JP3302833B2 - Dehumidification method and dehumidification system - Google Patents
Dehumidification method and dehumidification systemInfo
- Publication number
- JP3302833B2 JP3302833B2 JP14847294A JP14847294A JP3302833B2 JP 3302833 B2 JP3302833 B2 JP 3302833B2 JP 14847294 A JP14847294 A JP 14847294A JP 14847294 A JP14847294 A JP 14847294A JP 3302833 B2 JP3302833 B2 JP 3302833B2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- storage
- lithium chloride
- liquid
- dehumidification
- 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
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
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)
Description
【0001】[0001]
【産業上の利用分野】本発明は、減湿方法及び減湿シス
テムに関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a dehumidification method and a dehumidification system.
【0002】[0002]
【従来の技術】従来の減湿(除湿)装置は、その減湿方
式によって冷却式、吸収式、吸着式、圧縮式に大別され
るが、その中で例えば吸収式減湿装置は、水分を吸収す
る性質を有する吸収剤と、処理空気とを接触させて空気
中の水分を除去する構成を有している。この場合、吸収
剤を溶液で使うものは湿式減湿装置、吸収剤を多孔質の
担体に含侵させて使うものは乾式減湿装置と呼ばれてい
る。2. Description of the Related Art Conventional dehumidification (dehumidification) devices are roughly classified into a cooling type, an absorption type, an adsorption type, and a compression type according to the dehumidification method. It has a configuration in which an absorbent having a property of absorbing water and treated air are brought into contact with each other to remove moisture in the air. In this case, a device using an absorbent in a solution is called a wet dehumidifier, and a device using an absorbent impregnated in a porous carrier is called a dry dehumidifier.
【0003】そして代表的な湿式減湿装置の構成につい
ていうと、従来のこの種の減湿装置は、処理空気に対し
て吸収液をノズル等で噴霧させて減湿処理を行う吸収器
と、水分を吸収して濃度がうすくなった吸収液を再生処
理する再生器とを有しており、吸収器においては水分吸
収の際に発生した熱を冷却コイル等で降温させ、他方再
生器においては、濃度が淡くなった吸収液を加熱コイル
で加熱して水分を蒸発させて濃度を濃くし、再び吸収器
側へと戻すようにしていた。[0003] Regarding the configuration of a typical wet dehumidifier, this type of conventional dehumidifier includes an absorber for performing a dehumidification process by spraying an absorption liquid onto a processing air with a nozzle or the like; A regenerator that regenerates the absorbing solution whose concentration has been reduced by absorbing moisture.In the absorber, the heat generated at the time of absorbing the water is cooled by a cooling coil or the like, and in the regenerator, The absorption liquid whose concentration has been reduced is heated by a heating coil to evaporate water to increase the concentration and return to the absorber side.
【0004】[0004]
【発明が解決しようとする課題】ところで前記した吸収
式減湿装置は、主として昼間運転されており、そのため
運転費が高くつき、特に再生運転の際に要する費用がか
さみ、減湿装置の使用に大きな障害となっていた。これ
は吸収器側で冷却を行うための冷却水と、再生器側で加
熱するための蒸気とを各々用意しなければならず、熱源
の種類を多とし、その結果装置の運転コストが高くつく
ものとなっていたのである。However, the above-mentioned absorption type dehumidifier is operated mainly in the daytime, so that the operation cost is high, and especially the cost required for the regeneration operation is high, and the use of the dehumidifier is difficult. It was a major obstacle. This requires the provision of cooling water for cooling on the absorber side and steam for heating on the regenerator side, which increases the number of types of heat sources, resulting in high operating costs of the apparatus. It had become something.
【0005】本発明はかかる点に鑑みてなされたもので
あり、安価な夜間電力を利用して夜間時に蓄冷して、昼
間時の減湿(除湿)運転の際の冷源とするような構成を
持たせて、前記問題の解決を図ることを目的とするもの
である。The present invention has been made in view of the above points, and has a configuration in which inexpensive nighttime electric power is used to store cold at nighttime to be used as a cold source for dehumidification (dehumidification) operation in daytime. To solve the above-mentioned problem.
