さて、上記従来の除湿
装置は、LiCl水溶液36を室内Rの吸湿に用いる際に
は、タンク34の冷却コイル35で冷却し、放湿モジュ
ール41での外気への放湿に用いる際は、ヒータ43で
加熱している。そして、冷却コイル35やヒータ43
は、特に明記されていないが、家庭用としては圧縮機に
より冷媒を循環させる冷凍回路の蒸発器や凝縮器である
のが普通である。ところが、除湿装置にこのような冷凍
回路を備えると、装置全体が大型化して据え付けに手間
がかかり、広い設置スペースが必要になるうえ、LiCl
水溶液を加熱,冷却するための圧縮機の運転音が大きい
ため、騒音の問題が生じる。
When the LiCl aqueous solution 36 is used for absorbing moisture in the room R, the conventional dehumidifying apparatus described above cools the cooling coil 35 of the tank 34 to the outside air in the moisture releasing module 41. When it is used for releasing moisture, it is heated by the heater 43. Then, the cooling coil 35 and the heater 43
Although not particularly specified, is usually an evaporator or a condenser of a refrigeration circuit in which a refrigerant is circulated by a compressor for household use. However, if such a refrigerating circuit is provided in the dehumidifier, the entire apparatus becomes large and the installation is troublesome, and a large installation space is required.
Since the operation noise of the compressor for heating and cooling the aqueous solution is loud, noise problems occur.

【0005】そこで、本発明の目的は、LiCl水溶液な
どの吸湿液体の加熱,冷却方法を工夫することによっ
て、簡素な構造で小型化が図れ、据え付けが容易で、設
置スペースが削減でき、しかも運転に伴う騒音をなくす
ことができる水蒸気透過膜式除湿装置を提供することに
ある。
Therefore, an object of the present invention is to devise a method of heating and cooling a hygroscopic liquid such as an aqueous solution of LiCl, which can be downsized with a simple structure, can be easily installed, can reduce the installation space, and can be operated. It is an object of the present invention to provide a water vapor permeable membrane type dehumidifier capable of eliminating noise caused by the above.

【0006】[0006]

【課題を解決するための手段】上記目的を達成する為、
本発明の第1の除湿装置は、図1に例示するように、吸
湿液体36を蓄えるタンク34と、入口1aが室内に接
続され、出口1b,1cが室内と室外に切換連通される通
風路1と、この通風路1に設けられ、水蒸気透過膜製の
チューブ32内の吸湿液体とチューブ32外の流通空気
との間で膜を介して水分の授受を行なう吸,放湿モジュ
ール31と、この吸,放湿モジュール31に上記タンク
34の吸湿液体36を循環させるように接続され、吸湿
液体36を圧送するポンプ37が介設された管路38,
39と、この管路38または上記タンク34に熱交換し
うるように設けられ、ペルチェ効果により吸湿液体を択
一的に加熱または冷却する電子冷凍素子3を備えること
を特徴とする。また、本発明の第2の除湿装置は、図2
の例示するように、吸湿液体36を蓄えるタンク34
と、室内Rに設けられ、水蒸気透過膜製のチューブ12
内の吸湿液体とチューブ12外の室内空気との間で膜を
介して水分の授受を行なう吸湿モジュール11と、室外
に設けられ、水蒸気透過膜製のチューブ22内の吸湿液
体とチューブ22外の室外空気との間で膜を介して水分
の授受を行なう放湿モジュール21と、上記吸湿モジュ
ール11および放湿モジュール21に上記タンク34の
吸湿液体36を循環させるように接続され、吸湿液体3
6を圧送するポンプ37と吸湿液体の循環方向を切り換
える切換弁7が介設された管路8,9,10,19,20
と、この管路または上記タンク34に熱交換しうるよう
に設けられ、ペルチェ効果により吸湿液体36を択一的
に加熱または冷却する電子冷凍素子3を備えることを特
徴とする。
[Means for Solving the Problems] To achieve the above object,
As shown in FIG. 1, the first dehumidifying device of the present invention has a tank 34 for storing a hygroscopic liquid 36, an inlet 1a connected indoors, and outlets 1b, 1c for switching between indoor and outdoor ventilation passages. 1 and an absorption / desorption module 31 provided in the ventilation passage 1 for exchanging moisture between the hygroscopic liquid in the tube 32 made of a water vapor permeable membrane and the circulating air outside the tube 32 through the membrane. A pipe line 38 connected to the moisture absorption / desorption module 31 so as to circulate the moisture absorption liquid 36 in the tank 34 and provided with a pump 37 for pumping the moisture absorption liquid 36,
39 and an electronic refrigeration element 3 which is provided so as to be able to exchange heat with the pipe 38 or the tank 34 and selectively heats or cools the hygroscopic liquid by the Peltier effect. The second dehumidifying device of the present invention is shown in FIG.
As illustrated, the tank 34 that stores the hygroscopic liquid 36
And a tube 12 made of a water vapor permeable membrane provided in the room R
The moisture absorbing module 11 that exchanges moisture between the moisture absorbing liquid inside and the room air outside the tube 12 via a membrane, and the moisture absorbing liquid inside the tube 22 made of a water vapor permeable membrane and provided outside the tube and outside the tube 22. A moisture releasing module 21 that exchanges moisture with the outdoor air through a membrane, and the moisture absorbing module 11 and the moisture releasing module 21 are connected so as to circulate the moisture absorbing liquid 36 in the tank 34, and the moisture absorbing liquid 3
The pipes 8, 9, 10, 19, 20 provided with a pump 37 for feeding 6 under pressure and a switching valve 7 for switching the circulating direction of the hygroscopic liquid.
And an electronic refrigerating element 3 which is provided so as to be able to exchange heat with this pipe or the tank 34 and selectively heats or cools the hygroscopic liquid 36 by the Peltier effect.

