JPS61230719A - Dehumidifier - Google Patents
DehumidifierInfo
- Publication number
- JPS61230719A JPS61230719A JP60069965A JP6996585A JPS61230719A JP S61230719 A JPS61230719 A JP S61230719A JP 60069965 A JP60069965 A JP 60069965A JP 6996585 A JP6996585 A JP 6996585A JP S61230719 A JPS61230719 A JP S61230719A
- Authority
- JP
- Japan
- Prior art keywords
- air
- adsorbent
- absorbent
- dehumidification
- dehumidified
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-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
- F24F3/12—Air-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
- F24F3/14—Air-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
- F24F3/1411—Air-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
- F24F3/1417—Air-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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-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
- F24F3/12—Air-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
- F24F3/14—Air-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
- F24F3/1411—Air-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
- F24F3/1423—Air-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 a moving bed of solid desiccants, e.g. a rotary wheel supporting solid desiccants
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F2203/00—Devices or apparatus used for air treatment
- F24F2203/10—Rotary wheel
- F24F2203/1004—Bearings or driving means
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F2203/00—Devices or apparatus used for air treatment
- F24F2203/10—Rotary wheel
- F24F2203/1016—Rotary wheel combined with another type of cooling principle, e.g. compression cycle
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F2203/00—Devices or apparatus used for air treatment
- F24F2203/10—Rotary wheel
- F24F2203/1032—Desiccant wheel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F2203/00—Devices or apparatus used for air treatment
- F24F2203/10—Rotary wheel
- F24F2203/1056—Rotary wheel comprising a reheater
- F24F2203/106—Electrical reheater
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F2203/00—Devices or apparatus used for air treatment
- F24F2203/10—Rotary wheel
- F24F2203/1068—Rotary wheel comprising one rotor
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F2203/00—Devices or apparatus used for air treatment
- F24F2203/10—Rotary wheel
- F24F2203/1084—Rotary wheel comprising two flow rotor segments
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Gases (AREA)
Abstract
Description
【発明の詳細な説明】
（産業上の利用分野）
本発明は、冷却除湿と吸着（吸収）除湿とを組合せた除
湿装置に関し、圧縮空気用除湿機、空調用除湿機などに
適用する除湿装置に関する。Detailed Description of the Invention (Field of Industrial Application) The present invention relates to a dehumidification device that combines cooling dehumidification and adsorption (absorption) dehumidification, and is applicable to compressed air dehumidifiers, air conditioning dehumidifiers, etc. Regarding.
（従来の技術）
第５図は、従来の吸着式除湿装置を示す図である。従来
装置は、第３図に示すように、除湿塔は１と１′の２つ
有り、又替に除湿と再生を切換えて連続的に除湿するこ
とができるようになっている。除湿塔１，１″には吸着
剤２，２′が充填されており、吸着剤２．２′に接する
ように冷却器５，３があり、この冷却器３，５は除湿に
よる吸着熱を冷やす為にあり、冷却水の配管には弁８，
９が有って除湿している塔の冷却器に冷却水を流すよう
にＩＩＩＩ成されている。(Prior Art) FIG. 5 is a diagram showing a conventional adsorption type dehumidifier. As shown in FIG. 3, the conventional device has two dehumidification towers, 1 and 1', and can perform continuous dehumidification by switching between dehumidification and regeneration. The dehumidifying towers 1, 1'' are filled with adsorbents 2, 2', and there are coolers 5, 3 in contact with the adsorbents 2, 2'. It is for cooling, and the cooling water pipe has valve 8,
9 is installed so that cooling water flows into the cooler of the dehumidifying tower.
再生は加熱器５で空気を昇温して吸着剤２゜２′の水分
を蒸発させる。高圧空気の一部をエジェクタ４に通し、
大量の再生空気を吸入して加熱器５へ送る。なお、除湿
と再生の切換の為に四方弁６，７が配設されている。In the regeneration, the temperature of the air is raised by the heater 5 to evaporate the moisture in the adsorbent 2.2'. A part of the high pressure air is passed through the ejector 4,
A large amount of regenerated air is sucked in and sent to the heater 5. Note that four-way valves 6 and 7 are provided for switching between dehumidification and regeneration.
従来の除湿装置は、上記したように、再生の為に加熱器
があり、これは電気ヒータ、蒸気ヒータであるが、エネ
ルギー消費量が大きい欠点を有している。また、高圧空
気の入口の湿度が高い場合には除湿能力が不足してくる
ので、不足を見込んだ大きな装置となり、費用もかかる
欠点を有している。As mentioned above, conventional dehumidification devices include a heater for regeneration, which can be an electric heater or a steam heater, but has the drawback of large energy consumption. Furthermore, if the humidity at the inlet of the high-pressure air is high, the dehumidification capacity will be insufficient, so the device will need to be large and expensive to accommodate the shortage.
