JPH07108127A - Dehumidification regenerator using hygroscopic liquid - Google Patents

Dehumidification regenerator using hygroscopic liquid

Info

Publication number
JPH07108127A
JPH07108127A JP5257017A JP25701793A JPH07108127A JP H07108127 A JPH07108127 A JP H07108127A JP 5257017 A JP5257017 A JP 5257017A JP 25701793 A JP25701793 A JP 25701793A JP H07108127 A JPH07108127 A JP H07108127A
Authority
JP
Japan
Prior art keywords
dehumidifying
hygroscopic liquid
tank
liquid
pump
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
JP5257017A
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 JP5257017A priority Critical patent/JPH07108127A/en
Publication of JPH07108127A publication Critical patent/JPH07108127A/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
    • 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
    • F24F2003/144Air-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 dehumidification only

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Central Air Conditioning (AREA)
  • Drying Of Gases (AREA)

Abstract

PURPOSE:To regenerate a hygroscopic liquid with high energy efficiency while preventing the hygroscopic liquid from scattering by a simple and inexpensive constitution. CONSTITUTION:A dehumidifying module 1 for absorbing the moisture contained in air in a room flowing to the other side of tubes into a hygroscopic liquid L circulating to one side of the tubes through the membrane of the tubes 3 made of a steam permeable membrane, a tank 4 having a heater 5 and for storing a hygroscopic liquid L, and feed piping 6 and return piping 7 for connecting the dehumidifying module 1 and the tank 4 so that the hygroscopic liquid may be circulated are provided. In the feed piping 6, a cooler 8 and a pump 9 which is on the dehumidifying module 1 side of the cooler 8 are installed. The delivery of the pump 9 is controlled by a controller 19 so as to increase in the first and last stages of operation. The upper surface of the tank 4 is covered with a cover 4 on which a discharge duct 15 whose end part is bent at right angles is erected.

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、空気中の水分を吸湿液
体に吸収して室内を除湿するとともに、吸水で希釈され
た吸湿液体から水分を除去して再生する吸湿液体を用い
た除湿再生装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a dehumidifying regeneration using a hygroscopic liquid which absorbs moisture in the air into the hygroscopic liquid to dehumidify the inside of the room and removes moisture from the hygroscopic liquid diluted with water to regenerate it. Regarding the device.

【0002】[0002]

【従来の技術】従来、この種の除湿再生装置として、た
とえば図5に示すようなものが知られている(特開平2
−140535号公報)。この除湿再生装置は、吸湿液
体たる塩化リチウム(LiCl)の水溶液が、これに接触す
る空気の相対湿度を、当該水溶液の濃度が高いほど、ま
た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、この除湿再生装置は、空気調和室21内に、
水蒸気透過膜製の数本のチューブ23を並列に配設して
なる調湿ユニット22,22と送風ファン24を設け、
クーラ26,撹拌機27,給水弁28を備えたタンク25
内に貯えたLiCl水溶液29を、ポンプ30により送り
配管31,戻り配管32を経て上記調湿ユニット22に
循環供給する。一方、室外に、送風ファン34をもつ上
記調湿ユニットと同様の濃縮ユニット33とヒータ35
を設け、タンク25内のLiCl水溶液29を、ポンプ3
6により配管37,38を経て上記ヒータ35と濃縮ユ
ニット33に循環供給する。
2. Description of the Related Art Conventionally, as a dehumidifying / regenerating device of this type, a device as shown in FIG.
-140535 publication). This dehumidification regeneration device utilizes the principle that an aqueous solution of lithium chloride (LiCl), which is a hygroscopic liquid, keeps the relative humidity of the air in contact with it at a lower value as the concentration of the aqueous solution is higher and the temperature is lower. ing. That is, this dehumidifying / regenerating device is provided in the air conditioning chamber 21.
Provided are humidity control units 22 and 22 in which several tubes 23 made of a water vapor permeable film are arranged in parallel and a blower fan 24.
Tank 25 equipped with cooler 26, stirrer 27, and water supply valve 28
The LiCl aqueous solution 29 stored therein is circulated and supplied to the humidity control unit 22 by a pump 30 via a feed pipe 31 and a return pipe 32. On the other hand, outside the room, a concentration unit 33 and a heater 35 similar to the humidity control unit having the blower fan 34 are provided.
Is provided, and the LiCl aqueous solution 29 in the tank 25 is pumped to the pump 3
6 is circulated and supplied to the heater 35 and the concentrating unit 33 through the pipes 37 and 38.

【0003】そして、空気調和室21を加湿するには、
濃度検出器39が検出する濃度に基づきコントローラ4
0によって、ヒータ35を動作させかつ給水弁28を開
くことで、タンク25内のLiCl水溶液29を所定の高
温,低濃度にしてポンプ30により調湿ユニット22に
供給し、LiCl水溶液中の水分をチューブ膜を透過させ
て室内に放出する。また、空気調和室21を除湿するに
は、濃度検出器39の検出濃度が所定の高濃度になるま
で、コントローラ40によってポンプ36,ヒータ3
5,送風ファン34を動作させ、タンク25内のLiCl
水溶液29を高温にして濃縮ユニット33に供給し、水
溶液中の水分をチューブ膜を透過させて室外に放出す
る。次いで、所定の高濃度となったタンク25内のLi
Cl水溶液を、クーラ26で所定の低温まで冷却した
後、ポンプ30により調湿ユニット22に供給し、空気
調和室21内の空気に含まれる水分をチューブ膜を透過
させてLiCl水溶液に吸収する。
To humidify the air conditioning chamber 21,
The controller 4 based on the concentration detected by the concentration detector 39
When the heater 35 is operated and the water supply valve 28 is opened by 0, the LiCl aqueous solution 29 in the tank 25 is adjusted to have a predetermined high temperature and a low concentration, and is supplied to the humidity control unit 22 by the pump 30 so that the water in the LiCl aqueous solution is removed. It permeates the tube membrane and is released indoors. To dehumidify the air conditioning chamber 21, the controller 40 pumps the pump 36 and the heater 3 until the detected concentration of the concentration detector 39 reaches a predetermined high concentration.
5. Operate the blower fan 34 to operate the LiCl in the tank 25.
The aqueous solution 29 is heated to a high temperature and supplied to the concentrating unit 33, and the water in the aqueous solution permeates the tube membrane and is discharged to the outside of the room. Next, Li in the tank 25, which has reached a predetermined high concentration,
After the Cl aqueous solution is cooled to a predetermined low temperature by the cooler 26, it is supplied to the humidity control unit 22 by the pump 30 so that the water contained in the air in the air conditioning chamber 21 permeates the tube membrane and is absorbed in the LiCl aqueous solution.