【0007】[0007]

【作用】請求項1に記載の除湿装置において、室内を除
湿する場合、電子冷却素子3にこの素子が吸熱する方向
に電流を流し、入口1aが室内に連なる通風路1の出口
1bを室内側に切換連通し、ポンプ37を起動する。す
ると、タンク34内の高濃度の吸湿液体36は、タンク
34または管路38に設けられた上記電子冷凍素子3の
ペルチェ効果による吸熱で冷却されつつ、ポンプ37に
より上記通風路1内の吸,放湿モジュール31に送られ
る。吸,放湿モジュール31のチューブ32内に送られ
た吸湿液体は、蒸気圧差によりチューブ32の水蒸気透
過膜を経て、外部の通風路1を流れる室内空気に含まれ
る水分を吸収し、水分を奪われた空気は再び室内に戻さ
れて室内が除湿される。一方、水分を吸収した吸湿液体
は吸水に伴う潜熱で少し温められるとともに少し低濃度
になって、タンク34に戻る。この吸湿液体36の循環
による吸湿動作は、吸湿液体の吸水能が飽和するまで続
けられる。一方、室外に放湿する場合、電子冷凍素子3
に上述と逆の発熱する方向に電流を流し、通風路1の出
口1cを室外側に切換連通し、ポンプ37を起動する。
すると、吸水で低濃度となったタンク34内の吸湿液体
36は、電子冷凍素子3のペルチェ効果による発熱で加
熱されつつ、ポンプ37により通風路1内の吸,放湿モ
ジュール31に送られる。吸,放湿モジュール31のチ
ューブ32内に送られた吸湿液体は、水蒸気透過膜内外
の蒸気圧差により、内部の水分が膜を透過して通風路1
を流れる室内空気に放出され、水分を与えられた空気
は、通風路1の出口1cから室外へ排気される。一方、
水分を放出した吸湿液体は、脱水に伴う潜熱で少し温め
られるとともに高濃度になって、タンク34に戻る。こ
の吸湿液体36の循環による放湿動作は、吸湿液体の吸
水能が回復するまで続けられる。
In the dehumidifying apparatus according to claim 1, when dehumidifying the room, an electric current is passed through the electronic cooling element 3 in a direction in which the element absorbs heat, and the outlet 1b of the ventilation passage 1 having the inlet 1a connected to the inside of the room is placed on the indoor side. Then, the pump 37 is started. Then, the high-concentration hygroscopic liquid 36 in the tank 34 is cooled by the heat absorption by the Peltier effect of the electronic refrigeration element 3 provided in the tank 34 or the conduit 38, while the pump 37 absorbs the air in the ventilation passage 1. It is sent to the moisture releasing module 31. The hygroscopic liquid sent into the tube 32 of the moisture absorption / desorption module 31 passes through the water vapor permeable membrane of the tube 32 due to the difference in vapor pressure, absorbs moisture contained in the indoor air flowing through the external ventilation passage 1 and absorbs moisture. The released air is returned to the room again to dehumidify the room. On the other hand, the hygroscopic liquid that has absorbed the water is slightly warmed by the latent heat accompanying the water absorption and becomes slightly low in concentration, and then returns to the tank 34. The moisture absorption operation by the circulation of the moisture absorption liquid 36 is continued until the water absorption capacity of the moisture absorption liquid is saturated. On the other hand, when releasing moisture to the outside, the electronic refrigeration element 3
A current is passed in the direction of heat generation opposite to the above, the outlet 1c of the ventilation passage 1 is switched and communicated with the outdoor side, and the pump 37 is started.
Then, the hygroscopic liquid 36 in the tank 34, which has a low concentration due to water absorption, is heated by the heat generated by the Peltier effect of the electronic refrigerating element 3 and is sent by the pump 37 to the hygroscopic module 31 in the air passage 1. The moisture absorbing liquid sent into the tube 32 of the moisture absorbing / desorbing module 31 has a moisture pressure inside and outside the water vapor permeable membrane, so that moisture inside the membrane permeates the membrane and the ventilation passage 1
The air that has been discharged into the room air flowing through and is given moisture is discharged from the outlet 1c of the ventilation path 1 to the outside of the room. on the other hand,
The hygroscopic liquid that has released the water is slightly warmed by latent heat accompanying dehydration and becomes high in concentration, and then returns to the tank 34. The moisture releasing operation by circulating the hygroscopic liquid 36 is continued until the water absorbing ability of the hygroscopic liquid is restored.

【0008】請求項2に記載の除湿装置において、室内
Rを除湿する場合、電子冷凍素子3に吸熱する方向に電
流を流し、切換弁7を室内Rの吸湿モジュール11側に
切り換えてポンプ37を起動する。すると、タンク34
内の高濃度の吸湿液体36は、タンク34又は管路に設
けられた上記電子冷凍素子3のペルチェ効果による吸熱
で冷却されつつ、ポンプ37により室内Rの吸湿モジュ
ール11に送られる。吸湿モジュール11のチューブ1
2内に送られた吸湿液体は、蒸気圧差によりチューブ1
2の水蒸気透過膜を経て、外部を流れる室内空気に含ま
れる水分を吸収し、室内が除湿される。一方、水分を吸
収した吸湿液体は吸水に伴う潜熱で少し温められるとと
もに少し低濃度になって、タンク34に戻る。この吸湿
液体36の循環による吸湿動作は、吸湿液体の吸水能が
飽和するまで続けられる。一方、室外に放湿する場合、
電子冷凍素子3に発熱する方向に電流を流し、切換弁7
を室外の放湿モジュール21側に切り換えてポンプ37
を起動する。すると、吸水で低濃度となったタンク34
内の吸湿液体36は、電子冷凍素子3のペルチェ効果に
よる発熱で加熱されつつ、ポンプ37により室外の放湿
モジュール21に送られる。放湿モジュール21のチュ
ーブ22内に送られた吸湿液体は、水蒸気透過膜内外の
蒸気圧差により、内部の水分が膜を透過して屋外を流れ
る大気に放出される。一方、水分を放出した吸湿液体
は、脱水に伴う潜熱で少し温められるとともに高濃度に
なって、タンク34に戻る。この吸湿液体36の循環に
よる放湿動作は、吸湿液体の吸水能が回復するまで続け
られる。
In the dehumidifying apparatus according to claim 2, when dehumidifying the room R, an electric current is passed in a direction in which the electronic refrigeration element 3 absorbs heat, and the switching valve 7 is switched to the moisture absorption module 11 side of the room R to turn the pump 37 on. to start. Then, the tank 34
The highly concentrated hygroscopic liquid 36 therein is sent to the hygroscopic module 11 in the room R by the pump 37 while being cooled by the heat absorption by the Peltier effect of the electronic refrigeration element 3 provided in the tank 34 or the pipe line. Tube 1 of moisture absorption module 11
The hygroscopic liquid sent to the inside of the tube 2 is transferred to the tube 1 due to the difference in vapor pressure.
The water contained in the indoor air flowing outside is absorbed through the water vapor permeable membrane 2 to dehumidify the room. On the other hand, the hygroscopic liquid that has absorbed the water is slightly warmed by the latent heat accompanying the water absorption and becomes slightly low in concentration, and then returns to the tank 34. The moisture absorption operation by the circulation of the moisture absorption liquid 36 is continued until the water absorption capacity of the moisture absorption liquid is saturated. On the other hand, when releasing moisture to the outside,
An electric current is applied to the electronic refrigeration element 3 in the direction of heat generation, and the switching valve 7
Is switched to the outdoor moisture release module 21 side and the pump 37
To start. Then, the tank 34 that became low concentration due to water absorption
The hygroscopic liquid 36 inside is heated by the heat generated by the Peltier effect of the electronic refrigeration element 3 and is sent to the outdoor moisture releasing module 21 by the pump 37. The hygroscopic liquid sent into the tube 22 of the moisture releasing module 21 is released to the atmosphere flowing through the moisture inside the membrane through the membrane due to the difference in vapor pressure between the inside and the outside of the water vapor permeable membrane. On the other hand, the hygroscopic liquid that has released water is slightly warmed by latent heat accompanying dehydration and becomes high in concentration, and then returns to the tank 34. The moisture releasing operation by circulating the hygroscopic liquid 36 is continued until the water absorbing ability of the hygroscopic liquid is restored.

