JPS6223418A - Wet type dehumidifier - Google Patents
Wet type dehumidifierInfo
- Publication number
- JPS6223418A JPS6223418A JP60162604A JP16260485A JPS6223418A JP S6223418 A JPS6223418 A JP S6223418A JP 60162604 A JP60162604 A JP 60162604A JP 16260485 A JP16260485 A JP 16260485A JP S6223418 A JPS6223418 A JP S6223418A
- Authority
- JP
- Japan
- Prior art keywords
- evaporator
- heat
- heat exchange
- exchange coil
- dehumidifying
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
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
- F24F2003/144—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 dehumidification only
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、空気中の湿分を除湿液を用いて除去する湿式
除湿機に係り、とくに、除湿液の再生を省エネルギー的
に行えるようにした蒸気再圧縮ヒートポンプ再生式の湿
式除湿機の改善に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a wet dehumidifier that removes moisture from the air using a dehumidifying liquid, and particularly relates to a wet dehumidifier that uses a dehumidifying liquid to regenerate the dehumidifying liquid in an energy-saving manner. This invention relates to an improvement of a vapor recompression heat pump regeneration type humidifier.
従来より、大量の空気を除湿する装置として湿式除湿機
が多用されている。周知のように、従来の湿式除湿機は
、取入空気と除湿液（通常ＬｉＣｌ液が使用される）と
を気液接触させる除湿塔と。Conventionally, wet dehumidifiers have been widely used as devices for dehumidifying large amounts of air. As is well known, conventional wet dehumidifiers include a dehumidification tower that brings the intake air into gas-liquid contact with a dehumidifying liquid (usually LiCl liquid).
除湿液中の水分を除去する再生塔とからなるのが最も普
通であり、再生塔においては、熱源としての蒸気がその
中に供給されるコイルに除湿液を散液すると共にこの熱
交換部に数人外気を通気し。Most commonly, it consists of a regeneration tower that removes moisture from the dehumidifying liquid, and in the regenerating tower, the dehumidifying liquid is sprinkled onto a coil into which steam as a heat source is supplied, and at the same time, the dehumidifying liquid is dispersed into this heat exchange section. A few people ventilated the outside air.
コイルによって加熱される除湿液と数人外気とを気液接
触させることにより、除湿液中の水分を数人外気中に放
出するものであった。By bringing the dehumidifying liquid heated by the coil into gas-liquid contact with the outside air, the moisture in the dehumidifying liquid is released into the outside air.
湿式除湿機の運転には除湿液再生のための熱源が不可欠
であり、この熱源費用が運転費用の大半を占める。この
ため、再生効率を高めるべく、熱ａ蒸気との熱交換効率
の向上や廃熱回収などの様々な工夫が提案されているが
、それなりの設備を必要とするし、また大気中に放出さ
れる熱の全てを回収することは実際には難しく、設備費
用の点でもランニングコストの点でも負担増となるとい
う問題があった。また、このような再生塔による除湿液
再生方式は高圧蒸気が多量に存在する化学工場や精練所
では有利な面はあっても、熱源蒸気を別途製造しなけれ
ばならないところでは、この蒸気製造のための設備が余
分に必要となり、この設備に大きな負担がかかっていた
。A heat source for regenerating the dehumidifying liquid is essential for operating a wet dehumidifier, and the cost of this heat source accounts for most of the operating cost. Therefore, in order to increase the regeneration efficiency, various measures have been proposed, such as improving the efficiency of heat exchange with thermal a-steam and recovering waste heat, but these require certain equipment and are not released into the atmosphere. In practice, it is difficult to recover all of the heat generated by the system, which poses a problem in that it increases the burden on both equipment costs and running costs. In addition, although the dehumidifying liquid regeneration method using such a regeneration tower is advantageous in chemical factories and smelters where large amounts of high-pressure steam exist, in places where heat source steam must be separately produced, it is difficult to produce this steam. This required additional equipment, which placed a heavy burden on this equipment.