（発明が解決しようとする問題点）
本発明は、従来装置の上記欠点を解消し、省エネルギー
と高能力を有する除湿装置を提供することを目的とする
。(Problems to be Solved by the Invention) An object of the present invention is to eliminate the above-mentioned drawbacks of conventional devices and provide a dehumidifying device that saves energy and has high performance.
（問題点を解決するための手段）
そして、本発明に、上記目的を達成する手段として、処
理側を冷却除湿し、それを熱源としたヒートポンプで再
生を行うようにしたものである。すなわち、本発ＢＡは
、吸収剤又は吸着剤を用いて吸湿し、吸湿した吸収剤又
は吸着剤を加熱して再生するようにした除湿装置におい
て、前記吸収剤又は吸着剤により吸湿される前の空気と
熱交換して同空気を冷却除湿する蒸発器と、前記吸収剤
又は吸着剤を加熱再生する空気と熱交換して同空気を加
熱する凝縮器とからなるヒートポンプを設けたことを特
徴とする除湿装置である。(Means for Solving the Problems) In the present invention, as a means to achieve the above object, the processing side is cooled and dehumidified, and regeneration is performed using a heat pump using this as a heat source. That is, the BA of the present invention is a dehumidifying device that absorbs moisture using an absorbent or adsorbent and heats and regenerates the absorbed absorbent or adsorbent. It is characterized by being equipped with a heat pump consisting of an evaporator that cools and dehumidifies the air by exchanging heat with the air, and a condenser that heats the air by exchanging heat with the air that heats and regenerates the absorbent or adsorbent. This is a dehumidifying device.
本発明では、除湿機において、処理側の空気をまず冷却
式除湿をし、その後吸着または吸収で除湿する。また、
吸着剤または吸収剤の再生に、本発明では、冷却式除湿
をした冷凍機の凝縮器の放熱を用いる工う罠したもので
ある。In the present invention, in the dehumidifier, air on the processing side is first subjected to cooling dehumidification, and then dehumidified by adsorption or absorption. Also,
In the present invention, the heat dissipation from the condenser of a refrigerator with cooling type dehumidification is used to regenerate the adsorbent or absorbent.
以下、本発明の実施例金あげて、本発明の詳細な説明す
る。Hereinafter, the present invention will be explained in detail by giving examples of the present invention.
〔実施例１〕
第１図は本発明の実施例１を示す図であって、２塔切換
方式の例を示す。この除湿装置に、エジェクタ４、蒸発
器（冷却器）１１、凝縮器（加熱器）１２、補助ヒータ
１６、（冷媒）圧縮機１８、キャピラリチーブ等の減圧
機構１９、ドレンパン２０、除湿塔２１．２１’、吸着
剤又は吸収剤２２．２２’、四方弁２５．２４よフ構成
されている。[Embodiment 1] FIG. 1 is a diagram showing Embodiment 1 of the present invention, and shows an example of a two-column switching system. This dehumidification device includes an ejector 4, an evaporator (cooler) 11, a condenser (heater) 12, an auxiliary heater 16, a (refrigerant) compressor 18, a pressure reducing mechanism 19 such as a capillary chive, a drain pan 20, a dehumidification tower 21. 21', an adsorbent or absorbent 22, 22', and a four-way valve 25, 24.
上記除湿装置には、除湿塔は２つあシ、除湿と再生を交
互に切換えて連続的に除湿できる。The dehumidification device has two dehumidification towers, and can dehumidify continuously by alternately switching between dehumidification and regeneration.
除湿塔２１．２１’ににシリカゲル、活性炭等の吸着剤
又は塩化カルシウム等の吸収剤２２．２２がカートリッ
ジ状またはバラに納められている。In the dehumidification tower 21.21', an adsorbent such as silica gel or activated carbon or an absorbent 22.22 such as calcium chloride is stored in a cartridge shape or in bulk.
冷媒回路は圧縮機１８、蒸発器１１、凝縮器１２、減圧
機構１９を主構成部品とする冷媒圧縮式のヒートポンプ
を構成している。The refrigerant circuit constitutes a refrigerant compression type heat pump whose main components are a compressor 18, an evaporator 11, a condenser 12, and a pressure reduction mechanism 19.