【0006】[0006]
【課題を解決するための手段】前記目的を達成するた
め、本発明では、無機質の共晶物体を利用した潜熱蓄冷
材を槽内に装填する潜熱蓄冷システムに着目し、夜間時
においては冷凍機の冷水・冷媒と間接的に熱交換した塩
化リチウム液を、潜熱蓄冷材として蓄冷させると共に、
昼間時には、これを減湿用の吸収剤として使用すること
によって、蓄冷効果による低湿度の空気を得るようにし
たことを特徴とするものである。In order to achieve the above object, the present invention focuses on a latent heat storage system for loading a latent heat storage material using an inorganic eutectic material into a tank. Lithium chloride liquid that has indirectly exchanged heat with the cold water / refrigerant is stored cold as a latent heat storage material,
In the daytime, this is used as a dehumidifying absorbent to obtain low-humidity air due to the cool storage effect.
【0007】具体的には、次の構成を有する。即ちまず
請求項1によれば、吸収剤を処理空気と接触させて当該
処理空気を減湿する方法であって、夜間時において適宜
の冷媒と熱交換して蓄冷させた塩化リチウム液を、昼間
時において処理空気の減湿用の冷却源と吸収剤として使
用することを特徴とする、減湿方法が提供される。この
場合、請求項2に記載したように、前記処理空気を冷却
するための冷凍機の冷媒と夜間時において熱交換して蓄
冷させてもよい。さらに請求項3に記載したように、夜
間時において、安価な深夜電力によりさらに塩化リチウ
ム液に対して再生処理、即ち濃縮処理も施すようにして
もよい。Specifically, it has the following configuration. That is, first, according to claim 1, a method for dehumidifying the treated air by bringing the absorbent into contact with the treated air, wherein the lithium chloride liquid stored in the cold by exchanging heat with an appropriate refrigerant at nighttime is used. A dehumidification method is provided, characterized in that it is sometimes used as a cooling source and absorber for dehumidification of process air. In this case, as described in claim 2, heat may be exchanged with a refrigerant of a refrigerator for cooling the processing air during nighttime to cool the air. Further, as described in claim 3, during the nighttime, the lithium chloride solution may be further subjected to a regenerating process, that is, a concentration process, using inexpensive midnight power.
【0008】そして請求項4によれば、塩化リチウム液
を蓄える貯液槽と、上方に噴霧装置が配された蓄冷材を
収納した蓄冷・減湿槽と、冷凍機の冷媒と蓄冷・減湿槽
内の液体とを熱交換させる熱交換器と、貯液槽内の塩化
リチウム液を当該貯液槽外部で濃縮させる濃縮機とを有
し、前記貯液槽の塩化リチウム液を前記蓄冷・減湿槽内
の噴霧装置に供給自在に構成すると共に、前記蓄冷・減
湿槽内の液体を貯液槽に移送自在に構成し、さらに前記
蓄冷・減湿槽内への処理空気の導入口と、導入した処理
空気を槽外へと排出する排出口とを設け、これら導入口
と排出口は夫々閉塞自在に構成したことを特徴とする、
減湿システムが提供される。According to the present invention, a liquid storage tank for storing a lithium chloride solution, a cool storage / dehumidification tank containing a cool storage material provided with a spraying device above, a refrigerant for a refrigerator and a cool storage / dehumidification. A heat exchanger for exchanging heat with the liquid in the tank; and a concentrator for concentrating the lithium chloride solution in the storage tank outside the storage tank. In addition to being configured to be able to be supplied to the spraying device in the dehumidifying tank, the liquid in the cool storage / humidification tank is configured to be able to be transferred to the liquid storage tank, and an inlet for processing air into the cool storage / humidification tank. And a discharge port for discharging the introduced processing air to the outside of the tank is provided, and the introduction port and the discharge port are each configured to be freely closed,
A dehumidification system is provided.
【0009】また請求項5に記載の減湿システムは、前
記請求項4に記載された減湿システムにおいて、前記冷
凍機の冷媒が、昼間時に前記処理空気、即ち蓄冷・減湿
槽内に導入する処理空気の前処理冷却用冷媒としても使
用自在となるように、冷媒配管されていることを特徴と
するものである。According to a fifth aspect of the present invention, in the dehumidification system according to the fourth aspect, the refrigerant of the refrigerator is introduced into the processing air, that is, the cool storage / humidification tank during daytime. It is characterized by being provided with a refrigerant pipe so that it can be used as a refrigerant for pretreatment cooling of the treated air.