【0009】[0009]

【実施例】以下、本発明を図示の実施例により詳細に説
明する。図1は、請求項1に記載の水蒸気透過膜式除湿
装置の一例を示す回路図であり、図4で述べた部材と同
じ部材には同一番号を付している。この除湿装置は、吸
湿液体としてのLiCl水溶液36を蓄えるタンク34
と、入口1aが図示しないダクトで室内に接続され、出
口1b,1cがダンパ2の開閉により図示しないダクトを
経て室内と室外とに切換連通される通風路1と、この通
風路1に設けられ、水蒸気透過膜製のチューブ32内の
LiCl水溶液とチューブ外の流通空気との間で水分の授
受を行なう吸,放湿モジュール31と、この吸,放湿モジ
ュール31に入口1a側から風を送るファン33を備え
る。また、吸,放湿モジュール31の両端に、ポンプ3
7を介設した管路38と管路39とを夫々接続して、タ
ンク34のLiCl水溶液36を吸,放湿モジュール31
に循環させると共に、ペルチェ効果によりLiCl水溶液
を択一的に加熱または冷却する電子冷凍素子3を、上記
管路38と熱交換しうるように設けている。
The present invention will be described in detail below with reference to the embodiments shown in the drawings. FIG. 1 is a circuit diagram showing an example of the water vapor permeable membrane type dehumidifier according to claim 1, and the same members as the members described in FIG. 4 are denoted by the same reference numerals. This dehumidifying device has a tank 34 for storing a LiCl aqueous solution 36 as a hygroscopic liquid.
The inlet 1a is connected to the room by a duct (not shown), and the outlets 1b, 1c are provided to the air passage 1 and the ventilation passage 1 which is switched by the opening / closing of the damper 2 to communicate indoors and outdoors through the duct (not shown). , A moisture absorption / desorption module 31 for exchanging moisture between the LiCl aqueous solution in the water vapor permeable membrane tube 32 and the circulating air outside the tube, and the air is sent from the inlet 1a side to the moisture absorption / desorption module 31. A fan 33 is provided. In addition, the pump 3 is provided at both ends of the absorption and desorption module 31.
7 are connected to each other to connect a pipe line 39 and a pipe line 39, respectively, to absorb and dehumidify the LiCl aqueous solution 36 in the tank 34.
An electronic refrigerating element 3 is provided so that it can be heat-exchanged with the above-mentioned pipe line 38 while being circulated in the above manner and selectively heating or cooling the LiCl aqueous solution by the Peltier effect.

【0010】上記電子冷凍素子3は、放熱板4a,4bを
固着した両面が発熱面,吸熱面になっており、図示の位
置にあるスイッチ5を介して直流電源6に正方向に接続
されると、LiCl水溶液の管路38に接する放熱板4a
側の片面が吸熱し,他の片面が発熱する一方、スイッチ
5の矢印方向への切り換えで直流電源6に逆方向に接続
されると、放熱板4a側の片面が発熱し、他の片面が吸
熱するようになっている。そして、放熱板4aが吸熱し
て管路38を流れるLiCl水溶液を冷却する吸湿運転時
には、ダンパ2が図示の位置にあって通風路の一方の出
口1bを室内に連通し、放熱板4aが発熱してLiCl水溶
液を加熱する放湿運転時には、ダンパ2が矢印方向に切
り換えられて他方の出口1aを室外に連通するととも
に、いずれの場合も、ファン33が運転されて室内の空
気を矢印の如く入口1aから吸い込む。
Both sides of the electronic refrigeration element 3 to which the heat radiating plates 4a and 4b are fixed serve as a heat generating surface and a heat absorbing surface, and are connected in the forward direction to the DC power source 6 via the switch 5 at the position shown in the figure. And a heat radiating plate 4a in contact with the pipeline 38 for the LiCl aqueous solution.
While one side on one side absorbs heat and the other side generates heat, when the switch 5 is switched in the direction of the arrow and connected in the reverse direction to the DC power source 6, one side on the heat sink 4a side generates heat and the other side changes. It is designed to absorb heat. During the moisture absorption operation in which the heat radiating plate 4a absorbs heat and cools the LiCl aqueous solution flowing in the pipe 38, the damper 2 is located at the position shown in the figure and one outlet 1b of the ventilation path communicates with the inside of the room, and the heat radiating plate 4a generates heat. During the dehumidifying operation for heating the LiCl aqueous solution, the damper 2 is switched in the direction of the arrow to communicate the other outlet 1a to the outside of the room, and in any case, the fan 33 is operated to move the air in the room as shown by the arrow. Inhale through the entrance 1a.

