JP2722086B2 - Multi-stage solution concentration controller for liquid absorption type dehumidifier - Google Patents

Multi-stage solution concentration controller for liquid absorption type dehumidifier

Info

Publication number
JP2722086B2
JP2722086B2 JP63276010A JP27601088A JP2722086B2 JP 2722086 B2 JP2722086 B2 JP 2722086B2 JP 63276010 A JP63276010 A JP 63276010A JP 27601088 A JP27601088 A JP 27601088A JP 2722086 B2 JP2722086 B2 JP 2722086B2
Authority
JP
Japan
Prior art keywords
liquid
air
temperature
solution concentration
tower
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.)
Expired - Fee Related
Application number
JP63276010A
Other languages
Japanese (ja)
Other versions
JPH02122810A (en
Inventor
富男 横溝
弘一 北原
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.)
Koito Industries Ltd
Original Assignee
Koito Industries Ltd
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Filing date
Publication date
Application filed by Koito Industries Ltd filed Critical Koito Industries Ltd
Priority to JP63276010A priority Critical patent/JP2722086B2/en
Publication of JPH02122810A publication Critical patent/JPH02122810A/en
Application granted granted Critical
Publication of JP2722086B2 publication Critical patent/JP2722086B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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
    • F24F2003/144Air-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)
  • Drying Of Gases (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、生殖形質の保存や、その他の貯蔵などで室
内空気を低温度かつ低湿度に保持するために使用する液
体吸収式除湿器の多段階溶液濃度制御装置に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a liquid absorption type dehumidifier used for keeping indoor air at low temperature and low humidity for preservation of reproductive traits and other storage. The present invention relates to a multi-stage solution concentration control device.

〔従来の技術〕[Conventional technology]

液体吸収式除湿装置は、吸湿性の水溶液を湿り空気と
接触させて空気中の水分を吸収し、除湿を行う装置であ
り、吸湿剤には塩化リチウムやトリエチレングリコール
などが使用される。
The liquid absorption type dehumidifying device is a device for absorbing moisture in the air by bringing a hygroscopic aqueous solution into contact with moist air to dehumidify, and lithium chloride, triethylene glycol or the like is used as a moisture absorbing agent.

塩化リチウム水溶液は、濃度と温度により平衡蒸気圧
が定まり、同一濃度では、温度と平衡蒸気圧は比例し、
同一温度では濃度と平衡蒸気圧は反比例する。これらの
関係は塩化リチウム水溶液平衡線図(第3図参照)に表
され、液の濃度と温度を決めることにより平衡蒸気圧に
相当する任意の露点湿度が得られる。第3図では、40%
濃度の液温25℃の平衡蒸気圧が4.0mmHgを示しており、
相当露点温度は−2℃である。湿り空気がこの液と完全
接触することにより、任意の露点温度が得られるという
ことである。
The equilibrium vapor pressure of a lithium chloride aqueous solution is determined by its concentration and temperature. At the same concentration, the temperature and the equilibrium vapor pressure are proportional,
At the same temperature, the concentration and the equilibrium vapor pressure are inversely proportional. These relationships are shown in a lithium chloride aqueous solution equilibrium diagram (see FIG. 3). An arbitrary dew point humidity corresponding to the equilibrium vapor pressure can be obtained by determining the concentration and temperature of the solution. In Fig. 3, 40%
The equilibrium vapor pressure at a liquid temperature of 25 ° C of the concentration indicates 4.0 mmHg,
The equivalent dew point temperature is -2 ° C. The complete contact of the humid air with this liquid means that any dew point temperature is obtained.

一般的な液体吸収式除湿装置は、調整塔、液タンク及
び再生塔で構成されており、空気と液を十分接触させる
ためのスプレーノズル、空気と液を冷却させるための冷
却器、送風器及び空気加熱器等により循環空気の温湿度
を調整する調整塔と、液ポンプにより液タンクの液位を
一定に保持する液位制御装置を有する液タンクと、外気
空気と液を十分に接触させるためのスプレーノズル、液
を加熱するための液加熱器及び送風器などを有する再生
塔とから構成され、吸湿剤を溶かした溶液を加熱し、再
生空気中に散布して調整塔の循環空気中から吸湿し、液
位増加した相当量分の水分を放出させ、タンク内の液位
を一定に保持することにより液位の濃度を一定に保持す
るようになっている。
A general liquid absorption type dehumidifier is composed of a regulating tower, a liquid tank and a regeneration tower, a spray nozzle for bringing air and liquid into sufficient contact, a cooler for cooling air and liquid, a blower and An adjustment tower that adjusts the temperature and humidity of circulating air with an air heater, a liquid tank with a liquid level control device that keeps the liquid level of the liquid tank constant by a liquid pump, and sufficient contact between the outside air and the liquid. And a regeneration tower having a liquid heater for heating the liquid, a blower, and the like.The solution in which the desiccant is dissolved is heated, and is dispersed in the regeneration air to be discharged from the circulation air of the adjustment tower. It absorbs moisture, releases a considerable amount of water whose liquid level has increased, and keeps the liquid level in the tank constant so that the concentration of the liquid level is kept constant.