【0010】[0010]
【作用】発明者の知見によれば、減湿用の吸収剤として
用いられる塩化リチウム液は、潜熱蓄冷材としても優れ
ている。従って、請求項1のように、夜間時において適
宜の冷媒と熱交換して蓄冷させた塩化リチウム液を、昼
間時において処理空気の減湿用の吸収剤として使用する
ことにより、処理空気に対して減湿と、冷却とを同時に
実施することができる。また夜間時に適宜の冷媒と熱交
換して蓄冷させるので、夜間における安価な電力を使用
できる。According to the inventor's knowledge, the lithium chloride liquid used as a dehumidifying absorbent is also excellent as a latent heat storage material. Therefore, as described in claim 1, the lithium chloride liquid which has been cooled by heat exchange with an appropriate refrigerant at nighttime is used as an absorbent for dehumidifying the processing air at daytime, whereby the processing air can be reduced. Thus, dehumidification and cooling can be performed simultaneously. In addition, since heat is stored by exchanging heat with an appropriate refrigerant at night, inexpensive electric power at night can be used.
【0011】この場合、請求項2のように、昼間時に前
記処理空気を冷却するための冷凍機の冷媒と熱交換し
て、塩化リチウム液と蓄冷材を蓄冷させるようにすれ
ば、処理空気冷却用の冷凍機を効率よく使用でき、しか
も蓄冷のための冷媒源を他に求める必要はない。従って
システムを構築した場合、これを簡素化できる。In this case, if the lithium chloride liquid and the regenerator material are stored by exchanging heat with the refrigerant of the refrigerator for cooling the process air during the daytime, the process air cooling can be performed. Refrigeration equipment can be used efficiently, and there is no need to find another refrigerant source for cold storage. Therefore, when a system is constructed, this can be simplified.
【0012】そして請求項3のように、夜間時におい
て、塩化リチウム液に対して再生処理を施すようにすれ
ば、夜間時の安価な電力の下でさらに塩化リチウム液を
濃縮しておくことができる。If the lithium chloride solution is subjected to a regeneration treatment at night, the lithium chloride solution can be further concentrated under inexpensive electric power at night. it can.
【0013】請求項4の減湿システムによれば、夜間時
において、導入口と排出口とを閉塞状態にして、貯液槽
の塩化リチウム液を噴霧装置を介して蓄冷・減湿槽に移
送して、熱交換器によってこれを冷却して蓄冷材を蓄冷
させることができる。他方、濃縮機によって、貯液槽内
の塩化リチウム液を濃縮して再生しておくことができ
る。そして昼間時において、蓄冷・減湿槽内の蓄冷され
た塩化リチウム液を貯液槽へと戻し、次いで導入口と排
出口の閉塞状態を解除して処理空気を蓄冷・減湿槽内に
導入しつつ噴霧装置から貯液槽の塩化リチウム液を噴霧
させると、処理空気は蓄冷材を滴下する塩化リチウム液
と接触して減湿、冷却され、排出口から排出される。According to the dehumidifying system of the present invention, at night, the inlet and the outlet are closed, and the lithium chloride solution in the storage tank is transferred to the cool storage / dehumidification tank via the spray device. Then, it can be cooled by the heat exchanger to cool the cold storage material. On the other hand, the lithium chloride solution in the storage tank can be concentrated and regenerated by the concentrator. Then, during the daytime, the cooled lithium chloride liquid in the cool storage / humidification tank is returned to the liquid storage tank, and then the closed state of the inlet and the discharge port is released to introduce the processing air into the cool storage / humidification tank. When the lithium chloride liquid in the liquid storage tank is sprayed from the spraying device, the treated air comes into contact with the lithium chloride liquid into which the regenerator material is dropped, is dehumidified, cooled, and discharged from the discharge port.
【0014】この場合、請求項5のように、冷凍機の冷
媒が、昼間時に処理空気、即ち蓄冷・減湿槽内に導入す
る処理空気の前処理冷却用冷媒としても使用自在となる
ように冷媒配管しておけば、冷凍機を、熱交換器による
夜間時の塩化リチウムの蓄冷用と、昼間時における処理
空気のプレ冷却用とに使用することができる。In this case, the refrigerant of the refrigerator can be used as pretreatment cooling refrigerant for processing air in the daytime, that is, processing air introduced into the cool storage / humidification tank. If a refrigerant pipe is provided, the refrigerator can be used for cold storage of lithium chloride by a heat exchanger at night and for pre-cooling of processing air at daytime.