【0011】上記構成の水蒸気透過膜式除湿装置は、次
のように動作する。室内を除湿する場合、スイッチ5を
図1に示す位置にして直流電源6から電子冷凍素子3に
正方向に電流を流し、通風路1のダンパ2を図示の位置
にして出口1bを室内に連通させるとともにファン33
を駆動し、ポンプ37を起動する。すると、タンク34
内の高濃度のLiCl水溶液36は、ポンプ37により管
路38を送られながら、ペルチェ効果で吸熱する電子冷
凍素子3の片面に放熱板4aを介して接触して、冷却さ
れて通風路1内の吸,放湿モジュール31に達する。吸,
放湿モジュール31のチューブ内に入った低温で高濃度
のLiCl水溶液は、蒸気圧差によりチューブをなす水蒸
気透過膜を経て、ファン33によって通風路1を流され
る室内空気に含まれる水分を吸収し、水分を奪われた空
気は、出口1bから再び室内に戻されて室内が除湿され
る。一方、水分を吸収したLiCl水溶液は、吸水に伴う
潜熱で少し温められるとともに少し低濃度になって、タ
ンク34に戻る。このLiCl水溶液36の循環による吸
湿動作は、LiCl水溶液の吸水能が飽和するまで続けら
れる。なお、この吸湿動作は、室内を除湿する必要が高
い梅雨期や夏期の昼間などに行なわれる。
The water vapor permeable membrane type dehumidifier having the above structure operates as follows. When dehumidifying the room, the switch 5 is moved to the position shown in FIG. 1 so that a current flows from the DC power source 6 to the electronic refrigeration element 3 in the positive direction, the damper 2 of the ventilation passage 1 is moved to the position shown in the drawing, and the outlet 1b is communicated with the room. Let and fan 33
To drive the pump 37. Then, the tank 34
The high-concentration LiCl aqueous solution 36 in the inside comes into contact with one side of the electronic refrigeration element 3 which absorbs heat by the Peltier effect via the heat radiating plate 4a while being sent through the pipe 38 by the pump 37, and is cooled and then in the ventilation passage 1 It reaches the absorption and desorption module 31 of. Sucking,
The low-temperature, high-concentration LiCl aqueous solution that has entered the tube of the moisture releasing module 31 absorbs the water contained in the indoor air that is made to flow through the ventilation passage 1 by the fan 33 through the water vapor permeable membrane that forms the tube due to the difference in vapor pressure. The air deprived of water is returned to the room through the outlet 1b to dehumidify the room. On the other hand, the LiCl aqueous solution that has absorbed water is slightly warmed by the latent heat associated with water absorption and becomes slightly low in concentration, and then returns to the tank 34. The moisture absorption operation by circulating the LiCl aqueous solution 36 is continued until the water absorption capacity of the LiCl aqueous solution is saturated. The moisture absorption operation is performed during the rainy season or summer daytime when it is highly necessary to dehumidify the room.

【0012】一方、吸水能が飽和したLiCl水溶液から
脱水する場合、スイッチ5を矢印方向に切り換えて電子
冷凍素子3に逆方向の電流を流し、通風路1のダンパ2
を矢印方向に切り換えて出口1cを室外に連通させると
ともにファン33を駆動し、ポンプ37を起動する。す
ると、吸水で低濃度となったタンク34内のLiCl水溶
液36は、ポンプ37により管路38を送られながら、
ペルチェ効果で発熱する電子冷凍素子3の片面に放熱板
4aを介して接触して、加熱されて通風路1内の吸,放湿
モジュール31に達する。吸,放湿モジュール31のチ
ューブ内に入った高温で低濃度のLiCl水溶液は、水蒸
気透過膜内外の蒸気圧差により、内部の水分が膜を透過
して通風路1を流れる室内空気に放出され、水分を与え
られた空気は、通風路の出口1cから室外へ排出され
る。一方、水分を放出したLiCl水溶液は、脱水に伴う
潜熱で少し温められるとともに高濃度になって、タンク
34に戻る。このLiCl水溶液36の循環による放湿動
作は、LiCl水溶液の吸水能が回復するまで続けられ
る。なお、この放湿動作は、室内を除湿する必要の少な
い梅雨期や夏期の夜間などに行なわれる。
On the other hand, when dehydrating the LiCl aqueous solution having saturated water absorption capacity, the switch 5 is switched in the direction of the arrow so that the electric current flows in the opposite direction to the electronic refrigeration element 3 and the damper 2 in the ventilation passage 1 is rotated.
Is switched to the direction of the arrow to communicate the outlet 1c with the outside of the room, the fan 33 is driven, and the pump 37 is started. Then, the LiCl aqueous solution 36 in the tank 34, which has become low in concentration due to water absorption, is sent through the pipe 38 by the pump 37,
It contacts one surface of the electronic refrigeration element 3 which generates heat due to the Peltier effect via the heat radiating plate 4a, and is heated to reach the absorption and desorption module 31 in the ventilation passage 1. The high-temperature, low-concentration LiCl aqueous solution that has entered the tube of the moisture absorption / desorption module 31 is released into the indoor air flowing through the ventilation passage 1 due to the internal moisture permeating through the membrane due to the vapor pressure difference between the inside and outside of the water vapor permeable membrane. The air to which moisture has been added is discharged to the outside from the outlet 1c of the ventilation passage. On the other hand, the LiCl aqueous solution from which water has been released is slightly warmed by latent heat accompanying dehydration and becomes high in concentration, and then returns to the tank 34. The moisture releasing operation by circulating the LiCl aqueous solution 36 is continued until the water absorbing ability of the LiCl aqueous solution is restored. It should be noted that this moisture releasing operation is performed during the rainy season or the summer night when it is not necessary to dehumidify the room.