この除湿装置において、除湿塔２１が除湿、２１′が再
生の場合を説明する。（なお、逆の時は四方弁２５．２
４が切換シ、破線矢印の方向に流路を形成する。）
空気圧縮機より送られた空気は、蒸発器１１により冷却
され、水分が結霧し、凝縮水としてドレンパン２０に集
められて排出される。冷却除湿された９気は四方弁２３
を通って除湿塔２１に入る。In this dehumidification device, a case will be explained in which the dehumidification tower 21 is used for dehumidification and the dehumidification tower 21' is used for regeneration. (In addition, in the case of reverse, the four-way valve 25.2
4 is a switching point and forms a flow path in the direction of the broken line arrow. ) The air sent from the air compressor is cooled by the evaporator 11, water is atomized, and the condensed water is collected in the drain pan 20 and discharged. The cooled and dehumidified 9 air is passed through the four-way valve 23.
It passes through and enters the dehumidification tower 21.
除湿塔２１の中の吸着剤また扛吸収剤２２でさらに除湿
されて四方弁２４を通って除湿空気として送シ出す。The air is further dehumidified by the adsorbent or filter absorbent 22 in the dehumidifying tower 21 and sent out through the four-way valve 24 as dehumidified air.
一方、再生空気はエジェクタ４で空気を吸入して風量が
多くなシ、圧力が下がって凝縮器１２に送られ、加熱さ
れて温度の高い空気となる。On the other hand, the regenerated air is sucked in by the ejector 4, the air volume is large, the pressure is reduced, and the air is sent to the condenser 12, where it is heated and becomes high-temperature air.
なお、補助ヒータ１６はさらに温度を高くする必要があ
る場合のみに設けて、温度コント０−ルする場合がめる
。温度の高い空気は四方弁２４を通り、除湿塔２１′に
入り、中の吸着剤または吸収剤２２′の水分を蒸発させ
、四方弁２３を通って湿つ危空気は排出される。冷媒回
路の機能は、低温側から高温側に熱を移動させる所にあ
る。圧縮機１８に吸入された低圧の冷媒は圧縮されて、
高温・高圧のガスとなり凝縮器１２に行き、放熱するこ
とによって冷媒は凝縮する。Note that the auxiliary heater 16 is provided only when it is necessary to further increase the temperature to control the temperature. The high-temperature air passes through the four-way valve 24 and enters the dehumidification tower 21' to evaporate the moisture in the adsorbent or absorbent 22' therein, and the humid hazardous air is discharged through the four-way valve 23. The function of the refrigerant circuit is to move heat from the low temperature side to the high temperature side. The low pressure refrigerant sucked into the compressor 18 is compressed,
The refrigerant becomes a high-temperature, high-pressure gas, goes to the condenser 12, and radiates heat, thereby condensing the refrigerant.
液化し九冷媒は減圧機構１９で減圧されて、蒸発器１１
へ行き、Ｉ９媒な吸熱゛して蒸発し、圧縮機１８に戻る
。The liquefied refrigerant is depressurized by the decompression mechanism 19 and transferred to the evaporator 11.
The I9 medium absorbs heat and evaporates, and returns to the compressor 18.
〔実施例２〕
第２図は本発明の実施例２を示す図であって、ロータ方
式の例を示す。この除湿装置は、エジェクタ４、蒸発器
（冷却・器）１１、凝縮器（加熱器）１２、除湿容器１
３、吸着剤又は吸収剤のロータ１４、駆動モータ１５、
補助ヒータ１６、空気熱交換器１７、（冷媒）圧縮機１
８、キャピラリチーブ等の減圧機構、ドレンパン２０よ
り構成されている。[Embodiment 2] FIG. 2 is a diagram showing Embodiment 2 of the present invention, and shows an example of a rotor system. This dehumidification device includes an ejector 4, an evaporator (cooler/container) 11, a condenser (heater) 12, and a dehumidification container 1.
3. Adsorbent or absorbent rotor 14, drive motor 15,
Auxiliary heater 16, air heat exchanger 17, (refrigerant) compressor 1
8, a pressure reducing mechanism such as a capillary tube, and a drain pan 20.
この除湿装置は、ロータ１４が回転することによル除湿
と再生とをくシ返すものである。口−タ１４は回転蓄熱
式熱交換器と同様な構造のものであり、蓄熱材のかわシ
に吸着剤又は吸収剤が使用されているものであって、ハ
ニカム式、乾式と称されているものである。This dehumidifying device alternates dehumidification and regeneration by rotating the rotor 14. The port 14 has a similar structure to a rotary regenerative heat exchanger, in which an adsorbent or absorbent is used for the heat storage material, and is called a honeycomb type or dry type. It is something.