【0015】[0015]
【実施例】以下、本発明の実施例を図面に基づき説明す
れば、図1は本実施例にかかる減湿システムの系統を示
しており、貯液槽1の中には塩化リチウム液が蓄えられ
ており、その底部に接続された取液管2には、循環ポン
プ3を介して、供給管4と再生用供給管5が接続されて
いる。供給管4は、バルブ6を介して、蓄冷・減湿槽7
内の上部に設けられた噴霧装置8に接続されている。DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 shows a system of a dehumidification system according to the present embodiment. A supply pipe 4 and a regeneration supply pipe 5 are connected to a liquid collection pipe 2 connected to the bottom of the supply pipe 2 via a circulation pump 3. The supply pipe 4 is connected to a cool storage / dehumidification tank 7 via a valve 6.
It is connected to the spraying device 8 provided in the upper part inside.
【0016】一方再生用供給管5は、バルブ9、液ヒー
タ10を介して濃縮機11内上部に設けられた噴霧装置
12に接続されている。この濃縮機11は、再生送風機
13によって取り入れられた外気を空気ヒータ14を介
して濃縮機11内の処理空間に導入する構成を有してお
り、前記噴霧装置12によって噴霧される塩化リチウム
液を、前記空気ヒータ14を通過して加熱された再生空
気によって加熱して、水分を蒸発させ、この塩化リチウ
ム液を濃縮するように構成されている。そして濃縮され
た塩化リチウム液は、戻し管15によって貯液槽1内へ
と戻されるようになっている。On the other hand, the regeneration supply pipe 5 is connected via a valve 9 and a liquid heater 10 to a spraying device 12 provided in the upper part of the concentrator 11. The concentrator 11 has a configuration in which outside air taken in by the regenerative blower 13 is introduced into a processing space in the concentrator 11 through an air heater 14, and the lithium chloride liquid sprayed by the spray device 12 is supplied to the concentrator 11. It is configured to be heated by the regenerated air that has passed through the air heater 14 to evaporate water and concentrate the lithium chloride solution. Then, the concentrated lithium chloride solution is returned to the storage tank 1 by the return pipe 15.
【0017】前記蓄冷・減湿槽7内における噴霧装置8
の下方には、蓄冷材16が設置されている。この蓄冷材
16は、その表面に例えばフィンを多数有した外形を持
った容器を有し、その内部には、潜熱蓄熱材が充填され
ている。そして噴霧装置8から噴霧された塩化リチウム
液は、この蓄冷材16の表面を滴下して蓄冷・減湿槽7
の底部へと下降するようになっている。そして蓄冷・減
湿槽7の当該底部には、バルブ17を介して戻し管18
が接続されており、蓄冷・減湿槽7内に溜まった塩化リ
チウム液は、この戻し管18を通じて貯液槽1へ戻され
るように構成されている。A spray device 8 in the cool storage / humidification tank 7
A cold storage material 16 is provided below the space. The cold storage material 16 has a container having an outer shape having a large number of fins on its surface, for example, and the inside thereof is filled with a latent heat storage material. Then, the lithium chloride liquid sprayed from the spray device 8 is dropped on the surface of the cold storage material 16 to cool and cool the dehumidification tank 7.
It descends to the bottom. A return pipe 18 is provided at the bottom of the cool storage / humidification tank 7 through a valve 17.
Is connected, so that the lithium chloride liquid accumulated in the cool storage / dehumidification tank 7 is returned to the liquid storage tank 1 through the return pipe 18.
【0018】前記蓄冷・減湿槽7内には、さらに前出蓄
冷材16を挟んで対向している冷媒ヘッダ21、22が
設置されており、これら冷媒ヘッダ21、22は、蓄冷
・減湿槽7の外部にて、循環管路23によって結ばれて
いる。そしてこの循環管路23には、熱交換器24、循
環ポンプ25が介装されている。前記熱交換器24は、
冷凍機26の冷媒と熱交換するように構成されており、
バルブ27を開放して冷凍機26の冷媒が、冷媒管路2
8を介して熱交換器24に供給されることによって、循
環管路23を流れる塩化リチウム液は、熱交換器24に
よって冷却されるようになっている。In the cool storage / humidification tank 7, refrigerant headers 21 and 22 facing each other with the above-mentioned cold storage material 16 interposed therebetween are installed. Outside the tank 7, they are connected by a circulation line 23. A heat exchanger 24 and a circulation pump 25 are provided in the circulation line 23. The heat exchanger 24 includes:
It is configured to exchange heat with the refrigerant of the refrigerator 26,
When the valve 27 is opened, the refrigerant of the refrigerator 26 is
The lithium chloride liquid flowing through the circulation line 23 is supplied to the heat exchanger 24 via the cooling device 8, and is cooled by the heat exchanger 24.