本発明は、前記のような問題点を解決すべく創案された
もので、取入空気と除湿液とを気液接触させる除ｌ！塔
に、除湿液中の水分を除去する再生装置を接続してなる
湿式除湿機において。The present invention has been devised to solve the above-mentioned problems, and is a method of eliminating air-liquid contact between intake air and dehumidifying liquid. In a wet dehumidifier in which a regenerator for removing moisture from a dehumidifying liquid is connected to a tower.
気密容器からなる蒸発器内に、その中の除湿液と接する
ように熱交換コイルを設置し、この蒸発器で発生した蒸
気を圧・縮する圧縮機を該蒸発器に接続すると共にこの
圧縮機で圧縮された流体を該熱交換コイルに導いてこの
熱交換コイルを凝縮器として機能させるヒートポンプを
構成し、このヒートポンプを前記の再生装置としたこと
を特徴とする湿式除湿機を提供するものである。この場
合に、蒸発器内の熱交換コイルには、外部より蒸気を補
助熱源として供給することができる。また蒸発器に入る
前の除湿液を、熱交換コイルから出た流体および蒸発器
から出た除ンＷ液と熱交換するようにすると一層の省エ
ネルギーを図ることができる。A heat exchange coil is installed in the evaporator, which is an airtight container, in contact with the dehumidifying liquid inside the evaporator, and a compressor that compresses and compresses the vapor generated in the evaporator is connected to the evaporator. The present invention provides a wet dehumidifier comprising a heat pump that guides fluid compressed by the heat exchange coil to the heat exchange coil to function as a condenser, and the heat pump is used as the regeneration device. be. In this case, steam can be supplied from the outside to the heat exchange coil in the evaporator as an auxiliary heat source. Further, if the dehumidifying liquid before entering the evaporator is heat exchanged with the fluid coming out of the heat exchange coil and the dehumidifying liquid coming out of the evaporator, further energy saving can be achieved.
以下に図面の実施例に従って本発明の湿式除湿機の内容
を具体的に説明する。The contents of the wet dehumidifier of the present invention will be specifically explained below according to the embodiments shown in the drawings.
第１図は本発明に従う湿式除湿機の全体示したものであ
る。１は除湿塔であり、これは従来と同様の構造のもの
が使用されている。すなわちこの除湿塔１においては、
充填物層２に向けて散液装置３から除湿液が散液され、
空気取入口４から塔内に導入された空気がこの充填物層
２を上昇する間に、除湿液と気液接触して除湿され、エ
リミネータ−５および熱交換器６を経て除湿空気７が取
り出される。本発明においては、除湿塔１については図
示の例に限らず従来のあらゆるものが使用可能である。FIG. 1 shows the entire wet dehumidifier according to the present invention. 1 is a dehumidification tower, which has the same structure as the conventional one. That is, in this dehumidification tower 1,
A dehumidifying liquid is sprinkled from the liquid dispersion device 3 toward the filling layer 2,
While the air introduced into the tower from the air intake port 4 rises through the packed layer 2, it comes into contact with the dehumidifying liquid and is dehumidified, and the dehumidified air 7 is taken out through the eliminator 5 and the heat exchanger 6. It will be done. In the present invention, the dehumidification tower 1 is not limited to the illustrated example, and any conventional dehumidification tower can be used.
８は除湿液タンクであり、除湿塔１で湿分を吸収して希
釈された除湿液が管路９を経てこの除湿液タンク８に戻
される。そして、この除湿液タンク８内からポンプＩＯ
によって除湿液が汲み上げられ、主管路１１を経て除湿
塔１の散液装置３に送られる。この間に必要に応じて冷
却器１２を介装させておく。8 is a dehumidifying liquid tank, and the dehumidifying liquid that has been diluted by absorbing moisture in the dehumidifying tower 1 is returned to this dehumidifying liquid tank 8 via a pipe line 9. Then, from inside this dehumidifying liquid tank 8, the pump IO
The dehumidifying liquid is pumped up and sent to the liquid dispersion device 3 of the dehumidifying tower 1 via the main pipe 11. During this time, a cooler 12 is inserted as necessary.