【0004】[0004]

【発明が解決しようとする課題】ところが、上記従来の
除湿再生装置は、吸水したLiCl水溶液29を、ヒータ
35にて140〜150℃に加熱後、送風ファン34で
通風される濃縮ユニット33に通して濃縮しているた
め、加熱されたLiCl水溶液がもつ熱量が、送風ファン
の風に多量に奪われて熱損失が大きく、再生時のエネル
ギ効率が50%程度まで低下するという問題がある。ま
た、加熱されたLiCl水溶液は、風で冷却されるにすぎ
ないので、チューブ23や配管38などの腐食や劣化を
防ぐ観点からLiCl水溶液を余り高温に加熱できず、そ
れ故、高濃度の濃縮が期待できない。また、LiCl水溶
液を再生するのに、ポンプ36,配管37,ヒータ35,
送風ファン34,濃縮ユニット33などの多くの部材が
必要なため、装置が複雑化し、高価になるという問題が
ある。さらに、クーラ26をタンク25内に設けている
ため、タンク内のLiCl水溶液29全体を所定の低温
(例えば20℃)まで冷却してからでないと、調湿ユニッ
ト22に供給することができず、容量の大きい大型のク
ーラ26が必要になるという問題がある。
However, in the conventional dehumidifying / regenerating apparatus described above, the absorbed LiCl aqueous solution 29 is heated to 140 to 150 ° C. by the heater 35 and then passed through the concentration unit 33 which is ventilated by the blower fan 34. Since the concentrated LiCl solution is concentrated, the amount of heat of the heated LiCl aqueous solution is absorbed by a large amount of air from the blower fan, resulting in a large heat loss, and the energy efficiency during regeneration is reduced to about 50%. Further, since the heated LiCl aqueous solution is only cooled by the wind, the LiCl aqueous solution cannot be heated to a very high temperature from the viewpoint of preventing the corrosion and deterioration of the tube 23, the pipe 38, etc., and therefore, the concentrated high concentration solution is used. Can not be expected. Moreover, in order to regenerate the LiCl aqueous solution, the pump 36, the pipe 37, the heater 35,
Since many members such as the blower fan 34 and the concentrating unit 33 are required, the device becomes complicated and expensive. Furthermore, since the cooler 26 is provided in the tank 25, the entire LiCl aqueous solution 29 in the tank is kept at a predetermined low temperature.
There is a problem that it cannot be supplied to the humidity control unit 22 until it is cooled to (for example, 20 ° C.), and a large-sized cooler 26 having a large capacity is required.

【0005】そこで、本発明の目的は、タンクの構造や
吸湿液体の濃縮手法,冷却器の配置及び送液ポンプの制
御を工夫することによって、簡素かつ安価な構成でもっ
て、吸湿液体の飛散を防止しつつ、高いエネルギ効率で
吸湿液体を再生でき、ランニングコストの低減を図るこ
とができる吸湿液体を用いた除湿再生装置を提供するこ
とにある。
Therefore, an object of the present invention is to devise the structure of the tank, the method of concentrating the hygroscopic liquid, the arrangement of the cooler, and the control of the liquid feed pump to prevent the hygroscopic liquid from scattering with a simple and inexpensive structure. It is an object of the present invention to provide a dehumidification / regeneration device using a hygroscopic liquid that can regenerate the hygroscopic liquid with high energy efficiency while reducing the running cost.

【0006】[0006]

【課題を解決するための手段】上記目的を達成するた
め、請求項1の除湿再生装置は、図1に例示するよう
に、水蒸気透過膜3を通してこの膜3の一方に循環する
吸湿液体Lに、上記膜3の他方に流れる室内空気に含ま
れる水分を吸収する除湿モジュール1と、ヒータ5を有
して上記吸湿液体Lを貯えるタンク4と、上記吸湿液体
Lが循環するように上記除湿モジュール1とタンク4と
を接続する送り配管6および戻り配管7と、吸湿液体L
を圧送するポンプ9と、上記送り配管6に介設され、循
環する吸湿液体Lを冷却する冷却器8を備えたことを特
徴とする。請求項2の除湿再生装置は、上記ポンプ9
を、上記送り配管6の上記冷却器8よりも除湿モジュー
ル1側に介設している。請求項3の除湿再生装置は、請
求項1または2に記載の上記タンク4の上面が、所定角
度で先端部が屈曲する排気ダクト15を立設した蓋14
によって覆われている。
In order to achieve the above object, the dehumidifying / regenerating apparatus according to the first aspect of the present invention uses a moisture absorbing liquid L circulating through one of the vapor permeable membranes 3 to one of the membranes 3 as shown in FIG. , A dehumidifying module 1 for absorbing water contained in the room air flowing through the other side of the membrane 3, a tank 4 having a heater 5 for storing the hygroscopic liquid L, and the dehumidifying module for circulating the hygroscopic liquid L. 1 and the feed pipe 6 and the return pipe 7 connecting the tank 4 and the hygroscopic liquid L
And a cooler 8 which is provided in the feed pipe 6 and cools the circulating hygroscopic liquid L. The dehumidifying / regenerating device according to claim 2 is the pump 9
Is provided on the dehumidifying module 1 side of the feed pipe 6 with respect to the cooler 8. A dehumidifying / regenerating apparatus according to a third aspect is a lid 14 in which an exhaust duct 15 whose tip portion is bent at a predetermined angle is provided on the upper surface of the tank 4 according to the first or second aspect.
Is covered by.

【0007】請求項4の除湿再生装置は、請求項1また
は2に記載のタンクが、排気ダクト15を立設した蓋1
4によって覆われており、上記排気ダクト15の内面
に、吸湿液体Lの放出を防止する隔離板18が設けられ
ている。請求項5の除湿再生装置は、請求項3または4
に記載の上記排気ダクト15の先端部19が、屈曲して
いて、水槽20の水W中に浸されている。請求項6の除
湿再生装置は、請求項1の上記ポンプ9の送液流量Q
が、制御器10によって運転初期に多くなるように制御
される。請求項7の除湿再生装置は、請求項6に記載の
上記制御器10が、上記ポンプ9の送液流量Qを、運転
終期においても多くなるように制御する。
In the dehumidifying / regenerating apparatus according to a fourth aspect, the tank according to the first or second aspect is a lid 1 in which an exhaust duct 15 is provided upright.
4, a separator plate 18 for preventing the release of the hygroscopic liquid L is provided on the inner surface of the exhaust duct 15. The dehumidifying / regenerating device according to claim 5 is the dehumidifying / regenerating device according to claim 3 or 4.
The tip portion 19 of the exhaust duct 15 described in 1 above is bent and immersed in the water W in the water tank 20. The dehumidifying / regenerating device according to claim 6 is the liquid supply flow rate Q of the pump 9 according to claim 1.
Are controlled by the controller 10 to increase in the initial stage of operation. In the dehumidifying / regenerating apparatus according to claim 7, the controller 10 according to claim 6 controls the liquid supply flow rate Q of the pump 9 so as to increase even at the end of the operation.