【0019】また前記蓄冷・減湿槽7の天板には、処理
空気の導入口31と排出口32が設けられており、これ
ら導入口31と排出口32とは、前出蓄冷材16を挟ん
で離隔している位置関係にある。またこれら導入口31
と排出口32には、それぞれ導入ダクト33と排出ダク
ト34とが接続されており、さらにこれら導入ダクト3
3と排出ダクト34には、各々モータダンパ35、36
が介装されている。従って、これら各モータダンパ3
5、36を閉止すれば、蓄冷・減湿槽7は外部雰囲気か
らは気密に遮断される。The top plate of the cool storage / dehumidification tank 7 is provided with an inlet 31 and an outlet 32 for the processing air. They are in a positional relationship of being sandwiched and separated. In addition, these inlets 31
The outlet duct 32 is connected to an inlet duct 33 and an outlet duct 34, respectively.
3 and the discharge duct 34 have motor dampers 35 and 36, respectively.
Is interposed. Therefore, each of these motor dampers 3
By closing 5, 36, the cool storage / humidification tank 7 is airtightly shut off from the external atmosphere.
【0020】前記導入ダクト33は、外気導入路37と
接続されており、フィルタ38、空調機39を介して導
入された空気は、この導入ダクト33を通じて蓄冷・減
湿槽7内に導入されるようになっている。また他方排出
ダクト34には、送風機40が介装されている。従っ
て、送風機40を作動させると、空調機39を通過して
例えばプレ冷却された処理空気は、導入ダクト33、導
入口31を通じて蓄冷・減湿槽7内に導入され、蓄冷材
16を通過して排出口32、排出ダクト34を通じて送
風機40により所定の室へと送風されるようになってい
る。The introduction duct 33 is connected to an outside air introduction passage 37, and air introduced through a filter 38 and an air conditioner 39 is introduced into the cool storage / humidification tank 7 through the introduction duct 33. It has become. On the other hand, a blower 40 is interposed in the discharge duct 34. Therefore, when the blower 40 is operated, the processing air pre-cooled through the air conditioner 39, for example, is introduced into the cool storage / humidification tank 7 through the introduction duct 33 and the introduction port 31, and passes through the cool storage material 16. The air is blown into a predetermined chamber by a blower 40 through a discharge port 32 and a discharge duct 34.
【0021】そして前記空調機39の冷媒は、バルブ4
1を有しかつ前出冷媒管路28と分岐した冷媒管路42
によって、前出冷凍機26から供給されるように構成さ
れている。The refrigerant of the air conditioner 39 is supplied to the valve 4
1 and branched from the preceding refrigerant line 28
Thus, it is configured to be supplied from the refrigerator 26 described above.
【0022】本実施例にかかる減湿システムは以上のよ
うに構成されており、次にこの減湿システムを用いた運
転例について説明すると、まず夜間時においては、蓄冷
及び塩化リチウム液の濃縮運転がなされる。The dehumidification system according to the present embodiment is configured as described above. Next, an operation example using this dehumidification system will be described. Is made.
【0023】即ち、まずバルブ17を閉鎖した状態で、
バルブ6を開放して循環ポンプ3を作動させ、貯液槽1
にある塩化リチウム液の一部を、供給管4、噴霧装置8
を介して、蓄冷・減湿槽7内に移送して、充満させる。
そして移送完了後バルブ6を閉鎖する一方、冷媒管路4
2のバルブ41を閉鎖、冷媒管路28のバルブ27を開
放して循環ポンプ25を作動させ、同時に冷凍機26を
作動させる。そうすると、蓄冷・減湿槽7の塩化リチウ
ム液は、循環管路23を通じて冷媒ヘッダ22→熱交換
器24→冷媒ヘッダ21→蓄冷・減湿槽7、というよう
に循環し、一方冷凍機26の冷媒は、冷媒管路28を通
じて熱交換器24との間で循環し、貯液槽1の塩化リチ
ウム液は、この熱交換によって冷却、蓄冷される。That is, first, with the valve 17 closed,
The circulation pump 3 is operated by opening the valve 6, and the liquid storage tank 1 is opened.
A part of the lithium chloride solution in the supply pipe 4 and the spraying device 8
And transferred into the cool storage / humidification tank 7 to be filled.