【0013】図2は、請求項2に記載の水蒸気透過膜式
除湿装置の一例を示す回路図である。この除湿装置は、
水蒸気透過膜製の数本のチューブ12または22を並列
に配設した図1で述べた吸,放湿モジュール31と同じ
構造の吸湿モジュール11をファン13と共に室内R
に、放湿モジュール21をファン23と共に室外に夫々
設けた点を除いて、図1で述べた除湿装置と略同じ構成
であり、同じ部材には同一番号を付して説明を省略す
る。ポンプ37が介設されてタンク内のLiCl水溶液3
6に浸される管路8の先端には、循環方向を管路9また
は19を経て吸湿モジュール11または放湿モジュール
21のいずれかに切り換える三方弁7が設けられ、両モ
ジュール11,21とタンク34は、管路10,20で夫
々接続されている。この実施例の電子冷凍素子3は、放
熱板4aのない片面が金属製のタンク34と直接接触し
ていて、LiCl水溶液36を吸熱,放熱により冷却,加熱
するようになっている。
FIG. 2 is a circuit diagram showing an example of the water vapor permeable membrane type dehumidifier according to the second aspect. This dehumidifier is
A moisture absorbing module 11 having the same structure as the moisture absorbing and desorbing module 31 described in FIG. 1 in which several tubes 12 or 22 made of a water vapor permeable film are arranged in parallel is installed in a room R together with a fan 13.
In addition, the dehumidifying module 21 has substantially the same configuration as that of the dehumidifying device described in FIG. 1 except that the dehumidifying module 21 and the fan 23 are provided outside the room. An aqueous solution of LiCl 3 in the tank with a pump 37 installed
A three-way valve 7 for switching the circulation direction to either the moisture absorption module 11 or the moisture desorption module 21 via the conduits 9 or 19 is provided at the tip of the conduit 8 immersed in 6. 34 are connected to each other by pipelines 10 and 20, respectively. The electronic refrigerating element 3 of this embodiment has one side without the heat radiating plate 4a in direct contact with the metal tank 34, and is adapted to cool and heat the LiCl aqueous solution 36 by absorbing heat and radiating heat.

【0014】この除湿装置の動作は、次のとおりであ
る。室内Rを除湿する場合、スイッチ5を図2に示す位
置にして直流電源6から電子冷凍素子3に正方向に電流
を流し、三方弁7を図示の位置にするとともにファン1
3を駆動し、ポンプ37を起動する。すると、ペルチェ
効果で吸熱する電子冷凍素子3により冷却されるタンク
34内の高濃度のLiCl水溶液36は、管路9から室内
Rの吸湿モジュール11に送られる。吸湿モジュール1
1のチューブ12内に入った低温で高濃度のLiCl水溶
液は、蒸気圧差により水蒸気透過膜を経て、外部を流れ
る室内空気から水分を吸収し、水分を奪われた空気は室
内Rに戻って室内が除湿される。一方、水分を吸収した
LiCl水溶液は、吸水に伴う潜熱で少し温められ少し低
濃度になって、タンク34に戻り、この吸湿動作は、梅
雨期等の昼間などにLiCl水溶液36の吸水能が飽和す
るまで続けられる。
The operation of this dehumidifying device is as follows. When dehumidifying the room R, the switch 5 is set to the position shown in FIG. 2, a current is passed from the DC power source 6 to the electronic refrigeration element 3 in the positive direction, the three-way valve 7 is set to the position shown, and the fan 1
3 is driven and the pump 37 is started. Then, the high-concentration LiCl aqueous solution 36 in the tank 34, which is cooled by the electronic refrigeration element 3 that absorbs heat by the Peltier effect, is sent from the conduit 9 to the moisture absorption module 11 in the room R. Moisture absorption module 1
The low-temperature, high-concentration LiCl aqueous solution that has entered the tube 12 of No. 1 absorbs moisture from the indoor air flowing outside through the water vapor permeable membrane due to the difference in vapor pressure, and the deprived air returns to the indoor room R and returns to the indoor room. Is dehumidified. On the other hand, the LiCl aqueous solution that has absorbed water is warmed a little by the latent heat associated with the water absorption and becomes a little low concentration, and then returns to the tank 34. This moisture absorption operation causes the water absorption capacity of the LiCl aqueous solution 36 to be saturated during the daytime such as the rainy season. You can continue until you do.

【0015】一方、吸水能が飽和したLiCl水溶液から
脱水する場合、スイッチ5を矢印方向に切り換えて電子
冷凍素子3に逆方向に電流を流し、三方弁7を図中の破
線の流路に切り換えるとともにファン23を駆動し、ポ
ンプ37を起動する。すると、ペルチェ効果で発熱する
電子冷凍素子3により加熱されるタンク34内の低濃度
のLiCl水溶液36は、管路19から室外の放湿モジュ
ール21に送られる。放湿モジュール21のチューブ2
2内に入った高温で低濃度のLiCl水溶液は、水蒸気透
過膜内外の蒸気圧差により、内部の水分が膜を透過して
屋外をファン23により流れる大気に放出される。一
方、水分を放出したLiCl水溶液は、脱水に伴う潜熱で
少し冷やされ少し高濃度になって、タンク34に戻り、
この放湿動作は、梅雨期等の夜間などにLiCl水溶液3
6の吸水能が回復するまで続けられる。
On the other hand, when dehydrating the LiCl aqueous solution having saturated water absorption capacity, the switch 5 is switched in the direction of the arrow to flow a current in the opposite direction to the electronic refrigeration element 3, and the three-way valve 7 is switched to the flow path indicated by the broken line in the figure. At the same time, the fan 23 is driven and the pump 37 is started. Then, the low-concentration LiCl aqueous solution 36 in the tank 34, which is heated by the electronic refrigeration element 3 that generates heat by the Peltier effect, is sent from the conduit 19 to the outdoor moisture releasing module 21. Tube 2 of the moisture release module 21
The high-temperature, low-concentration LiCl aqueous solution that has entered the inside 2 is released to the atmosphere flowing through the fan 23 outside through the water inside because of the vapor pressure difference between the inside and outside of the water vapor permeable membrane. On the other hand, the LiCl aqueous solution from which water has been released is cooled slightly to a high concentration by the latent heat accompanying dehydration, and returns to the tank 34,
This moisture releasing operation is performed in the LiCl aqueous solution 3 at night such as in the rainy season.
This is continued until the water absorption capacity of 6 is restored.