【0008】[0008]

【作用】まず、請求項1の除湿再生装置で室内を除湿す
る場合、送り配管6に介設された冷却器8を動作させる
とともに、タンク4内の高濃度の吸湿液体Lをポンプ9
によって上記送り配管6を経て除湿モジュール1へ送り
出す。すると、高濃度の吸湿液体Lは、冷却器8で所定
の低温まで冷却されて、除湿モジュール1の水蒸気透過
膜3の一方(例えばチューブの外側)に流れて、水蒸気透
過膜3の他方(例えばチューブの内側)に流れる室内空気
に含まれる水分を、膜を通して吸収する。吸水で低濃度
になった吸湿液体Lは、戻り配管7を経てタンク4に戻
され、かかる吸湿液体の循環によって、室内が除湿され
る。上記冷却器8は、タンク4内の全吸湿液体でなく、
除湿モジュール1へ送られる吸湿液体だけを冷却すれば
よいので、容量が小さい小型のもので足る。つぎに、吸
水で低濃度になったタンク4内の吸湿液体Lを再生する
場合、吸湿液体Lを送り配管6,戻り配管7に循環させ
ずに、ヒータ5を動作させる。すると、吸湿液体Lは所
定の高温まで加熱され、吸湿液体Lに含まれていた水分
は、タンク4の上面から大気中へ蒸発し、吸湿液体L
は、脱水により濃縮,再生される。このように、タンク
4内の吸湿液体を加熱して水分蒸発で再生を行なうの
で、ポンプ,ヒータ,ファン付きの濃縮ユニットを介設し
た配管に吸湿液体を循環させて濃縮,再生する手法に比
して、構成が簡素なうえ、放熱による損失が著しく少な
く、再生時のエネルギ効率が大幅に向上する。
First, when dehumidifying the room with the dehumidifying / regenerating apparatus of claim 1, the cooler 8 provided in the feed pipe 6 is operated and the highly concentrated hygroscopic liquid L in the tank 4 is pumped.
Is sent to the dehumidifying module 1 through the feed pipe 6. Then, the highly concentrated hygroscopic liquid L is cooled to a predetermined low temperature by the cooler 8 and flows into one of the water vapor permeable membranes 3 of the dehumidification module 1 (for example, the outside of the tube) and the other of the water vapor permeable membranes 3 (for example, Moisture contained in the room air flowing inside the tube) is absorbed through the membrane. The hygroscopic liquid L having a low concentration due to water absorption is returned to the tank 4 through the return pipe 7, and the room is dehumidified by the circulation of the hygroscopic liquid. The cooler 8 is not all the hygroscopic liquid in the tank 4,
Since only the hygroscopic liquid sent to the dehumidifying module 1 needs to be cooled, a small one with a small capacity is sufficient. Next, when regenerating the hygroscopic liquid L in the tank 4 having a low concentration due to water absorption, the heater 5 is operated without circulating the hygroscopic liquid L in the feed pipe 6 and the return pipe 7. Then, the hygroscopic liquid L is heated to a predetermined high temperature, the moisture contained in the hygroscopic liquid L evaporates from the upper surface of the tank 4 into the atmosphere, and the hygroscopic liquid L
Is concentrated and regenerated by dehydration. As described above, since the hygroscopic liquid in the tank 4 is heated and regenerated by evaporation of water, it is possible to circulate the hygroscopic liquid in a pipe provided with a concentrating unit having a pump, a heater, and a fan to concentrate and regenerate the liquid. As a result, the structure is simple, the loss due to heat dissipation is extremely small, and the energy efficiency during regeneration is greatly improved.

【0009】請求項2の除湿再生装置では、送り配管6
の冷却器8よりも除湿モジュール1側にポンプ9が介設
されている。従って、ポンプ9には、冷却された低温の
吸湿液体が流れるので、高温の吸湿液体によるポンプ9
の腐食や故障を防止することができる。請求項3の除湿
再生装置では、タンク4の上面が、先端部が所定角度で
屈曲する排気ダクト15を立設した蓋14によって覆わ
れている。従って、再生時のヒータ加熱で吸湿液体中の
水分が沸騰する際、吸湿液体Lが液面から外へ飛散して
も、蓋14や排気ダクト15で遮られて外部へ殆んど出
ず、外部の機器が吸湿液体で腐食等されることもない。
また、タンク4上面が開放されている場合に比して、ヒ
ータ5による加熱効率も向上する。
In the dehumidifying / regenerating apparatus of claim 2, the feed pipe 6
A pump 9 is provided on the dehumidifying module 1 side of the cooler 8. Therefore, since the cooled low-temperature hygroscopic liquid flows through the pump 9, the pump 9 using the high-temperature hygroscopic liquid
It is possible to prevent corrosion and failure of the. In the dehumidifying / regenerating apparatus according to the third aspect, the upper surface of the tank 4 is covered with the lid 14 in which the exhaust duct 15 whose tip portion bends at a predetermined angle is provided upright. Therefore, when the moisture in the hygroscopic liquid is boiled by heating with the heater during regeneration, even if the hygroscopic liquid L is scattered from the liquid surface to the outside, it is blocked by the lid 14 and the exhaust duct 15 and hardly comes out. External equipment will not be corroded by the hygroscopic liquid.
Further, the heating efficiency of the heater 5 is improved as compared with the case where the upper surface of the tank 4 is opened.

【0010】請求項4の除湿再生装置では、タンクの上
面が排気ダクト15を立設した蓋14で覆われており、
排気ダクト15の内面に、隔離板18が設けられてい
る。従って、再生時の水分の沸騰に伴って液面から外へ
飛散する吸湿液体Lは、隔離板18に遮られて外部への
放出が一層防止され、外部の機器の腐食等も一層防止さ
れる。請求項5の除湿再生装置では、排気ダクト15の
先端部19が、屈曲していて、水槽20の水W中に浸さ
れている。したがって、外部へ出ようとする吸湿液体L
は、水中に総て捕らえられ、吸湿液体Lの外部への放出
は皆無となる。
In the dehumidifying / regenerating apparatus of the fourth aspect, the upper surface of the tank is covered with the lid 14 in which the exhaust duct 15 is erected.
A separator plate 18 is provided on the inner surface of the exhaust duct 15. Therefore, the hygroscopic liquid L scattered from the liquid surface due to boiling of water during regeneration is blocked by the separator 18 to be further prevented from being discharged to the outside, and corrosion of the external equipment is further prevented. . In the dehumidifying / regenerating apparatus of the fifth aspect, the tip end portion 19 of the exhaust duct 15 is bent and immersed in the water W in the water tank 20. Therefore, the hygroscopic liquid L that is about to go out
Are all trapped in the water, and the hygroscopic liquid L is never released to the outside.