After the transfer is completed, the valve 6 is closed while the refrigerant line 4 is closed.
The second valve 41 is closed, the valve 27 of the refrigerant line 28 is opened, and the circulation pump 25 is operated, and at the same time, the refrigerator 26 is operated. Then, the lithium chloride liquid in the cool storage / humidification tank 7 circulates through the circulation pipe 23 in the order of the refrigerant header 22 → the heat exchanger 24 → the refrigerant header 21 → the cool storage / humidification tank 7, while the refrigerator 26 The refrigerant circulates through the refrigerant line 28 with the heat exchanger 24, and the lithium chloride liquid in the liquid storage tank 1 is cooled and stored by this heat exchange.
【0024】またそれとは別にバルブ9を開放させた状
態では、貯液槽1の塩化リチウム液は、再生用供給管5
を経て、液ヒータ10によって加熱されつつ濃縮機11
の噴霧装置12によって濃縮機11内に噴霧される。こ
のとき再生送風機13を作動させて外気を空気ヒータ1
4によって加熱しながら濃縮機11内に導入すると、前
記噴霧された塩化リチウム液中の水分は、大気中に排気
されて濃縮される。そして濃縮された塩化リチウム液
は、戻し管15を介して貯液槽1内に戻され、かかる循
環濃縮経路によって貯液槽1の塩化リチウム液は、極め
て濃縮された状態で貯液槽1内に蓄えられて、昼間時の
減湿運転に備えられる。In a state where the valve 9 is opened separately, the lithium chloride solution in the storage tank 1 is supplied to the supply pipe 5 for regeneration.
Through the concentrator 11 while being heated by the liquid heater 10.
Is sprayed into the concentrator 11 by the spraying device 12. At this time, the regenerative blower 13 is operated to supply outside air to the air heater 1.
When introduced into the concentrator 11 while heating by 4, the water in the sprayed lithium chloride solution is exhausted to the atmosphere and concentrated. Then, the concentrated lithium chloride solution is returned into the storage tank 1 through the return pipe 15, and the lithium chloride solution in the storage tank 1 is extremely concentrated in the storage tank 1 by such a circulating concentration path. And be prepared for dehumidifying operation in the daytime.
【0025】このような夜間運転が終了して、塩化リチ
ウム液の蓄冷・濃縮、及び蓄冷材16の蓄冷が完了する
と、昼間時の減湿運転がなされる。即ち、まず蓄冷・減
湿槽7と貯液槽1とを結んでいる戻し管18のバルブ1
7を開放し、蓄冷された蓄冷・減湿槽7内の塩化リチウ
ム液を貯液槽1に移送する。また冷媒管路28のバルブ
27を閉鎖し、循環ポンプ25を停止させる。When the nighttime operation is completed and the cold storage / concentration of the lithium chloride solution and the cold storage material 16 are completed, the daytime dehumidification operation is performed. That is, first, the valve 1 of the return pipe 18 connecting the cold storage / dehumidification tank 7 and the liquid storage tank 1.
7 is opened, and the stored lithium chloride solution in the cold storage / humidification tank 7 is transferred to the liquid storage tank 1. Further, the valve 27 of the refrigerant pipe 28 is closed, and the circulation pump 25 is stopped.
【0026】そして冷媒管路42のバルブ41を開放し
て空調機39を作動させると共に、送風機40を作動さ
せ、同時に再生用供給管路5のバルブ9を閉鎖して、貯
液槽1の塩化リチウム液を供給管4、噴霧装置8を通じ
て蓄冷・減湿槽7内の蓄冷材16に向けて噴霧させる。The air conditioner 39 is operated by opening the valve 41 of the refrigerant pipe 42 and the blower 40 is operated. At the same time, the valve 9 of the regeneration supply pipe 5 is closed, and The lithium liquid is sprayed toward the cold storage material 16 in the cold storage / humidification tank 7 through the supply pipe 4 and the spray device 8.