【0016】図3は、図2で述べた吸湿モジュール11
と放湿モジュール21を、図示しないファンと1次熱交
換器15を収容し,室外に対して室内を換気する熱交換
型換気装置14内の仕切板14a,14bで仕切られた吸
気通路と排気通路に夫々設置し、図2の三方弁7を省略
すると共に、電子冷凍素子3の両面の放熱板4a,4bを
LiCl水溶液36の冷却と加熱に用いるようにした他の
実施例を示している。そして、タンク34内のLiCl水
溶液36を、ポンプ37を介設した管路16で吸湿モジ
ュール11に供給し、ここから放熱板4bとの接触で加
熱しつつ管路17を経て放湿モジュール21に送り、さ
らに管路18を経て放熱板4aとの接触で冷却しつつタ
ンク34に戻すようにしている。
FIG. 3 shows the moisture absorption module 11 described in FIG.
And a moisture releasing module 21, a fan and a primary heat exchanger 15 (not shown) are housed, and an intake passage and an exhaust air which are partitioned by partition plates 14a and 14b in a heat exchange type ventilation device 14 for ventilating the room to the outside. 2 shows another embodiment in which the three-way valve 7 of FIG. 2 is omitted and the heat radiating plates 4a and 4b on both sides of the electronic refrigerating element 3 are used for cooling and heating the LiCl aqueous solution 36, respectively. . Then, the LiCl aqueous solution 36 in the tank 34 is supplied to the moisture absorption module 11 through the pipe line 16 provided with the pump 37, and is heated to the moisture release module 21 through the line line 17 while contacting with the heat dissipation plate 4b. It is sent to the tank 34 and then returned to the tank 34 while being cooled by coming into contact with the heat dissipation plate 4a through the pipe line 18.

【0017】上記実施例では、室外から1次熱交換器1
5を経て冷却されて矢印の如く吸い込まれる外気は、吸
湿モジュール11において、放熱板4aで冷却されてポ
ンプ37で供給される低温で高濃度のLiCl水溶液36
により上述と同じメカニズムで除湿されて室内に流入す
る一方、室内から1次熱交換器15を経て矢印の如く吐
き出される空気は、吸湿で低濃度となり放熱板4bの加
熱で高温になったLiCl水溶液から、放湿モジュール2
1において上述と同じメカニズムで放出される水分を得
て、室外に排気される。この実施例では、電子冷凍素子
3の吸熱と発熱の両面を用いて、LiCl水溶液の吸湿の
ための冷却と放湿のための加熱を同時に行なっているの
で、少量のLiCl水溶液でも吸水能が飽和することがな
く、しかもエネルギが有効に利用できるという利点があ
る。また、吸湿モジュール11に加えて1次熱交換器1
5を備えているので、吸湿効果が大きいので1次熱交換
器15を僅に冷房運転するだけで十分な冷房感を得るこ
とができる。
In the above embodiment, the primary heat exchanger 1 is installed from the outside.
In the moisture absorption module 11, the outside air that has been cooled through 5 and sucked in as indicated by the arrow is cooled by the heat radiating plate 4a and supplied by the pump 37 at a low temperature and a high concentration of the LiCl aqueous solution 36.
While the air is dehumidified by the same mechanism as described above and flows into the room, the air discharged from the room through the primary heat exchanger 15 as shown by the arrow has a low concentration due to moisture absorption and becomes a high temperature by heating the heat dissipation plate 4b. From the moisture release module 2
In 1, the moisture released by the same mechanism as described above is obtained and exhausted to the outside of the room. In this embodiment, both the heat absorption and heat generation of the electronic refrigeration element 3 are used to simultaneously cool the LiCl aqueous solution for absorbing moisture and heat for releasing moisture, so that the water absorbing ability is saturated even with a small amount of LiCl aqueous solution. There is an advantage that energy can be effectively used without doing so. In addition to the moisture absorption module 11, the primary heat exchanger 1
Since 5 is provided, the moisture absorption effect is large, so that a sufficient cooling feeling can be obtained by only slightly cooling the primary heat exchanger 15.

【0018】以上のいずれの実施例においても、吸湿液
体たるLiCl水溶液36の加熱,冷却に電子冷凍素子3
のペルチェ効果を用いているので、圧縮機により蒸発器
や凝縮器に冷媒を循環させる冷凍回路を用いる場合に比
して、装置全体が簡素かつ小型化でき、据え付けも容易
で設置スペースが削減でき、しかも運転に伴う騒音をな
くすことができる。また、電子冷凍素子3は、冷凍回路
に比して加熱効率が大きく、LiCl水溶液の脱水処理に
有利である。尚、電子冷凍素子の冷却効率は、冷凍回路
より多少低いが、LiCl水溶液の吸水能力は、少し冷え
れば大幅に回復するので問題はない。
In any of the above embodiments, the electronic refrigeration element 3 is used for heating and cooling the LiCl aqueous solution 36 which is a hygroscopic liquid.
Since the Peltier effect is used, the entire device can be simplified and downsized compared to the case where a refrigeration circuit that circulates a refrigerant through a compressor is used to circulate the refrigerant, the installation is easy and the installation space can be reduced. Moreover, it is possible to eliminate the noise caused by driving. Further, the electronic refrigeration element 3 has a higher heating efficiency than the refrigeration circuit and is advantageous for the dehydration treatment of the LiCl aqueous solution. Although the cooling efficiency of the electronic refrigeration element is somewhat lower than that of the refrigeration circuit, there is no problem because the water absorption capacity of the LiCl aqueous solution recovers significantly if cooled a little.