【0011】タンク4内の所定の低温,高濃度の吸湿液
体Lは、所定体積であるから、除湿モジュール1への低
温,高濃度の吸湿液体の流量Qを少なくすると、長時間
運転が可能になるが,運転直後の除湿能力の立ち上がり
が緩慢になる一方、上記流量Qを多くすると、運転開始
と共に除湿能力は急増するが,その後すぐに減少する。
請求項6の除湿再生装置では、ポンプ9の送液流量Q
が、制御器10によって運転初期に多くなるように制御
されるので、起動時の除湿能力の立ち上がりを急峻にし
つつ、長時間に亘って除湿運転を行なうことができる。
請求項7の除湿再生装置では、上記制御器10が、ポン
プ9の送液流量Qを運転終期においても多くなるように
制御する。したがって、吸湿過程全体の時間は幾分少な
くなるが、吸湿液体の運転終期における除湿能力の急激
な低下が防止できる。
Since the predetermined low temperature, high concentration hygroscopic liquid L in the tank 4 has a predetermined volume, if the flow rate Q of the low temperature, high concentration hygroscopic liquid to the dehumidifying module 1 is reduced, long-term operation becomes possible. However, while the dehumidifying capacity immediately after the operation rises slowly, when the flow rate Q is increased, the dehumidifying capacity rapidly increases with the start of the operation, but decreases immediately thereafter.
In the dehumidifying / regenerating apparatus according to claim 6, the liquid feeding flow rate Q of the pump 9
However, since it is controlled by the controller 10 so as to increase in the initial stage of the operation, it is possible to perform the dehumidifying operation for a long time while making the dehumidifying capacity at the start-up steep.
In the dehumidifying / regenerating apparatus according to claim 7, the controller 10 controls the liquid supply flow rate Q of the pump 9 so as to increase even at the end of the operation. Therefore, although the time of the entire moisture absorption process is somewhat reduced, it is possible to prevent the dehumidification ability of the hygroscopic liquid at the end of the operation from rapidly decreasing.

【0012】[0012]

【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、本発明の吸湿液体を用いた除湿再生装
置の一例を示す構成図である。この除湿再生装置は、容
器2を貫通するように多数の水蒸気透過膜製のチューブ
3,3,…を長手方向(図1の紙面に垂直な方向)に配置し
て、各チューブ3の内側を流れる室内空気に含まれる水
分を、各チューブ3の外側の容器内を循環する吸湿液体
たるLiCl水溶液に吸収する1対の除湿モジュール1
と、ヒータ5を有してLiCl水溶液Lを貯えるタンク4
と、LiCl水溶液Lが循環するように上記除湿モジュー
ル1とタンク4とを接続する送り配管6および戻り配管
7と、循環するLiCl水溶液を冷却すべく,送り配管6
に介設された冷却器8と、LiCl水溶液を圧送すべく,
この冷却器8よりも除湿モジュール1側の送り配管6に
介設されたポンプ9と、このポンプ9の送液流量を運転
時期に応じて制御する制御器10を備えている。
The present invention will be described in detail below with reference to the embodiments shown in the drawings. FIG. 1 is a configuration diagram showing an example of a dehumidifying / regenerating apparatus using the hygroscopic liquid of the present invention. In this dehumidifying / regenerating device, a large number of water vapor permeable membrane tubes 3, 3, ... Are arranged in the longitudinal direction (perpendicular to the paper surface of FIG. 1) so as to penetrate the container 2, and the inside of each tube 3 is A pair of dehumidification modules 1 for absorbing the water contained in the flowing indoor air into the LiCl aqueous solution which is a hygroscopic liquid circulating in the container outside each tube 3.
And a tank 4 having a heater 5 for storing the LiCl aqueous solution L
And a feed pipe 6 and a return pipe 7 that connect the dehumidifying module 1 and the tank 4 so that the LiCl aqueous solution L circulates, and the feed pipe 6 for cooling the circulating LiCl aqueous solution.
In order to pump the LiCl aqueous solution,
A pump 9 provided in the feed pipe 6 on the dehumidification module 1 side of the cooler 8 and a controller 10 for controlling the liquid flow rate of the pump 9 according to the operation timing are provided.

【0013】上記除湿モジュール1は、各チューブ3内
に室内空気を送り込むファン11を有する一方、送り配
管6の除湿モジュールへの分岐配管6a,6bには、開閉
弁12を夫々設けている。上記タンク4は、上面を除く
外周を断熱材13で覆うとともに、上面を、先端部が9
0°の角度で屈曲する排気ダクト15を立設した蓋14
で覆っている。上記冷却器8は、除湿モジュール1へ送
られる高濃度のLiCl水溶液を、送り配管6において冷
却するものであって、具体的には、図2(A)に示す空冷
用の螺旋状の配管16や、図2(B)に示すLiCl水溶液
用の管17aと冷却液用の管17bを接合してなる2重熱
交換配管17で構成することができる。
The dehumidifying module 1 has a fan 11 for feeding indoor air into each tube 3, while branch pipes 6a, 6b to the dehumidifying module of the feed pipe 6 are provided with open / close valves 12, respectively. The tank 4 covers the outer periphery except the upper surface with a heat insulating material 13, and the upper surface has a tip portion of 9
A lid 14 in which an exhaust duct 15 that bends at an angle of 0 ° is erected
Covered with. The cooler 8 cools the high-concentration LiCl aqueous solution sent to the dehumidifying module 1 in the feed pipe 6, and specifically, the spiral pipe 16 for air cooling shown in FIG. 2 (A). Alternatively, the double heat exchange pipe 17 shown in FIG. 2B may be formed by joining the LiCl aqueous solution pipe 17a and the cooling liquid pipe 17b.