除湿液タンク８内の除湿液は漸次水分が増加するのでこ
れを再生する必要があるが２本発明においては、ヒート
ポンプの蒸発器１３に給液してこの再生を行う。蒸発器
１３は、熱交換コイル１４がその中に設置された気密容
器であり、主管路１１を流れる除湿液の一部が往管１５
を経てこの版発器１３内に供給され、この蒸発器１３で
再生された除湿液は戻り管１６を経て除？Ｗ Ｈタンク
８に戻される。Since the moisture content of the dehumidifying liquid in the dehumidifying liquid tank 8 gradually increases, it is necessary to regenerate it. In the present invention, this regeneration is performed by supplying the liquid to the evaporator 13 of the heat pump. The evaporator 13 is an airtight container in which a heat exchange coil 14 is installed, and a portion of the dehumidifying liquid flowing through the main pipe 11 is transferred to the outgoing pipe 15.
The dehumidifying liquid that is supplied into the plate generator 13 through the evaporator 13 and regenerated in the evaporator 13 is removed through the return pipe 16. It is returned to the WH tank 8.
蒸発器１３内の熱交換コイル１４は蒸発器１３に供給さ
れた除湿液の液相１７と熱交換するように設置される。A heat exchange coil 14 in the evaporator 13 is installed to exchange heat with the liquid phase 17 of the dehumidifying liquid supplied to the evaporator 13.
一方、蒸発器１３の気相部分１８（蒸気）は管路１９に
よって圧ｌｌ１ｆａ２０に接続される。すなわち１蒸発
器１３にはここで発生する蒸気を取り出す管路１９を設
け、これを圧縮機２０の吸込側に接続する。On the other hand, the gas phase portion 18 (steam) of the evaporator 13 is connected to the pressure ll1fa20 by a pipe 19. That is, the first evaporator 13 is provided with a pipe line 19 for taking out the steam generated therein, and this pipe line 19 is connected to the suction side of the compressor 20.
そして、この圧縮機２０の吐出側の高圧管路２１を蒸発
器Ｉ３内の熱交換コイル１４に接続する。これによって
圧縮機２０を稼動すると、蒸発器１３内の蒸気が圧縮機
２０で圧縮されこの高圧茶気が熱交換コイル１４で凝縮
して放熱し、この放熱によって蒸発器１３内の除湿液か
ら蒸気が発生し、これが再び循環するというヒートポン
プを形成することになる。なお、熱交換コイル１４で凝
縮したドレンを含む流体は、管路２２を経て気水分離器
２３に送られ、ここでドレンと排気に分離される。ドレ
ンはドレン管２４によって系外に抜き出されるが、この
ドレンが除温液の再生によって除去された水分に相当す
ることになる。一方、気水分離器２３で分離された排気
は真空装置２５を経て大気に放出される。The high-pressure pipe line 21 on the discharge side of the compressor 20 is connected to the heat exchange coil 14 in the evaporator I3. When the compressor 20 is operated in this way, the steam in the evaporator 13 is compressed by the compressor 20, and this high-pressure brown gas is condensed in the heat exchange coil 14 and radiates heat. This generates a heat pump that circulates again. Note that the fluid containing the condensate condensed in the heat exchange coil 14 is sent to the steam/water separator 23 via the pipe line 22, where it is separated into condensate and exhaust gas. The drain is drawn out of the system through the drain pipe 24, and this drain corresponds to the water removed by regenerating the temperature removing liquid. On the other hand, the exhaust gas separated by the steam/water separator 23 is discharged to the atmosphere via the vacuum device 25.
なお、圧縮機２０から熱交換コイル１４に通ずる高圧管
路２１に蒸気管２５を接続し、この蒸気管２５を通して
外部より蒸気を供給するようにすると、この蒸気の熱が
蒸発器１３での蒸発熱源として利用され一層有利に蒸発
が進行し、圧縮機２０の負担を軽減することができる。Note that if a steam pipe 25 is connected to the high-pressure pipe 21 leading from the compressor 20 to the heat exchange coil 14 and steam is supplied from the outside through this steam pipe 25, the heat of this steam is evaporated in the evaporator 13. Utilized as a heat source, evaporation proceeds more advantageously, and the load on the compressor 20 can be reduced.