【0019】[0019]

【発明の効果】以上の説明で明らかなように、本発明の
請求項1に記載の水蒸気透過膜式除湿装置は、入口が室
内に接続され,出口が室内と室外に切換連通される通風
路内に、チューブの水蒸気透過膜を介して内部の吸湿液
体と外部の流通空気との間で水分の授受を行なう吸,放
湿モジュールを設け、この吸,放湿モジュールにポンプ
を介設した管路を経てタンク内の吸湿液体を循環させる
とともに、循環する吸湿液体を電子冷凍素子のペルチェ
効果により択一的に加熱または冷却するようにしている
ので、圧縮機,蒸発器,凝縮器を含む冷凍回路を用いる場
合に比して、装置全体が簡素かつ小型化でき、据え付け
も容易で設置スペースが削減でき、しかも運転に伴う騒
音をなくすことができる。また、本発明の請求項2に記
載の水蒸気透過膜式除湿装置は、共にチューブの水蒸気
透過膜を介して内部の吸湿液体と外部の空気との間で水
分の授受を行なう吸湿モジュールを室内に,放湿モジュ
ールを室外に夫々設け、循環方向を切り換える切換弁と
ポンプを介設した管路を経て、タンク内の吸湿液体を両
モジュールのいずれかに循環させるとともに、循環する
吸湿液体を電子冷凍素子のペルチェ効果により択一的に
加熱または冷却するようにしているので、上述と同様に
装置全体が簡素かつ小型化でき、据え付けも容易で設置
スペースが削減でき、しかも運転に伴う騒音をなくすこ
とができる。
As is clear from the above description, in the steam permeable membrane type dehumidifier according to claim 1 of the present invention, the inlet is connected to the inside of the room, and the outlet is connected to the inside and outside of the room for ventilation communication. Inside, there is a moisture absorption / desorption module that exchanges moisture between the moisture absorbing liquid inside and the external circulating air through the water vapor permeable membrane of the tube. Since the hygroscopic liquid in the tank is circulated through the passage and the circulating hygroscopic liquid is selectively heated or cooled by the Peltier effect of the electronic refrigeration element, the refrigeration system including the compressor, the evaporator, and the condenser is cooled. Compared to the case where a circuit is used, the entire device can be simple and compact, easy to install, the installation space can be reduced, and the noise caused by the operation can be eliminated. Further, in the water vapor permeable membrane type dehumidifier according to claim 2 of the present invention, a moisture absorption module which exchanges moisture between the moisture absorbent liquid inside and the outside air is provided inside the room through the water vapor permeable membrane of the tube. The moisture releasing module is provided outside the room, and the hygroscopic liquid in the tank is circulated to either of the modules via the switching valve for switching the circulation direction and the pipeline provided with the pump. As it is designed to selectively heat or cool by the Peltier effect of the element, the whole device can be simplified and downsized, the installation is easy and the installation space can be reduced, and the noise accompanying the operation can be eliminated. You can

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

【図1】 本発明の請求項1に記載の水蒸気透過膜式除
湿装置の一実施例を示す回路図である。
FIG. 1 is a circuit diagram showing an embodiment of a water vapor permeable membrane type dehumidifier according to claim 1 of the present invention.

【図2】 本発明の請求項2に記載の水蒸気透過膜式除
湿装置の一実施例を示す回路図である。
FIG. 2 is a circuit diagram showing an embodiment of a water vapor permeable membrane type dehumidifier according to claim 2 of the present invention.

【図3】 図2の実施例を変形した他の実施例を示す回
路図である。
FIG. 3 is a circuit diagram showing another embodiment obtained by modifying the embodiment of FIG.

【図4】 従来の除湿装置を示す図である。FIG. 4 is a diagram showing a conventional dehumidifying device.

【符号の説明】[Explanation of symbols]

1…通風路、2…ダンパ、3…電子冷凍素子、4a,4b
…放熱板、5…スイッチ、6…直流電源、7…三方弁、
8,9,10,19,20…管路、11…吸湿モジュール、
12,22,32…水蒸気透過膜製のチューブ、13,2
3,33…ファン、14…熱交換型換気装置、15…1
次熱交換器、16,17,18…管路、34…タンク、3
6…LiCl水溶液、37…ポンプ、38,39…管路。
1 ... Ventilation path, 2 ... Damper, 3 ... Electronic refrigeration element, 4a, 4b
... Heat sink, 5 ... Switch, 6 ... DC power supply, 7 ... Three-way valve,
8, 9, 10, 19, 20 ... Pipe line, 11 ... Moisture absorption module,
12,22,32 ... Tube made of water vapor permeable membrane, 13,2
3, 33 ... Fan, 14 ... Heat exchange type ventilation device, 15 ... 1
Next heat exchanger, 16, 17, 18 ... Pipe line, 34 ... Tank, 3
6 ... LiCl aqueous solution, 37 ... Pump, 38, 39 ... Pipe line.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 吸湿液体(36)を蓄えるタンク(34)
と、 入口(1a)が室内に接続され、出口(1b,1c)が室内と室
外に切換連通される通風路(1)と、 この通風路(1)に設けられ、水蒸気透過膜製のチューブ
(32)内の吸湿液体とチューブ(32)外の流通空気との
間で膜を介して水分の授受を行なう吸,放湿モジュール
(31)と、 この吸,放湿モジュール(31)に上記タンク(34)の吸
湿液体(36)を循環させるように接続され、吸湿液体
(36)を圧送するポンプ(37)が介設された管路(38,
39)と、 この管路(38)または上記タンク(34)に熱交換しうる
ように設けられ、ペルチェ効果により吸湿液体を択一的
に加熱または冷却する電子冷凍素子(3)を備えることを
特徴とする水蒸気透過膜式除湿装置。
1. A tank (34) for storing a hygroscopic liquid (36)
And an air passage (1) in which the inlet (1a) is connected to the room and the outlet (1b, 1c) is switched between indoor and outdoor for communication, and a tube made of a water vapor permeable membrane provided in the air passage (1).
Absorption and desorption module for exchanging moisture between the hygroscopic liquid inside (32) and the circulating air outside the tube (32) through a membrane.
(31) is connected to the absorbing / releasing module (31) so as to circulate the absorbing liquid (36) in the tank (34).
A conduit (38, 38) in which a pump (37) for pumping (36) is interposed.
39) and an electronic refrigeration element (3) which is provided so as to be able to exchange heat with the pipe line (38) or the tank (34) and selectively heats or cools the hygroscopic liquid by the Peltier effect. Characteristic water vapor permeable membrane type dehumidifier.
【請求項2】 吸湿液体(36)を蓄えるタンク(34)
と、 室内(R)に設けられ、水蒸気透過膜製のチューブ(12)
内の吸湿液体とチューブ(12)外の室内空気との間で膜
を介して水分の授受を行なう吸湿モジュール(11)と、 室外に設けられ、水蒸気透過膜製のチューブ(22)内の
吸湿液体とチューブ(22)外の室外空気との間で膜を介
して水分の授受を行なう放湿モジュール(21)と、 上記吸湿モジュール(11)および放湿モジュール(21)
に上記タンク(34)の吸湿液体(36)を循環させるよう
に接続され、吸湿液体(36)を圧送するポンプ(37)と
吸湿液体の循環方向を切り換える切換弁(7)が介設され
た管路(8,9,10,19,20)と、 この管路または上記タンク(34)に熱交換しうるように
設けられ、ペルチェ効果により吸湿液体(36)を択一的
に加熱または冷却する電子冷凍素子(3)を備えることを
特徴とする水蒸気透過膜式除湿装置。
2. A tank (34) for storing a hygroscopic liquid (36).
And a tube (12) made of a water vapor permeable membrane provided in the room (R)
A moisture absorption module (11) that exchanges moisture between a moisture absorbing liquid inside and the room air outside the tube (12) through a membrane, and moisture absorption inside a tube (22) made of a water vapor permeable membrane provided outside the room. A moisture releasing module (21) for transferring and receiving moisture between a liquid and the outdoor air outside the tube (22) through a membrane, and the moisture absorbing module (11) and the moisture releasing module (21).
A pump (37) for pumping the hygroscopic liquid (36) and a switching valve (7) for switching the circulating direction of the hygroscopic liquid are connected to the tank (34) so as to circulate the hygroscopic liquid (36). The pipes (8, 9, 10, 19, 20) and the pipes or the tank (34) are provided so as to exchange heat with each other, and selectively heat or cool the hygroscopic liquid (36) by the Peltier effect. A water vapor permeable membrane type dehumidifier comprising an electronic refrigeration element (3)
JP4308612A 1992-11-18 1992-11-18 Dehumidifier of steam-permeable membrane-type Pending JPH06154543A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4308612A JPH06154543A (en) 1992-11-18 1992-11-18 Dehumidifier of steam-permeable membrane-type