【0014】図3は、タンク4の上部の排気ダクト15
の変形例を示しており、図3(A)に示すように、排気ダ
クト15の内面にLiCl水溶液Lの外部への放出を防止
する複数の隔離板18を設けたり、図3(B)に示すよう
に、U字状に180°の角度で屈曲させた排気ダクトの
先端部19を、水槽20の水Wの中に浸したりすること
ができる。
FIG. 3 shows the exhaust duct 15 at the top of the tank 4.
3A, a plurality of separator plates 18 for preventing the release of the LiCl aqueous solution L to the outside are provided on the inner surface of the exhaust duct 15, or as shown in FIG. 3B. As shown, the tip portion 19 of the exhaust duct bent in a U shape at an angle of 180 ° can be immersed in the water W in the water tank 20.

【0015】上記制御器10は、LiCl水溶液Lを除湿
モジュール1に圧送するポンプ9の送液流量Qを、図4
(A)に示すように、運転初期および運転終期に多くな
り,その他の時期に少なくなるように制御する。この送
液流量Qの制御は、ポンプ9の回転数を変化させたり、
一定回転数のポンプ9をオン,オフ制御して行なうこと
ができる。吸湿のためにタンク4内に貯えられた高濃度
のLiCl水溶液Lの体積は、一定であるから、図4
(B)に示すように、送液流量Qを少なくすると、図中
の破線の如く長時間運転が可能になるが、運転初期の除
湿能力(単位時間当たりの吸水量)の立ち上がりが緩慢に
なり、かつ運転終期の除湿能力の立ち下がりが急峻にな
る。一方、送液流量Qを多くすると、図4(B)の実線で
示す如く運転開始と共に除湿能力は急増するが、その後
すぐに除湿能力は減少する。そこで、運転初期および運
転終期に送液流量Qを多くすることによって、図4(A)
の実線で示す如く、起動時の除湿能力の立ち上がりを急
峻にし、運転終期の除湿能力の急減を防止し、略均一な
除湿能力でもって比較的長時間に亘る除湿運転を可能に
するのである。なお、この場合の少ない送液流量Qの値
は、図4(A)の時間軸のフルスケールを1日の除湿時間
としたとき、曲線下の面積がタンク4内のLiCl水溶液
の全吸水可能量になるように設定される。
The controller 10 controls the liquid supply flow rate Q of the pump 9 for pumping the LiCl aqueous solution L to the dehumidifying module 1 as shown in FIG.
As shown in (A), control is performed such that the amount increases at the beginning and end of the operation and decreases at other times. The control of the liquid supply flow rate Q is performed by changing the rotation speed of the pump 9,
The pump 9 having a constant rotation speed can be controlled to be turned on and off. Since the volume of the high-concentration LiCl aqueous solution L stored in the tank 4 for absorbing moisture is constant, FIG.
As shown in (B), if the liquid flow rate Q is reduced, long-term operation is possible as indicated by the broken line in the figure, but the dehumidification capacity (water absorption per unit time) at the beginning of operation becomes slow to rise. In addition, the dehumidification capacity at the end of operation drops sharply. On the other hand, when the liquid delivery flow rate Q is increased, the dehumidifying ability rapidly increases with the start of operation as shown by the solid line in FIG. 4B, but immediately thereafter, the dehumidifying ability decreases. Therefore, by increasing the liquid delivery flow rate Q at the beginning and end of the operation,
As shown by the solid line, the rising of the dehumidifying ability at the start is made steep, the dehumidifying ability at the end of the operation is prevented from being sharply reduced, and the dehumidifying operation can be performed for a relatively long time with the substantially uniform dehumidifying ability. In this case, the small value of the liquid supply flow rate Q is such that the area under the curve is the total water absorption of the LiCl aqueous solution in the tank 4 when the full scale of the time axis of FIG. Set to be quantity.

【0016】上記構成の除湿再生装置の動作について、
図1を参照しつつ次に述べる。まず、昼間などに室内を
除湿する場合、タンク4に貯えられたLiCl水溶液Lを
所定の高濃度にし、送り配管6に介設された冷却器8と
ポンプ9を動作させて、高濃度のLiCl水溶液Lをタン
ク4から除湿モジュール1に送り出す。すると、高濃度
のLiCl水溶液Lは、冷却器8で所定の低温(例えば2
0℃)まで冷却されて、除湿モジュール1の各チューブ
3の外側の容器2内を循環して、各チューブ3の内側を
流れる室内空気に含まれる水分を、チューブ膜を通して
吸収する。吸水で低濃度になったLiCl水溶液は、戻り
配管7を経てタンク4に戻され、かかるLiCl水溶液の
循環によって室内が除湿される。上記冷却器8は、タン
ク4内の全LiCl水溶液でなく、除湿モジュール1に送
られるLiCl水溶液だけを冷却すればよいので、冷却容
量の小さい小型のもので足り、装置の小型化と低廉化が
図れる。また、ポンプ9でLiCl水溶液を除湿モジュー
ル1に圧送するので、LiCl水溶液の確実な供給ができ
るうえ、ポンプ9が冷却器8の下流側にあって、低温の
LiCl水溶液が流れるので、高温のLiCl水溶液による
ポンプ9の腐食や故障が防止でき、長期使用が可能にな
る。
Regarding the operation of the dehumidifying / regenerating apparatus having the above-mentioned structure,
Next, referring to FIG. First, when dehumidifying the room during the daytime, the LiCl aqueous solution L stored in the tank 4 is made to have a predetermined high concentration, and the cooler 8 and the pump 9 provided in the feed pipe 6 are operated to make the high concentration LiCl. The aqueous solution L is sent from the tank 4 to the dehumidification module 1. Then, the high-concentration LiCl aqueous solution L is cooled by the cooler 8 at a predetermined low temperature (for example, 2
It is cooled to 0 ° C.), circulates inside the container 2 outside each tube 3 of the dehumidification module 1, and absorbs moisture contained in the room air flowing inside each tube 3 through the tube membrane. The LiCl aqueous solution having a low concentration due to water absorption is returned to the tank 4 through the return pipe 7, and the room is dehumidified by the circulation of the LiCl aqueous solution. Since the cooler 8 needs to cool only the LiCl aqueous solution sent to the dehumidifying module 1 instead of the entire LiCl aqueous solution in the tank 4, a small cooling capacity is sufficient, and the apparatus can be downsized and inexpensive. Can be achieved. Moreover, since the LiCl aqueous solution is pressure-fed to the dehumidifying module 1 by the pump 9, the LiCl aqueous solution can be reliably supplied, and the low temperature LiCl aqueous solution flows in the downstream side of the cooler 8, so that the high temperature LiCl aqueous solution flows. Corrosion and failure of the pump 9 due to the aqueous solution can be prevented, and long-term use becomes possible.