この補助蒸気も熱交換コイル１４で一部はドレンとなる
が、なおこのドレンが熱を保存する場合には、この熱を
熱交換器２６で版発器１３に入る前の除湿液に付与する
。この熱交換器２６には蒸発器１３から出る再生済みの
除湿液も通して、この再生済み除湿液が持つ熱も蒸発器
１３に入る前の除湿液に付与するようにするとよい、蒸
気管２５から供給される蒸気はあくまでヒートポンプを
補佐するものであり、主として始動時用に使用されるが
、運転中にも使用して再生に要するエネルギーの一部を
受は持つことができる。A portion of this auxiliary steam also becomes drain in the heat exchange coil 14, but if this drain stores heat, this heat is applied to the dehumidifying liquid before entering the plate generator 13 in the heat exchanger 26. . It is preferable that the regenerated dehumidifying liquid discharged from the evaporator 13 also be passed through the heat exchanger 26 so that the heat of the regenerated dehumidifying liquid is also imparted to the dehumidifying liquid before entering the evaporator 13. The steam supplied from the heat pump is only used to assist the heat pump, and is primarily used during startup, but it can also be used during operation to provide a portion of the energy required for regeneration.
第１図の実施例は、−個の蒸発器１３を使用するいわば
単缶単効用方式を示したが、これを、第２図または第３
図に示したように、多缶単効用方式または二重効用方式
に複数の蒸発器１３を接続して除湿液の再生を図ること
もできる。第２図および第３図において第１図と同じ数
字で示したものは第１図で説明したのと同じものに対応
している。The embodiment shown in FIG. 1 shows a so-called single-can single-effect system using - number of evaporators 13.
As shown in the figure, it is also possible to connect a plurality of evaporators 13 in a multi-can single-effect system or a dual-effect system to regenerate the dehumidifying liquid. In FIGS. 2 and 3, the same numbers as in FIG. 1 correspond to the same components as explained in FIG.
第２図の多缶単効用方式は、除湿液の濃縮比が大きく且
つ沸点上昇が大きい場合に有利であり。The multi-can single-effect system shown in FIG. 2 is advantageous when the concentration ratio of the dehumidifying liquid is large and the boiling point rise is large.
第３図の二重効用方式は、沸点上昇が比較的小さい場合
に有利である。また３図示しないが、三重効用方式、或
いは単効用方式と二重効用方式を組み合わせた単効用十
二重効用方式とすることもできる。前者の場合には、沸
点上昇がない場合に有利であり、後者の場合には、濃縮
比が太き（沸点上昇も比較的大きい場合に有利である。The dual effect system of FIG. 3 is advantageous when the boiling point increase is relatively small. Although not shown in the drawings, a triple effect system or a single effect and double effect system that combines a single effect system and a double effect system may also be used. In the former case, it is advantageous when there is no increase in the boiling point, and in the latter case, it is advantageous when the concentration ratio is large (the increase in the boiling point is also relatively large).
本発明による再生装置は、蒸発した水蒸気の潜熱を除湿
液の加熱に利用してドレンとして排出できる。従って１
従来の再生塔のように大気に放熱していた分をそっくり
熱回収ができる。これにより除湿液再生のための熱源は
少量でよくなり、多量の熱源用蒸気を製造しなくてもよ
い。このため熱源蒸気を入手しがたい場合や小型のボイ
ラーしか存在しない場合でも廉価な費用で連続再生式の
湿式除湿機を構成して稼動できることになるし。The regeneration device according to the present invention can utilize the latent heat of evaporated water vapor to heat the dehumidifying liquid and discharge it as drain. Therefore 1
It is possible to recover the entire amount of heat that would otherwise be radiated to the atmosphere as in conventional regeneration towers. As a result, a small amount of heat source is required for regenerating the dehumidifying liquid, and there is no need to produce a large amount of steam for the heat source. Therefore, even if heat source steam is difficult to obtain or only a small boiler is available, a continuous regeneration type humidifier can be constructed and operated at low cost.