この除湿装置において、空気圧縮機で圧縮されたを気は
本装置に入シ、一方は蒸発器１１へ行く処理側系統に入
り、一方はエジェクタ４ｔ−通り再生側系統に入る。In this dehumidification device, air compressed by the air compressor enters the device, one of which enters the processing side system going to the evaporator 11, and one of which enters the regeneration side system through the ejector 4t.
まず、処理側から説明する。熱交換器１７で冷却後蒸発
器１１で除湿と冷却を受けた空気は熱交換器１７で加熱
後、除湿容器１５に入シ、ロータ１４の吸着剤、または
吸収剤でさらに除湿され、除湿空気として送シ出される
。なお、蒸発器１１で結露した水はドレンパン２０に集
め排出される。First, the processing side will be explained. After being cooled in the heat exchanger 17, the air is dehumidified and cooled in the evaporator 11. After being heated in the heat exchanger 17, the air enters the dehumidifying container 15, where it is further dehumidified by the adsorbent or absorbent in the rotor 14, and the air is dehumidified. It is sent as. Note that water condensed in the evaporator 11 is collected in a drain pan 20 and discharged.
一方再生１１１は、エジェクタ４で空気を吸入して風量
が多くなるが圧力は少し下がる。凝縮器１２で加熱され
て温度が上昇した空気線さらに補助ヒータ１６があれば
加熱されて除湿容器１３に入り、ロータ１４の再生側風
路を通り、吸着剤ま九は吸収剤を再生して排出される。On the other hand, in the regeneration 111, air is sucked in by the ejector 4, and the air volume increases, but the pressure decreases a little. The air line heated by the condenser 12 and raised in temperature is further heated by the auxiliary heater 16, enters the dehumidifying container 13, passes through the air passage on the regeneration side of the rotor 14, and the adsorbent regenerates the absorbent. be discharged.
ロータ１４は駆動モータ１５でゆつくフと回転されてお
り、除湿される所から再生される所にまた元に戻って除
湿される所へと連続的に移動している。The rotor 14 is slowly rotated by a drive motor 15, and continuously moves from a place where it is dehumidified to a place where it is regenerated and back again to a place where it is dehumidified.
実施例２では熱交換器１７を設けて熱回収し、効率を高
めているが、本発明ではこの熱交換器１７を配設しない
場合管も包含されるものであシ、また、実施例１におい
て、実施例２における熱交換器１７を配設し、効率を高
めることも可能であシ、これも本発明に包含されるもの
で６る。さらに、上記実施例１．２では圧縮空気用につ
いて説明したが、本発明は、空調用除湿機にも適用でき
るものでおり、これも本発明に包含されるものである。In Embodiment 2, a heat exchanger 17 is provided to recover heat and improve efficiency, but in the present invention, if this heat exchanger 17 is not provided, pipes are also included. In this case, it is also possible to arrange the heat exchanger 17 in Example 2 to increase the efficiency, and this is also included in the present invention. Furthermore, although the above-mentioned Example 1.2 describes the case for compressed air, the present invention can also be applied to a dehumidifier for air conditioning, and this is also included in the present invention.
本発明は、以上詳記したように、吸湿前の空気と熱交換
して同空気を冷却除湿する蒸発器と、吸収剤又μ吸着剤
を加熱再生する空気と熱交換して同空気を加熱する凝縮
器とからなるヒートポンプを配設したものであるから、
次の（１）〜（５）の顕著な効果が生ずるものである。As detailed above, the present invention includes an evaporator that cools and dehumidifies the air by exchanging heat with the air before moisture absorption, and an evaporator that heats the air by exchanging heat with the air that heats and regenerates the absorbent or μ-adsorbent. It is equipped with a heat pump consisting of a condenser that
The following remarkable effects (1) to (5) are produced.
（１）一旦、蒸発器で除湿するので、吸着剤または吸収
剤での除湿負荷が少なくなフ、吸着剤または吸収剤の量
を少なくできる。(1) Since dehumidification is first carried out in the evaporator, the dehumidifying load on the adsorbent or absorbent is small, and the amount of adsorbent or absorbent can be reduced.
（２） 冷却除湿で高露点温度域を除湿し、°低露点
温度域は吸着ないし吸収による除湿であり、適材適所で
ある。(2) Cooling dehumidification is used to dehumidify the high dew point temperature range, while dehumidification in the low dew point temperature range is by adsorption or absorption, which is the right material for the right place.
（３） 吸着剤または吸収剤に入る空気に冷却されて
いるので、吸着または吸収の能力が大きくなる。(3) Since the air entering the adsorbent or absorbent is cooled, the adsorption or absorption capacity is increased.