そして、この種の液体吸収式除湿装置は、従来、生殖
形質の保存やその他貯蔵などで、室内空気を低温度かつ
低湿度に保持するための溶液の濃度と温度は夏期の最大
冷却、除湿負荷に基づいて決定し、年間を通して運転し
ていた。
Conventionally, this type of liquid absorption type dehumidifier has been used to maintain the indoor air at low temperature and low humidity for preservation of reproductive traits and other storage. Was determined based on and was driven throughout the year.

〔発明が解決しようとする課題〕[Problems to be solved by the invention]

しかし、夏季の最大負荷時に基づく溶液濃度で年間を
通して運転しており、冷却・除湿負荷の減少する中間期
や冬季においても、溶液の平衡蒸気圧の関係から、夏季
の最大負荷を基準とした溶液温度に保つ必要がある。こ
のため調整塔の循環空気は不必要に冷却され、再び加熱
してから室内に送気するようになり大きなエネルギーロ
スを生ずるという欠点を有していた。
However, since the operation is performed throughout the year at the solution concentration based on the maximum load in summer, even in the interim period and winter when the cooling and dehumidification load decreases, the solution based on the maximum load in summer is used due to the equilibrium vapor pressure of the solution. It is necessary to keep the temperature. For this reason, the circulating air in the regulating tower is unnecessarily cooled, heated again, and then sent into the room, resulting in a large energy loss.

本発明は、上記問題に鑑みて創案されたもので、中間
期や冬季など、冷却・除湿負荷の低減期において、不必
要な冷却と加熱によるエネルギーロスを防止する方法の
うち、シンプルかつ安価な方式で実現した液体吸収式除
湿器の多段階溶液濃度制御装置を提供することを目的と
するものである。
The present invention has been devised in view of the above-described problems, and includes a simple and inexpensive method for preventing energy loss due to unnecessary cooling and heating during a period of reduction of a cooling / dehumidifying load, such as an intermediate period or winter. It is an object of the present invention to provide a multi-stage solution concentration control device for a liquid absorption type dehumidifier realized by a method.

〔課題を解決するための手段〕[Means for solving the problem]

上記目的を達成するために、本発明に係る液体吸収式
除湿器の多段階溶液濃度制御装置は、外気温度又は溶液
温度若しくは調整塔冷却器出口空気温度等、冷却・除湿
負荷に比例する要素と、電極式液位制御器との組み合わ
せで多段階に液位を制御することにより、負荷低減期の
冷却・除湿負荷に相当する溶液濃度を自動選択して制御
することを要旨とするものであり、即ち、空気調整室を
循環する循環空気が経由する調整塔と、外気が経由する
再生塔と、上記調整塔と再生塔の溜液を集合する液タン
クと、上記調整塔と再生塔の空気に該液タンクから塩化
リチウム又はトリエチレングリコール等の吸湿剤溶液を
供給噴霧する吸湿剤溶液噴霧手段とから成る液体吸収式
除湿器において、上記再生塔側の吸湿剤溶液噴霧手段か
ら噴霧する吸湿剤溶液を加熱する液加熱手段を構成し、
外気温度又は上記吸湿剤溶液温度若しくは冷却器出口温
度等の冷却・除湿負荷に比例する要素と、上記液タンク
に設けた電極式液位検出器からの液位出力の双方により
溶液濃度を多段階に制御する多段階溶液濃度制御装置に
よって上記液加熱手段を制御する構造に成る。
In order to achieve the above object, the multi-stage solution concentration control device for a liquid absorption dehumidifier according to the present invention includes an element that is proportional to a cooling / dehumidifying load, such as an outside air temperature or a solution temperature or an air temperature at a regulating tower cooler outlet. By controlling the liquid level in multiple stages in combination with an electrode type liquid level controller, the gist is to automatically select and control the solution concentration corresponding to the cooling / dehumidifying load in the load reduction period. That is, a regulating tower through which circulating air circulates in the air regulating chamber, a regeneration tower through which outside air passes, a liquid tank for collecting the liquid in the regulating tower and the regeneration tower, and air in the regulating tower and the regeneration tower. A liquid absorbent dehumidifier comprising: a liquid desiccant spraying means for supplying and spraying a desiccant solution such as lithium chloride or triethylene glycol from the liquid tank to the desiccant sprayed from the desiccant solution spraying means on the regeneration tower side. Dissolution It constitutes a liquid heating means for heating the,
The concentration of the solution is multi-stepped by both the element proportional to the cooling / dehumidifying load such as the outside air temperature or the temperature of the desiccant solution or the outlet temperature of the cooler, and the liquid level output from the electrode type liquid level detector provided in the liquid tank. The above-described liquid heating means is controlled by a multi-stage solution concentration control device that controls the temperature.