また従来の再生塔に比べて大きな省エネルギーが達成さ
れる。Additionally, significant energy savings can be achieved compared to conventional regeneration towers.
第１図は本発明の湿式除湿機全体の機器配置系統図、第
２図は再生装置の他の実施例を示す機器配置系統図、第
３図は再生装置のさらに他の実施例を示す機器配置系統
図である。
１・・除湿塔１． ８・・除湿液タンク。
１３・・蒸発器、１４・・熱交換コイル。
２０・・圧縮機、２６・・熱交換器。Fig. 1 is an equipment layout system diagram of the entire wet dehumidifier of the present invention, Fig. 2 is an equipment arrangement system diagram showing another embodiment of the regeneration device, and Fig. 3 is an equipment arrangement diagram showing still another embodiment of the regeneration device. It is a layout system diagram. 1. Dehumidification tower 1. 8. Dehumidifying liquid tank. 13...Evaporator, 14...Heat exchange coil. 20... Compressor, 26... Heat exchanger.
Claims (3)
除湿液中の水分を除去する再生装置を接続してなる湿式
除湿機において、 気密容器からなる蒸発器内に、その中の除湿液と接する
ように熱交換コイルを設置し、この蒸発器で発生した蒸
気を圧縮する圧縮機を該蒸発器に接続すると共にこの圧
縮機で圧縮された流体を該熱交換コイルに導いてこの熱
交換コイルを凝縮器として機能させるヒートポンプを構
成し、このヒートポンプを前記の再生装置としたことを
特徴とする湿式除湿機。(1) A dehumidification tower that brings the intake air into gas-liquid contact with the dehumidifying liquid,
In a humid dehumidifier that is connected to a regeneration device that removes water from the dehumidifying liquid, a heat exchange coil is installed in the evaporator, which is an airtight container, in contact with the dehumidifying liquid inside the evaporator. A heat pump is configured in which a compressor for compressing vapor is connected to the evaporator, and the fluid compressed by the compressor is guided to the heat exchange coil to function as a condenser. A wet dehumidifier characterized by being a regenerating device.
て供給される特許請求の範囲第１項記載の湿式除湿機。(2) The wet dehumidifier according to claim 1, wherein steam is supplied to the heat exchange coil from the outside as an auxiliary heat source.
た流体および蒸発器から出た除湿液と熱交換される特許
請求の範囲第１項または第２項記載の湿式除湿機。(3) The wet dehumidifier according to claim 1 or 2, wherein the dehumidifying liquid before entering the evaporator exchanges heat with the fluid coming out of the heat exchange coil and the dehumidifying liquid coming out of the evaporator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60162604A JPH0659381B2 (en) | 1985-07-23 | 1985-07-23 | Wet dehumidifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60162604A JPH0659381B2 (en) | 1985-07-23 | 1985-07-23 | Wet dehumidifier |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6223418A true JPS6223418A (en) | 1987-01-31 |
| JPH0659381B2 JPH0659381B2 (en) | 1994-08-10 |
Family
ID=15757748
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60162604A Expired - Fee Related JPH0659381B2 (en) | 1985-07-23 | 1985-07-23 | Wet dehumidifier |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0659381B2 (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008045803A (en) * | 2006-08-14 | 2008-02-28 | Hachiyo Engneering Kk | Energy-saving air conditioning system |
| USD634414S1 (en) | 2010-04-27 | 2011-03-15 | Dri-Eaz Products, Inc. | Dehumidifier housing |
| US8290742B2 (en) | 2008-11-17 | 2012-10-16 | Dri-Eaz Products, Inc. | Methods and systems for determining dehumidifier performance |
| USD731632S1 (en) | 2012-12-04 | 2015-06-09 | Dri-Eaz Products, Inc. | Compact dehumidifier |
| US9089814B2 (en) | 2009-04-27 | 2015-07-28 | Dri-Eaz Products, Inc. | Systems and methods for operating and monitoring dehumidifiers |