【0017】次に、吸水で低濃度になったタンク4内の
LiCl水溶液を、安価な夜間電力を用いて夜間などに再
生する場合、冷却器8とポンプ9を非動作にし,開閉弁
12を閉じて、LiCl水溶液を送り配管6,戻り配管7
に循環させることなく、ヒータ5を動作させる。する
と、タンク4内のLiCl水溶液Lは所定の高温(例えば
140〜150℃)まで加熱され、LiCl水溶液に含ま
れていた水分は、図1に示すように沸騰して、タンク上
部の排気ダクト15から大気中へ放出され、LiCl水溶
液は、脱水により濃縮,再生される。このように、タン
ク4内のLiCl水溶液Lを加熱して水分の沸騰で再生を
行なうので、図5で述べたポンプ36,ヒータ35,フ
ァン34付きの濃縮ユニット33を介設した配管37に
LiCl水溶液を循環させて濃縮,再生する場合に比し
て、装置の構成が簡素化し、コストダウンが図れるう
え、加熱LiCl水溶液の放熱による損失が著しく少なく
なるので、再生時のエネルギ効率が、図5での50%か
ら略90%までに大幅に向上する。なお、上記実施例で
は、安価な夜間電力を用いて再生を行なうので、ランニ
ングコストが低減できるうえ、タンク4を断熱材13で
覆っているので、放熱ロスが一層低減するという利点が
ある。
Next, when regenerating the LiCl aqueous solution in the tank 4 having a low concentration due to water absorption at night by using inexpensive night power, the cooler 8 and the pump 9 are deactivated and the opening / closing valve 12 is opened. Close and feed the LiCl aqueous solution pipe 6, return pipe 7
The heater 5 is operated without circulating it. Then, the LiCl aqueous solution L in the tank 4 is heated to a predetermined high temperature (for example, 140 to 150 ° C.), and the water contained in the LiCl aqueous solution boils as shown in FIG. Released into the atmosphere, the LiCl aqueous solution is concentrated and regenerated by dehydration. As described above, since the LiCl aqueous solution L in the tank 4 is heated to be regenerated by boiling water, the LiCl is connected to the pipe 37 having the pump 36, the heater 35, and the concentration unit 33 with the fan 34 described in FIG. As compared with the case of concentrating and regenerating the aqueous solution by circulating it, the structure of the apparatus can be simplified, the cost can be reduced, and the loss due to the heat radiation of the heating LiCl aqueous solution can be remarkably reduced. From 50% to about 90%. In addition, in the above-mentioned embodiment, since the regeneration is performed by using the cheap nighttime electric power, the running cost can be reduced, and the heat dissipation loss is further reduced because the tank 4 is covered with the heat insulating material 13.

【0018】ヒータ5の加熱でタンク4内のLiCl水溶
液Lから水分が沸騰するのに伴って、図1の矢印で示す
ように、LiCl水溶液が液面から外へ飛散するが、飛散
するLiCl水溶液は、蓋14や直角に屈曲する排気ダク
ト15で遮られ、排気ダクト内に図3(A)の如き隔離板
18を設けた場合は、さらにこの隔離板18で遮られて
外部に殆んど出なくなり、外部の機器等がLiCl水溶液
で腐食される虞もなくなる。また、排気ダクト15の先
端部19を、図3(B)に示すようにU字状に屈曲させ
て、水槽20の水Wの中に浸せば、外部へ出ようとする
LiCl水溶液は、水中に総て捕らえられて、外部へ全く
放出されなくなる。従って、LiCl水溶液の放出による
問題は皆無になる。
As the water is boiled from the LiCl aqueous solution L in the tank 4 by the heating of the heater 5, the LiCl aqueous solution scatters from the liquid surface to the outside as shown by the arrow in FIG. 1, but the scattered LiCl aqueous solution. Is shielded by the lid 14 and the exhaust duct 15 which is bent at a right angle, and when a separator 18 as shown in FIG. 3A is provided in the exhaust duct, it is further shielded by the separator 18 and almost completely exposed to the outside. It does not come out, and there is no risk of external equipment being corroded by the LiCl aqueous solution. Further, when the tip portion 19 of the exhaust duct 15 is bent in a U shape as shown in FIG. 3 (B) and immersed in the water W in the water tank 20, the LiCl aqueous solution that is going out to the outside is All of them are captured and never released to the outside. Therefore, there is no problem due to the release of the LiCl aqueous solution.

【0019】さらに、図4(A)で述べたように、ポンプ
9の送液流量Qを、制御器10によって運転初期および
運転終期に多くし,その他の時期に少なくするように制
御しているので、送液流量Qが一定の場合に比して、起
動時の除湿能力の立ち上がりを急峻にし、運転終期の除
湿能力の急減を防止し、略均一な除湿能力でもって比較
的長時間に亘る除湿運転が可能になる。
Further, as described with reference to FIG. 4 (A), the liquid feed flow rate Q of the pump 9 is controlled by the controller 10 so as to be increased at the beginning and end of the operation and decreased at other times. Therefore, compared with the case where the liquid supply flow rate Q is constant, the dehumidifying capacity at the start-up is made sharper, the dehumidifying capacity at the end of the operation is prevented from decreasing sharply, and the dehumidifying capacity is substantially uniform for a relatively long time. Dehumidification operation becomes possible.

【0020】[0020]

【発明の効果】以上の説明で明らかなように、請求項1
の吸湿液体を用いた除湿再生装置は、水蒸気透過膜を通
してこの膜の一方に循環する吸湿液体に、上記膜の他方
に流れる室内空気に含まれる水分を吸収する除湿モジュ
ールと、ヒータを有して上記吸湿液体を貯えるタンク
と、上記吸湿液体が循環するように上記除湿モジュール
とタンクとを接続する送り配管および戻り配管と、吸湿
液体を圧送するポンプと、上記送り配管に介設され、循
環する吸湿液体を冷却する冷却器を備えているので、タ
ンク内の吸湿液体を総て冷却する場合に比して、冷却器
の小型化と低廉化が図れ、ポンプ,ヒータ,濃縮ユニット
を配管に介設した再生装置に比して、構成が簡素化し、
しかも放熱による損失が著しく少なくて再生時のエネル
ギ効率を大幅に向上させ、ひいては装置のランニングコ
ストを低減することができる。
As is apparent from the above description, claim 1
The dehumidifying and regenerating apparatus using the moisture absorbing liquid of No. 1 has a dehumidifying module for absorbing moisture contained in room air flowing to the other side of the membrane into the moisture absorbing liquid circulating through one of the membranes through the water vapor permeable membrane, and a heater. A tank that stores the hygroscopic liquid, a feed pipe and a return pipe that connect the dehumidifying module and the tank so that the hygroscopic liquid circulates, a pump that pumps the hygroscopic liquid under pressure, and a circulating pipe that is provided in the feed pipe. Since a cooler for cooling the hygroscopic liquid is provided, the cooler can be made smaller and less expensive than the case where all the hygroscopic liquid in the tank is cooled. Compared to the installed playback device, the configuration is simplified,
Moreover, the loss due to heat dissipation is extremely small, and the energy efficiency at the time of regeneration can be greatly improved, and the running cost of the device can be reduced.