〔作用〕[Action]

上記構成によれば、外気温度等の冷却・除湿負荷に比
例する要素を検出して高温域、中温域或いは低温域であ
るかの三段階を判断するロジック回路を構築する一方、
電極式液位検出器は、高液位、中液域及び低液域の三段
階を検出するロジック回路を構築し、更に双方のロジッ
ク回路を組み合わせ、三段階の液位制御を行うロジック
回路を構築して外気が高温域で冷却・除湿負荷が大きな
場合は高液位に、外気が中温域で冷却・除湿負荷が中間
の場合は中液位に、外気が低温域で冷却・除湿負荷が少
ない場合は低液位に成るよう、再生塔の液加熱器を制御
することにより、冷却・除湿負荷に見合った三段階の溶
液濃度が得られるものである。
According to the above configuration, a logic circuit that detects an element proportional to a cooling / dehumidifying load such as an outside air temperature and determines a three-stage of a high-temperature region, a medium-temperature region, or a low-temperature region is constructed.
The electrode type liquid level detector constructs a logic circuit that detects three levels of high liquid level, middle liquid area and low liquid area, and combines the two logic circuits to form a logic circuit that performs three levels of liquid level control If the cooling and dehumidification load is large in the high temperature area and the outside air is high, the liquid level is high when the outside air is in the middle temperature area and the cooling and dehumidification load is medium, and the cooling and dehumidification load is low in the low temperature area. By controlling the liquid heater of the regeneration tower so that the liquid level becomes low when the amount is small, a three-stage solution concentration suitable for the cooling / dehumidifying load can be obtained.

この結果、外気温度等を冷却・除湿負荷量の目安とし
てとらえ、三段階に区分した負荷域の中で、各々適正な
平衡蒸気圧に近似した濃度が自動選択され、調整塔循環
空気の過冷却量と再加熱量を抑制することによって省エ
ネルギーを実現することができる。
As a result, the temperature of the outside air, etc., is taken as a measure of the cooling / dehumidifying load, and the concentration approximating the appropriate equilibrium vapor pressure is automatically selected in the load area divided into three stages. By suppressing the amount and the amount of reheating, energy saving can be realized.

なお、調整段階は、三段階に限ることはなく多段階に
することで、省エネルギー効果を高めることが可能であ
ることはいうまでもない。
It is needless to say that the adjustment stage is not limited to three stages but can be made multistage to enhance the energy saving effect.

〔実施例〕〔Example〕

以下、本発明に係る液体吸収式除湿器の多段階溶液濃
度制御装置の一実施例を第1図及び第2図に従って説明
する。
An embodiment of a multi-stage solution concentration control device for a liquid absorption type dehumidifier according to the present invention will be described below with reference to FIGS.