【0027】そうすると、まず導入外気は、前記空調機
39によってプレ冷却並びに減湿され、ダクト33、導
入口31を経て、蓄冷材16によって半ば仕切られた蓄
冷・減湿槽7内の一方の空間内に導入される。このとき
蓄冷材16表面には、噴霧装置8によって塩化リチウム
液が滴下しているので、導入された空気は蓄冷・減湿槽
7内の他方の空間へと移動するときにこの滴下する塩化
リチウム液と接触して減湿される。またこの塩化リチウ
ム液自体は、既述の如く夜間時において蓄冷されたもの
であり、また蓄冷材16も、夜間時の蓄冷によって極め
て大きな冷熱を蓄えているので、減湿の際に発生する熱
は吸収されるだけでなく、空気自体も冷却される。従っ
て、導入された空気は、減湿と同時に冷却がなされるの
である。そしてそのようにして減湿・冷却された空気
は、送風機40によって排出口32、ダクト34を通じ
て所定の室へと送風される。Then, the introduced outside air is pre-cooled and dehumidified by the air conditioner 39, passes through the duct 33 and the inlet 31, and is partially partitioned by the regenerator 16 in the cold storage / dehumidification tank 7. Introduced within. At this time, since the lithium chloride solution is dripped on the surface of the cold storage material 16 by the spraying device 8, the introduced air transfers the lithium chloride solution to the other space in the cool storage / humidification tank 7. Dehumidified by contact with liquid. As described above, the lithium chloride solution itself is cold-stored at nighttime, and the cold storage material 16 also stores extremely large cold heat due to cold storage at nighttime. Not only is absorbed, but also the air itself is cooled. Therefore, the introduced air is cooled at the same time as dehumidification. The air thus dehumidified and cooled is blown by a blower 40 to a predetermined room through a discharge port 32 and a duct 34.
【0028】なお昼間時に前記減湿運転によって希釈さ
れた塩化リチウム液は、戻し管18を通じて貯液槽1へ
と戻され、次の夜間時の濃縮に備えられる。In the daytime, the lithium chloride solution diluted by the dehumidifying operation is returned to the storage tank 1 through the return pipe 18, and is prepared for the next nighttime concentration.
【0029】以上のように本実施例によれば、まず夜間
の安価な電力を使用して塩化リチウム液の蓄冷、濃縮、
及び蓄冷材の蓄冷が図れる。そして昼間時の減湿運転の
際には、処理空気に対して減湿と同時に冷却を実施する
ことが可能である。しかも蓄冷に使用した冷媒は、昼間
時の処理空気に対してプレ冷却するために用いる空調機
39に使用する冷凍機26の冷媒であるから、装置自体
の稼働効率も良好であり、極めて効率のよいシステムと
なっている。As described above, according to this embodiment, cold storage and concentration of the lithium chloride solution are performed using inexpensive power at night.
And cold storage of the cold storage material can be achieved. In the dehumidification operation in the daytime, it is possible to cool the treated air simultaneously with the dehumidification. Moreover, since the refrigerant used for the cold storage is the refrigerant of the refrigerator 26 used for the air conditioner 39 used for pre-cooling the processing air in the daytime, the operation efficiency of the device itself is also good, and the efficiency is extremely high. It is a good system.
【0030】発明者の試算によると、前出本実施例にか
かる減湿システムを使用すれば、同一湿分を得るにあた
り、夜間電力が使用できない乾式減湿機と比べて、約1
/5の運転費で済むことがわかった。According to the inventor's calculation, the use of the dehumidification system according to the present embodiment provides about one unit in obtaining the same moisture as compared with a dry dehumidifier which cannot use electric power at night.
It turned out that the operation cost was / 5.
【0031】なお前出実施例において、送風機40の出
口に加湿器を設置することにより、低温度空気を得るこ
とが可能である。In the embodiment described above, it is possible to obtain low-temperature air by installing a humidifier at the outlet of the blower 40.
【0032】[0032]
【発明の効果】請求項1の減湿方法によれば、処理空気
に対して、減湿と冷却とを同時に実施することができ、
しかも夜間時に適宜の冷媒と熱交換して蓄冷させるの
で、夜間における安価な電力を使用して蓄冷させること
ができる。請求項2の減湿方法によれば、さらに処理空
気を冷却するための冷凍機の冷媒と熱交換しているの
で、蓄冷のための冷媒源を他に求める必要はなく、冷凍
機を有効に利用してシステムを簡素化できる。According to the first aspect of the present invention, the dehumidification and the cooling can be simultaneously performed on the processing air.
In addition, since cold is stored by exchanging heat with an appropriate refrigerant at night, cold can be stored using inexpensive electric power at night. According to the dehumidification method of claim 2, since the heat exchange is performed with the refrigerant of the refrigerator for further cooling the processing air, there is no need to obtain another refrigerant source for cool storage, and the refrigerator can be effectively used. It can be used to simplify the system.