【0021】請求項2の除湿再生装置では、送り配管の
冷却器よりも除湿モジュール側に、上記ポンプを介設し
ているから、ポンプに低温の吸湿液体が流れるので、ポ
ンプの腐食や故障を防止することができる。請求項3の
除湿再生装置では、タンクの上面が、先端部が所定角度
で屈曲する排気ダクトを立設した蓋で覆われているの
で、水分の沸騰に伴って液面から外へ飛散する吸湿液体
が、蓋や排気ダクトで遮られて外部へ殆んど出ず、吸湿
液体による外部の機器等の汚染や腐食を防ぐことがで
き、ヒータによる加熱効率も向上する。
In the dehumidifying / regenerating apparatus of the second aspect, since the pump is provided on the dehumidifying module side of the cooler of the feed pipe, a low-temperature hygroscopic liquid flows through the pump, so that the pump is not corroded or damaged. Can be prevented. In the dehumidifying / regenerating apparatus according to claim 3, since the upper surface of the tank is covered with a lid provided with an exhaust duct whose tip portion bends at a predetermined angle, moisture absorption that scatters from the liquid surface to the outside due to boiling of water. The liquid is almost not leaked to the outside by being blocked by the lid or the exhaust duct, and it is possible to prevent the external device or the like from being contaminated or corroded by the hygroscopic liquid, and the heating efficiency by the heater is improved.

【0022】請求項4の除湿再生装置では、タンクの上
面が排気ダクトを立設した蓋によって覆われており、排
気ダクトの内面に、隔離板が設けられているので、飛散
する吸湿液体が、隔離板で遮られて外部への放出が防止
され、吸湿液体による外部の機器等の汚染や腐食を防ぐ
ことができる。請求項5の除湿再生装置では、排気ダク
トの屈曲する先端部が、水槽の水中に浸されているの
で、吸湿液体は総て水中に捕らえられて、外部への放出
が皆無となる。
In the dehumidifying / regenerating apparatus of the fourth aspect, since the upper surface of the tank is covered by the lid in which the exhaust duct is erected, and the separator is provided on the inner surface of the exhaust duct, the hygroscopic liquid scattered is It can be prevented from being released to the outside by being shielded by the separator plate, and it is possible to prevent the external equipment or the like from being contaminated or corroded by the hygroscopic liquid. In the dehumidifying / regenerating apparatus of the fifth aspect, since the bent tip end portion of the exhaust duct is immersed in the water in the water tank, all the hygroscopic liquid is trapped in the water and is not discharged to the outside.

【0023】請求項6の除湿再生装置では、ポンプの送
液流量が、制御器によって運転初期に多くなるように制
御されるので、起動時の除湿能力の立ち上がりを急峻に
しつつ、長時間に亘って除湿運転を行なうことができ
る。請求項7の除湿再生装置では、制御器が、ポンプの
送液流量を運転終期においても多くなるように制御する
ので、吸湿液体の運転終期における除湿能力の急激な低
下が防止できる。
In the dehumidifying / regenerating apparatus according to the sixth aspect, the liquid feed flow rate of the pump is controlled by the controller so as to increase at the initial stage of the operation. The dehumidifying operation can be performed. In the dehumidifying / regenerating apparatus according to the seventh aspect, the controller controls the liquid supply flow rate of the pump so as to increase even at the end of the operation, so that the dehumidifying ability of the hygroscopic liquid at the end of the operation can be prevented from rapidly decreasing.

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

【図1】 本発明の吸湿液体を用いた除湿再生装置の一
実施例を示す構成図である。
FIG. 1 is a configuration diagram showing an embodiment of a dehumidifying / regenerating apparatus using a hygroscopic liquid according to the present invention.

【図2】 上記実施例の冷却器の具体例を示す図であ
る。
FIG. 2 is a diagram showing a specific example of the cooler of the above embodiment.

【図3】 上記実施例の排気ダクトの変形例を示す図で
ある。
FIG. 3 is a diagram showing a modification of the exhaust duct of the above embodiment.

【図4】 上記実施例のポンプの送液流量を変化させ、
または一定とした場合の除湿能力の時間変化を示す図で
ある。
FIG. 4 is a diagram showing the flow rate of the liquid fed by the pump of the above embodiment,
It is a figure which shows the time change of the dehumidification ability when making it constant.

【図5】 従来の除湿再生装置を示す構成図である。FIG. 5 is a configuration diagram showing a conventional dehumidifying / regenerating device.

【符号の説明】[Explanation of symbols]

1…除湿モジュール、2…容器、3…チューブ、4…タ
ンク、5…ヒータ、6…送り配管、7…戻り配管、8…
冷却器、9…ポンプ、10…制御器、14…蓋、15…
排気ダクト、18…隔離板、19…U字状の排気ダクト
の先端部、20…水槽、L…LiCl水溶液(吸湿液体)、
W…水。
1 ... Dehumidification module, 2 ... Container, 3 ... Tube, 4 ... Tank, 5 ... Heater, 6 ... Feed pipe, 7 ... Return pipe, 8 ...
Cooler, 9 ... Pump, 10 ... Controller, 14 ... Lid, 15 ...
Exhaust duct, 18 ... Separator plate, 19 ... Tip of U-shaped exhaust duct, 20 ... Water tank, L ... LiCl aqueous solution (hygroscopic liquid),
W ... water.