第1図は、多段階溶液濃度制御装置を設けた液体吸収
式除湿器の概要図を示すものであり、調整塔1、再生塔
2,液タンク3及び多段階溶液濃度制御装置4から成る。
調整塔1は、空気調整室(室温・湿度を設定値に保持し
ようとする閉鎖又は半閉鎖的空間)5からの換気ダクト
51に連通する空気洗浄室11と、空気調整室5への給気ダ
クト52と連通する給気室12を下端で連通したU字型を成
しており、下端を調整側戻液パイプ31を介して液タンク
3に連通したものである。また、上記空気洗浄室11には
冷却機6の熱交換部61が設けられると共に、スプレーノ
ズル13を上記熱交換部61の上方に設け、該スプレーノズ
ル13を塩化リチウム液供給パイプ34の先端に連通し、液
ポンプ33を介して液タンク3の液中に連通して成る。
FIG. 1 shows a schematic diagram of a liquid absorption type dehumidifier provided with a multi-stage solution concentration control device.
2, comprising a liquid tank 3 and a multi-stage solution concentration control device 4.
The control tower 1 is provided with a ventilation duct from an air control room (closed or semi-closed space for maintaining room temperature and humidity at a set value).
An air cleaning chamber 11 communicating with 51 and an air supply chamber 12 communicating with an air supply duct 52 to the air adjustment chamber 5 are formed at the lower end thereof in a U-shape. This is in communication with the liquid tank 3 via Further, the air cleaning chamber 11 is provided with a heat exchange part 61 of the cooler 6, and the spray nozzle 13 is provided above the heat exchange part 61, and the spray nozzle 13 is provided at the tip of the lithium chloride liquid supply pipe 34. It communicates with the liquid in the liquid tank 3 via the liquid pump 33.

更に、14は、給気室12の上端に連通した給気ダクト52
の給気口に設けた空気加熱器であり、ブロア15によって
空気調整室5に調整した空気を供給する調整側構造Aを
構成してある。
Further, 14 is an air supply duct 52 communicating with the upper end of the air supply chamber 12.
The air heater provided at the air supply port of (1) constitutes an adjustment-side structure A for supplying the air adjusted by the blower 15 to the air adjustment chamber 5.

一方、再生塔2から成る再生側構造Bは、略L字状を
為している底部液溜め21を液タンク3と再生側戻液パイ
プ35を介して連通すると共に、下側の吸気口22にブロア
23を設けて該吸気口22から上部に開設した大気開放口24
方向(矢印C)に流通する気流を構成し、該上昇気流中
にスプレーノズル25を設ける。該スプレーノズル25は、
前記塩化リチウム液供給パイプ34と分岐したパイプの先
端に連通するもので、該分岐側の塩化リチウム液供給パ
イプ34の途中には、液加熱器7が介装してあり、該液加
熱器7は液タンク3に設けた液位センサ8と外気温度セ
ンサ9の入力情報によって作動する多段階溶液濃度制御
装置4からの駆動信号によって加熱温度を制御し供給す
る塩化リチウム液を所定値まで加熱上昇する。
On the other hand, the regeneration side structure B composed of the regeneration tower 2 communicates the substantially L-shaped bottom liquid reservoir 21 with the liquid tank 3 via the regeneration side return liquid pipe 35 and the lower intake port 22. To blower
An air opening port 24 provided at the upper part from the intake port 22 by providing
An airflow flowing in the direction (arrow C) is formed, and a spray nozzle 25 is provided in the upward airflow. The spray nozzle 25 is
A liquid heater 7 is interposed in the middle of the lithium chloride liquid supply pipe 34 on the branch side, and communicates with a tip of a pipe branched from the lithium chloride liquid supply pipe 34. The heating temperature is controlled by a driving signal from a multi-stage solution concentration control device 4 which is operated based on input information of a liquid level sensor 8 and an outside air temperature sensor 9 provided in a liquid tank 3, and a supplied lithium chloride solution is heated to a predetermined value. I do.