（４） ヒートポンプにより吸着剤または吸収剤全再
生するので加熱に要するエネルギーが少なくてすむ。(4) Since the adsorbent or absorbent is completely regenerated by the heat pump, less energy is required for heating.
（５）吸着剤または吸収剤の圧力は除湿側が再生側より
高いので、除湿しやすく、再生しやすくなる。(5) Since the pressure of the adsorbent or absorbent is higher on the dehumidification side than on the regeneration side, it becomes easier to dehumidify and regenerate.
第１図は本発明の実施例１を示す図であシ、第２図は同
冥施例２ｔ−示す図である。第３図は従来の吸着式除湿
装置を示す図である。
復代理人 内 １） 明
復代理人 萩 原 亮 −FIG. 1 is a diagram showing a first embodiment of the present invention, and FIG. 2 is a diagram showing a second embodiment of the same. FIG. 3 is a diagram showing a conventional adsorption type dehumidification device. Sub-agents 1) Meifuku agent Ryo Hagiwara -
Claims (1)
吸着剤を加熱して再生するようにした除湿装置において
、前記吸収剤又は吸着剤により吸湿される前の空気と熱
交換して同空気を冷却除湿する蒸発器と、前記吸収剤又
は吸着剤を加熱再生する空気と熱交換して同空気を加熱
する凝縮器とからなるヒートポンプを設けたことを特徴
とする除湿装置。In a dehumidifying device that absorbs moisture using an absorbent or adsorbent and heats and regenerates the absorbed absorbent or adsorbent, the absorbent or adsorbent absorbs moisture by exchanging heat with the air before being absorbed by the absorbent or adsorbent. A dehumidification device comprising a heat pump comprising an evaporator that cools and dehumidifies air, and a condenser that heats the air by exchanging heat with the air that heats and regenerates the absorbent or adsorbent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60069965A JPS61230719A (en) | 1985-04-04 | 1985-04-04 | Dehumidifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60069965A JPS61230719A (en) | 1985-04-04 | 1985-04-04 | Dehumidifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS61230719A true JPS61230719A (en) | 1986-10-15 |
Family
ID=13417871
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60069965A Pending JPS61230719A (en) | 1985-04-04 | 1985-04-04 | Dehumidifier |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61230719A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007301010A (en) * | 2006-05-09 | 2007-11-22 | Sharp Corp | Washing/drying machine |
| JP2012166128A (en) * | 2011-02-10 | 2012-09-06 | Jfe Engineering Corp | Dehumidifier |
| JP2012250136A (en) * | 2011-05-31 | 2012-12-20 | Orion Machinery Co Ltd | Compressed air dehumidifier |
| CN103134121A (en) * | 2013-02-19 | 2013-06-05 | 东南大学 | Membrane method dehumidification device and method based on vapor compression and solution absorption |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5647728B2 (en) * | 1974-02-01 | 1981-11-11 | ||
| JPS6053315A (en) * | 1983-09-02 | 1985-03-27 | Murata Mfg Co Ltd | Laminated type ceramic filter |
| JPS61167425A (en) * | 1985-01-19 | 1986-07-29 | Matsushita Electric Works Ltd | Dehumidifier |
| JPS61192324A (en) * | 1985-02-21 | 1986-08-26 | C K D Seiki Kk | Apparatus for dehumidifying compressed gas |
-
1985
- 1985-04-04 JP JP60069965A patent/JPS61230719A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5647728B2 (en) * | 1974-02-01 | 1981-11-11 | ||
| JPS6053315A (en) * | 1983-09-02 | 1985-03-27 | Murata Mfg Co Ltd | Laminated type ceramic filter |
| JPS61167425A (en) * | 1985-01-19 | 1986-07-29 | Matsushita Electric Works Ltd | Dehumidifier |
| JPS61192324A (en) * | 1985-02-21 | 1986-08-26 | C K D Seiki Kk | Apparatus for dehumidifying compressed gas |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007301010A (en) * | 2006-05-09 | 2007-11-22 | Sharp Corp | Washing/drying machine |
| JP2012166128A (en) * | 2011-02-10 | 2012-09-06 | Jfe Engineering Corp | Dehumidifier |
| JP2012250136A (en) * | 2011-05-31 | 2012-12-20 | Orion Machinery Co Ltd | Compressed air dehumidifier |
| CN103134121A (en) * | 2013-02-19 | 2013-06-05 | 东南大学 | Membrane method dehumidification device and method based on vapor compression and solution absorption |
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