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 空気中の水分を吸湿液体(L)に吸収して
室内を除湿するとともに、吸水で希釈された吸湿液体
(L)から水分を除去して吸湿液体を再生する吸湿液体を
用いた除湿再生装置において、 水蒸気透過膜(3)を通してこの膜(3)の一方に循環する
上記吸湿液体(L)に、上記膜(3)の他方に流れる室内空
気に含まれる水分を吸収する除湿モジュール(1)と、 ヒータ(5)を有して上記吸湿液体(L)を貯えるタンク
(4)と、 上記吸湿液体(L)が循環するように上記除湿モジュール
(1)とタンク(4)とを接続する送り配管(6)および戻り
配管(7)と、 吸湿液体(L)を圧送するポンプ(9)と、 上記送り配管(6)に介設され、循環する吸湿液体(L)を
冷却する冷却器(8)を備えたことを特徴とする吸湿液体
を用いた除湿再生装置。
1. A hygroscopic liquid diluted with water while absorbing moisture in the air into the hygroscopic liquid (L) to dehumidify the room.
In a dehumidification / regeneration device using a hygroscopic liquid that removes water from (L) and regenerates the hygroscopic liquid, the hygroscopic liquid (L) circulating through the water vapor permeable membrane (3) to one of the membranes (3) is A dehumidifying module (1) that absorbs the water contained in the indoor air flowing through the other side of the membrane (3), and a tank that has a heater (5) and stores the above-mentioned hygroscopic liquid (L)
(4) and the dehumidifying module so that the hygroscopic liquid (L) circulates.
A feed pipe (6) and a return pipe (7) that connect the (1) and the tank (4), a pump (9) that pressure-feeds the hygroscopic liquid (L), and the feed pipe (6). A dehumidifying / regenerating apparatus using a hygroscopic liquid, comprising a cooler (8) for cooling the circulating hygroscopic liquid (L).
【請求項2】 上記ポンプ(9)を、上記送り配管(6)の
上記冷却器(8)よりも除湿モジュール(1)側に介設した
請求項1に記載の除湿再生装置。
2. The dehumidifying / regenerating apparatus according to claim 1, wherein the pump (9) is provided closer to the dehumidifying module (1) than the cooler (8) of the feed pipe (6).
【請求項3】 上記タンク(4)は、所定角度で先端部が
屈曲する排気ダクト(15)を立設した蓋(14)によって
上面が覆われている請求項1または2に記載の除湿再生
装置。
3. The dehumidifying regeneration according to claim 1, wherein the tank (4) has an upper surface covered with a lid (14) provided with an exhaust duct (15) whose tip portion bends at a predetermined angle. apparatus.
【請求項4】 上記タンクは、排気ダクト(15)を立設
した蓋(14)によって上面が覆われており、上記排気ダ
クト(15)の内面に、吸湿液体(L)の放出を防止する
隔離板(18)が設けられている請求項1または2に記載
の除湿再生装置。
4. The tank has an upper surface covered with a lid (14) provided with an exhaust duct (15), and prevents the hygroscopic liquid (L) from being discharged to the inner surface of the exhaust duct (15). The dehumidifying / regenerating apparatus according to claim 1 or 2, further comprising a separator (18).
【請求項5】 上記排気ダクト(15)の先端部(19)
は、屈曲していて、水槽(20)の水(W)中に浸されてい
る請求項3または4に記載の除湿再生装置。
5. A tip portion (19) of the exhaust duct (15)
The dehumidifying / regenerating apparatus according to claim 3 or 4, wherein is bent and is immersed in the water (W) in the water tank (20).
【請求項6】 上記ポンプ(9)の送液流量(Q)は、制御
器(10)によって運転初期に多くなるように制御される
請求項1に記載の除湿再生装置。
6. The dehumidifying / regenerating apparatus according to claim 1, wherein the liquid supply flow rate (Q) of the pump (9) is controlled by the controller (10) so as to increase at the initial stage of operation.
【請求項7】 上記制御器(10)は、上記ポンプ(9)の
送液流量(Q)を、運転終期においても多くなるように制
御する請求項6に記載の除湿再生装置。
7. The dehumidifying / regenerating apparatus according to claim 6, wherein the controller (10) controls the liquid supply flow rate (Q) of the pump (9) so as to increase even at the end of the operation.
JP5257017A 1993-10-14 1993-10-14 Dehumidification regenerator using hygroscopic liquid Pending JPH07108127A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5257017A JPH07108127A (en) 1993-10-14 1993-10-14 Dehumidification regenerator using hygroscopic liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5257017A JPH07108127A (en) 1993-10-14 1993-10-14 Dehumidification regenerator using hygroscopic liquid

Publications (1)

Publication Number Publication Date
JPH07108127A true JPH07108127A (en) 1995-04-25

Family

ID=17300582

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5257017A Pending JPH07108127A (en) 1993-10-14 1993-10-14 Dehumidification regenerator using hygroscopic liquid

Country Status (1)

Country Link
JP (1) JPH07108127A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1144439A (en) * 1997-07-28 1999-02-16 Daikin Ind Ltd Air conditioner
WO2002044624A1 (en) * 2000-12-01 2002-06-06 Daimlerchrysler Ag Device for continuously humidifying and dehumidifying additional air from manufacturing processes and ventilating and air conditioning systems
US8051602B2 (en) * 2005-11-02 2011-11-08 Nederlandse Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek Tno System for conditioning crops
WO2013038707A1 (en) * 2011-09-16 2013-03-21 ダイキン工業株式会社 Humidity control device
CN103185379A (en) * 2013-03-29 2013-07-03 江苏大学 Novel solar energy liquid dehumidifying air-conditioning system and implementation method
JP2014126345A (en) * 2012-12-27 2014-07-07 Daikin Ind Ltd Humidity controller
JP2014129930A (en) * 2012-12-28 2014-07-10 Daikin Ind Ltd Humidity control module and humidity controller including the same

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH1144439A (en) * 1997-07-28 1999-02-16 Daikin Ind Ltd Air conditioner
WO2002044624A1 (en) * 2000-12-01 2002-06-06 Daimlerchrysler Ag Device for continuously humidifying and dehumidifying additional air from manufacturing processes and ventilating and air conditioning systems
US6887303B2 (en) 2000-12-01 2005-05-03 Daimlerchrysler Ag Device for continuously humidifying and dehumidifying feed air
US8051602B2 (en) * 2005-11-02 2011-11-08 Nederlandse Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek Tno System for conditioning crops
WO2013038707A1 (en) * 2011-09-16 2013-03-21 ダイキン工業株式会社 Humidity control device
JP2013076559A (en) * 2011-09-16 2013-04-25 Daikin Industries Ltd Humidity controlling device
CN103782108A (en) * 2011-09-16 2014-05-07 大金工业株式会社 Humidity control device
US9874365B2 (en) 2011-09-16 2018-01-23 Daikin Industries, Ltd. Humidity control apparatus
JP2014126345A (en) * 2012-12-27 2014-07-07 Daikin Ind Ltd Humidity controller
JP2014129930A (en) * 2012-12-28 2014-07-10 Daikin Ind Ltd Humidity control module and humidity controller including the same
CN103185379A (en) * 2013-03-29 2013-07-03 江苏大学 Novel solar energy liquid dehumidifying air-conditioning system and implementation method
CN103185379B (en) * 2013-03-29 2015-01-07 江苏大学 Novel solar energy liquid dehumidifying air-conditioning system and implementation method

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