| WO2016155678A1 (en) * | 2015-03-30 | 2016-10-06 | Francisco Javier Velasco Valcke | Device for the extraction of water from the environment |
| EP3135365A4 (en) * | 2014-04-22 | 2018-01-03 | Panacea Quantum Leap Technology LLC | Device for extracting water from the environment |
| CN109475807A (en) * | 2016-07-06 | 2019-03-15 | 瑞典空水绿集团控股公司 | Device and aerial cooler for continuous absorption water |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102000478A (en) * | 2010-10-29 | 2011-04-06 | 中国农业大学 | Dehumidification liquid regenerating method and device |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61164621A (en) * | 1985-01-17 | 1986-07-25 | Mitsubishi Heavy Ind Ltd | Apparatus for removing moisture or condensible gas |
| JPS61259728A (en) * | 1985-05-13 | 1986-11-18 | Konishiroku Photo Ind Co Ltd | Dehumidifying apparatus |
-
1985
- 1985-07-23 JP JP60162604A patent/JPH0659381B2/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61164621A (en) * | 1985-01-17 | 1986-07-25 | Mitsubishi Heavy Ind Ltd | Apparatus for removing moisture or condensible gas |
| JPS61259728A (en) * | 1985-05-13 | 1986-11-18 | Konishiroku Photo Ind Co Ltd | Dehumidifying apparatus |
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008045803A (en) * | 2006-08-14 | 2008-02-28 | Hachiyo Engneering Kk | Energy-saving air conditioning system |
| US8290742B2 (en) | 2008-11-17 | 2012-10-16 | Dri-Eaz Products, Inc. | Methods and systems for determining dehumidifier performance |
| US9089814B2 (en) | 2009-04-27 | 2015-07-28 | Dri-Eaz Products, Inc. | Systems and methods for operating and monitoring dehumidifiers |
| USD634414S1 (en) | 2010-04-27 | 2011-03-15 | Dri-Eaz Products, Inc. | Dehumidifier housing |
| USD731632S1 (en) | 2012-12-04 | 2015-06-09 | Dri-Eaz Products, Inc. | Compact dehumidifier |
| EP3135365A4 (en) * | 2014-04-22 | 2018-01-03 | Panacea Quantum Leap Technology LLC | Device for extracting water from the environment |
| US10295203B2 (en) | 2014-04-22 | 2019-05-21 | Panacea Quantum Leap Technology Llc | Device for extracting water from the environment |
| WO2016155678A1 (en) * | 2015-03-30 | 2016-10-06 | Francisco Javier Velasco Valcke | Device for the extraction of water from the environment |
| CN107847848A (en) * | 2015-03-30 | 2018-03-27 | 万能量子飞跃技术有限公司 | For extracting the device of water from environment |
| JP2018511469A (en) * | 2015-03-30 | 2018-04-26 | パナシア クァンタム リープ テクノロジー エルエルシー | Equipment for extracting water from the surroundings |
| US10675583B2 (en) | 2015-03-30 | 2020-06-09 | Panacea Quantum Leap Technology, LLC | Device for the extraction of water from the environment |
| CN109475807A (en) * | 2016-07-06 | 2019-03-15 | 瑞典空水绿集团控股公司 | Device and aerial cooler for continuous absorption water |
| EP3782713A1 (en) * | 2016-07-06 | 2021-02-24 | Drupps Group AB | Device for continuous water absorption and an air cooler |
| US11131468B2 (en) | 2016-07-06 | 2021-09-28 | Drupps Group Ab | Device for continuous water absorption and an air cooler |
| CN109475807B (en) * | 2016-07-06 | 2022-04-08 | 乔普思有限公司 | Device for continuously absorbing water and air cooler |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0659381B2 (en) | 1994-08-10 |
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| LAPS | Cancellation because of no payment of annual fees |