第2図に示すように、上記多段階溶液濃度制御装置4
は、多極式電極保持器81から長さを異にする複数の電極
棒82,82…を液タンク3に垂下した液位センサ8と接続
し、「高液位」、「中液位」、「低液位」を検知する液
位検出ロジック回路41と、外気温度センサ9と接続して
「高温度域」、「中温度域」、「低温度域」を検知する
温度域検出ロジック回路42と、液位検出ロジック回路41
と温度域検出ロジック回路42からのロジック信号によ
り、次のように液加熱器7を温度制御する多段階溶液濃
度制御ロジック回路43とから構成して成る。該多段階溶
液濃度制御ロジック回路43の制御は、 (1)外気が高温域で冷却・除湿負荷が大の場合は高液
位、 (2)外気が中温域で冷却・除湿負荷が中の場合は中液
位、 (3)外気が低温域で冷却・除湿負荷が少の場合は低液
位、 である。
As shown in FIG. 2, the multi-stage solution concentration controller 4
Are connected to the liquid level sensor 8 hanging down from the multi-pole electrode holder 81 to the liquid tank 3 with a plurality of electrode rods 82, 82. , A liquid level detection logic circuit 41 for detecting “low liquid level” and a temperature range detection logic circuit for detecting “high temperature range”, “medium temperature range” and “low temperature range” by connecting to the outside air temperature sensor 9 42 and liquid level detection logic circuit 41
And a multi-stage solution concentration control logic circuit 43 for controlling the temperature of the liquid heater 7 in accordance with a logic signal from the temperature range detection logic circuit 42 as follows. The multi-stage solution concentration control logic circuit 43 controls (1) a high liquid level when the outside air is in a high temperature range and a large cooling / dehumidification load, and (2) a case where the outside air is a medium temperature range and the cooling / dehumidification load is medium. Is the middle liquid level, and (3) is the low liquid level when the outside air is in a low temperature range and the cooling / dehumidifying load is small.

上記構成に成る液体吸収式除湿器の多段階溶液濃度制
御装置は、上記調整塔1においてスプレーノズル13から
噴出する塩化リチウム又はトリエチレングリコール等の
吸収剤aの霧を空気と十分に接触させると同時に、冷却
器6の熱交換部61によって吸収剤a溶液を冷却させ、更
に循環空気も冷却・除湿した後、空気加熱器14によって
加熱調節した空気をフロア15によって空気調節室5に送
気して循環空気の温湿度を調整する。一方再生塔2にお
いては、スプレーノズル25から噴出する液加熱器7によ
って加熱調整した吸湿剤aを噴霧し、ブロア23によって
供給される外気空気Eと該吸湿剤aを充分に接触させ
る。この結果、調整塔1の循環空気中から吸湿し、液タ
ンク3の増加した液位相当量分の水分を放出させ、該液
位タンク内の液位を一定に保持することにより溶液の濃
度を一定に保持し、これにより空気調整室5の循環空気
の温度と湿度を一定に制御保持することができる。
The multi-stage solution concentration control device of the liquid absorption type dehumidifier having the above-described configuration is configured such that the mist of the absorbent a such as lithium chloride or triethylene glycol ejected from the spray nozzle 13 in the adjusting tower 1 is sufficiently brought into contact with air. At the same time, the absorbent a solution is cooled by the heat exchange section 61 of the cooler 6 and the circulating air is also cooled and dehumidified, and then the air heated by the air heater 14 is sent to the air control chamber 5 by the floor 15. To adjust the temperature and humidity of the circulating air. On the other hand, in the regeneration tower 2, the moisture absorbent a heated and adjusted by the liquid heater 7 ejected from the spray nozzle 25 is sprayed, and the outside air E supplied by the blower 23 and the moisture absorbent a are sufficiently brought into contact. As a result, moisture is absorbed from the circulating air of the regulating tower 1 and water corresponding to the increased liquid level in the liquid tank 3 is released, and the concentration of the solution is maintained by keeping the liquid level in the liquid level tank constant. The temperature and humidity of the circulating air in the air conditioning chamber 5 can be controlled and maintained at a constant value.

〔発明の効果〕〔The invention's effect〕

本発明に係る液体吸収式除湿器の多段階溶液濃度制御
装置は、以上のように構成したから、外気温度を冷却・
除湿負荷量の目安としてとらえ、多段階に区分した負荷
域の中で、各々適正な平衡蒸気圧に近似した濃度が自動
選択され、調整塔循環空気の過冷却量と再加熱量を抑制
し、冷却・除湿負荷に見合った多段階の溶液濃度が得ら
れるため省エネルギーを実現することができるものであ
り、本発明実施後の効果は極めて大きい。
The multi-stage solution concentration control device for the liquid absorption dehumidifier according to the present invention is configured as described above,
Considering the dehumidification load amount as a guide, the concentration approximating the appropriate equilibrium vapor pressure is automatically selected in the load area divided into multiple stages, suppressing the supercooling amount and reheating amount of the circulating air in the regulating tower, Since a multi-stage solution concentration corresponding to the cooling / dehumidification load can be obtained, energy saving can be realized, and the effect after the present invention is implemented is extremely large.