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4308612A JPH06154543A (en) 1992-11-18 1992-11-18 Dehumidifier of steam-permeable membrane-type

Publications (1)

Publication Number Publication Date
JPH06154543A true JPH06154543A (en) 1994-06-03

Family

ID=17983146

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4308612A Pending JPH06154543A (en) 1992-11-18 1992-11-18 Dehumidifier of steam-permeable membrane-type

Country Status (1)

Country Link
JP (1) JPH06154543A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19629719A1 (en) * 1995-07-24 1997-01-30 Mitsubishi Electric Corp Water evaporation cooling system and process based on an electrolytic reaction
US6434955B1 (en) * 2001-08-07 2002-08-20 The National University Of Singapore Electro-adsorption chiller: a miniaturized cooling cycle with applications from microelectronics to conventional air-conditioning
KR100801715B1 (en) * 2006-09-05 2008-02-15 아산엔텍 주식회사 Apparatus for humidity-control function of air conditioning facility
CN105910327A (en) * 2016-04-01 2016-08-31 段茨尤 Novel refrigeration air conditioner
CN106979573A (en) * 2017-05-16 2017-07-25 广东工业大学 Membrane type liquid desiccant air conditioning
JP2021133264A (en) * 2020-02-21 2021-09-13 パナソニックIpマネジメント株式会社 Steam concentrator, steam concentration method, humidified gas production method, fuel cell vehicle and gasoline vehicle
US11225025B2 (en) 2016-10-27 2022-01-18 Hewlett-Packard Development Company, L.P. Generating additive manufacturing instructions
CN115164455A (en) * 2022-06-20 2022-10-11 合肥通用机械研究院有限公司 Cold-carrying medium circulating system with moisture absorption prevention function

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5687576A (en) * 1995-07-24 1997-11-18 Mitsubishi Denki Kabushiki Kaisha Water-evaporation type cooling system based on electrolytic reaction and water-evaporation type cooling method therefor
DE19629719C2 (en) * 1995-07-24 1999-01-07 Mitsubishi Electric Corp Water evaporation cooling system and process based on an electrolytic reaction
DE19629719A1 (en) * 1995-07-24 1997-01-30 Mitsubishi Electric Corp Water evaporation cooling system and process based on an electrolytic reaction
US6434955B1 (en) * 2001-08-07 2002-08-20 The National University Of Singapore Electro-adsorption chiller: a miniaturized cooling cycle with applications from microelectronics to conventional air-conditioning
KR100801715B1 (en) * 2006-09-05 2008-02-15 아산엔텍 주식회사 Apparatus for humidity-control function of air conditioning facility
CN105910327B (en) * 2016-04-01 2018-04-10 段茨尤 A kind of New Refrigerating air-conditioning
CN105910327A (en) * 2016-04-01 2016-08-31 段茨尤 Novel refrigeration air conditioner
US11225025B2 (en) 2016-10-27 2022-01-18 Hewlett-Packard Development Company, L.P. Generating additive manufacturing instructions
CN106979573A (en) * 2017-05-16 2017-07-25 广东工业大学 Membrane type liquid desiccant air conditioning
CN106979573B (en) * 2017-05-16 2022-09-16 广东工业大学 Membrane type solution dehumidifying air conditioner
JP2021133264A (en) * 2020-02-21 2021-09-13 パナソニックIpマネジメント株式会社 Steam concentrator, steam concentration method, humidified gas production method, fuel cell vehicle and gasoline vehicle
CN115164455A (en) * 2022-06-20 2022-10-11 合肥通用机械研究院有限公司 Cold-carrying medium circulating system with moisture absorption prevention function
CN115164455B (en) * 2022-06-20 2023-10-24 合肥通用机械研究院有限公司 Cold-carrying medium circulation system with moisture absorption preventing function

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