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

第1図は本発明に係る液体吸収式除湿器の全体を示す概
要図、 第2図は本発明に係る液体吸収式除湿器の多段階溶液濃
度制御装置の一実施例を示すブロック系統図、 第3図は塩化リチウム水溶液平衡線図である。 1……調整塔、2……再生塔 3……液タンク 4……多段階溶液濃度制御装置 5……空気調整室、6……冷却機 7……液加熱器、8……液位センサ 9……外気温度センサ 41……液位検出ロジック回路 42……温度域検出ロジック回路 43……多段階溶液濃度制御ロジック回路
FIG. 1 is a schematic diagram showing the entirety of a liquid absorption type dehumidifier according to the present invention. FIG. 2 is a block diagram showing one embodiment of a multi-stage solution concentration control device for the liquid absorption type dehumidifier according to the present invention. FIG. 3 is an equilibrium diagram of a lithium chloride aqueous solution. DESCRIPTION OF SYMBOLS 1 ... Adjustment tower 2 ... Regeneration tower 3 ... Liquid tank 4 ... Multi-stage solution concentration control device 5 ... Air adjustment chamber, 6 ... Cooler 7 ... Liquid heater, 8 ... Liquid level sensor 9: outside air temperature sensor 41: liquid level detection logic circuit 42: temperature range detection logic circuit 43: multi-stage solution concentration control logic circuit

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】空気調整室を循環する循環空気が経由する
調整塔と、外気が経由する再生塔と、上記調整塔と再生
塔の溜液を集合する液タンクと、上記調整塔と再生塔の
空気に該液タンクから塩化リチウム又はトリエチレング
リコール等の吸湿剤溶液を供給噴霧する吸湿剤溶液噴霧
手段とから成る液体吸収式除湿器において、 上記再生塔側の吸湿剤溶液噴霧手段から噴霧する吸湿剤
溶液を加熱する液加熱手段を構成し、 外気温度又は上記吸湿剤溶液温度若しくは冷却器出口温
度等の冷却・除湿負荷に比例する要素と、上記液タンク
に設けた電極式液位検出器からの液位出力の双方により
溶液濃度を多段階に制御する多段階溶液濃度制御装置に
よって上記液加熱手段を制御することを特徴とする液体
吸収式除湿器の多段階溶液濃度制御装置。
1. A regulating tower through which circulating air circulates in an air regulating chamber, a regeneration tower through which outside air passes, a liquid tank for collecting the liquid in the regulating tower and the regeneration tower, the regulating tower and a regeneration tower A liquid absorbent dehumidifier comprising a liquid absorbent dehumidifier for supplying and spraying a desiccant solution such as lithium chloride or triethylene glycol from the liquid tank to the air of the liquid. A liquid heating means for heating the desiccant solution, an element proportional to a cooling / dehumidification load such as an outside air temperature or the desiccant solution temperature or a cooler outlet temperature, and an electrode type liquid level detector provided in the liquid tank A multi-stage solution concentration controller for a liquid absorption type dehumidifier, wherein the liquid heating means is controlled by a multi-stage solution concentration controller for controlling the solution concentration in multiple stages based on both of the liquid level outputs from the liquid.
JP63276010A 1988-11-02 1988-11-02 Multi-stage solution concentration controller for liquid absorption type dehumidifier Expired - Fee Related JP2722086B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63276010A JP2722086B2 (en) 1988-11-02 1988-11-02 Multi-stage solution concentration controller for liquid absorption type dehumidifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63276010A JP2722086B2 (en) 1988-11-02 1988-11-02 Multi-stage solution concentration controller for liquid absorption type dehumidifier

Publications (2)

Publication Number Publication Date
JPH02122810A JPH02122810A (en) 1990-05-10
JP2722086B2 true JP2722086B2 (en) 1998-03-04

Family

ID=17563526

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63276010A Expired - Fee Related JP2722086B2 (en) 1988-11-02 1988-11-02 Multi-stage solution concentration controller for liquid absorption type dehumidifier

Country Status (1)

Country Link
JP (1) JP2722086B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010036093A (en) * 2008-08-04 2010-02-18 Dyna-Air Co Ltd Humidity controller
CN109855198A (en) * 2017-11-30 2019-06-07 南京海桐环境科技有限公司 The accurate control method of solution humidifying Fresh air handling units
CN113639342A (en) * 2021-09-14 2021-11-12 北京联力源科技有限公司 Open type refrigeration system and refrigeration method

Also Published As

Publication number Publication date
JPH02122810A (en) 1990-05-10

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