【0033】請求項3の減湿方法によれば、昼間時の減
湿に備えて、夜間時の安価な電力の下でさらに塩化リチ
ウム液を濃縮しておくことができ、省エネによる減湿、
冷却が可能である。According to the dehumidifying method of the third aspect, the lithium chloride solution can be further concentrated under inexpensive electric power at night in preparation for dehumidifying during the daytime.
Cooling is possible.
【0034】請求項4の減湿システムによれば、請求項
1、3の方法を実施でき、さらに蓄冷と、減湿処理とを
1つの蓄冷・減湿槽において実施することができる。ま
た請求項5の減湿システムによれば、さらに昼間時にお
ける処理空気のプレ冷却用の冷凍機を有効利用でき、シ
ステム自体が簡素化されている。According to the dehumidification system of the fourth aspect, the methods of the first and third aspects can be carried out, and further, the cold storage and the dehumidification processing can be carried out in one cold storage / dehumidification tank. According to the dehumidification system of the fifth aspect, a refrigerator for pre-cooling the processing air during the daytime can be further effectively used, and the system itself is simplified.
【図1】本発明の実施例にかかる減湿システムの系統を
示す図であって、夜間時の運転状況を示す説明図であ
る。FIG. 1 is a diagram illustrating a system of a dehumidification system according to an embodiment of the present invention, and is an explanatory diagram illustrating an operation state at night.
【図2】本発明の実施例にかかる減湿システムの系統を
示す図であって、昼間時の運転状況を示す説明図であ
る。FIG. 2 is a diagram illustrating a system of a dehumidification system according to an embodiment of the present invention, and is an explanatory diagram illustrating an operation state during daytime.
1 貯液槽 3、25 循環ポンプ 7 蓄冷・減湿槽 8 噴霧装置 11 濃縮機 16 蓄冷材 21、22 冷媒ヘッダ 24 熱交換器 26 冷凍機 31 導入口 32 排出口 39 空調機 40 送風機 DESCRIPTION OF SYMBOLS 1 Storage tank 3, 25 Circulation pump 7 Cold storage / humidification tank 8 Sprayer 11 Concentrator 16 Cold storage material 21, 22 Refrigerant header 24 Heat exchanger 26 Refrigerator 31 Inlet 32 Outlet 39 Air conditioner 40 Blower
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) B01D 53/26 - 53/28 F24F 1/00 F24F 5/00 F28C 1/00 C09K 5/00 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) B01D 53/26-53/28 F24F 1/00 F24F 5/00 F28C 1/00 C09K 5/00
Claims (5)
空気を減湿する方法であって、夜間時において適宜の冷
媒と熱交換して蓄冷させた蓄冷材と塩化リチウム液を、
昼間時において処理空気の減湿用冷却源の吸収剤として
使用することを特徴とする、減湿方法。1. A method for bringing a absorbent into contact with treated air to dehumidify the treated air, wherein a cold storage material and a lithium chloride liquid which have been stored by exchanging heat with an appropriate refrigerant at nighttime are:
A dehumidification method characterized in that it is used as an absorbent for a dehumidification cooling source of treated air in the daytime.
空気を減湿する方法であって、前記処理空気を冷却する
ための冷凍機の冷媒と夜間時において熱交換して蓄冷さ
せた蓄冷材と塩化リチウム液を、昼間時において処理空
気の減湿用冷却源の吸収剤として使用することを特徴と
する、減湿方法。2. A method for dehumidifying processing air by bringing an absorbent into contact with processing air, the method comprising storing heat at night to exchange heat with a refrigerant of a refrigerator for cooling the processing air. A dehumidifying method, comprising using a material and a lithium chloride liquid as absorbents of a cooling source for dehumidifying treated air during daytime.
て再生濃縮処理を施すことを特徴とする、請求項1又は
2に記載の減湿方法。3. The dehumidification method according to claim 1, wherein a regeneration and concentration treatment is performed on the lithium chloride solution at night.
に噴霧装置が配された蓄冷材を収納した蓄冷・減湿槽
と、冷凍機の冷媒と蓄冷・減湿槽内の液体とを熱交換さ
せる熱交換器と、貯液槽内の塩化リチウム液を当該貯液
槽外部で濃縮させる濃縮機とを有し、前記貯液槽の塩化
リチウム液を前記蓄冷・減湿槽内の噴霧装置に供給自在
に構成すると共に、前記蓄冷・減湿槽内の液体を貯液槽
に移送自在に構成し、さらに前記蓄冷・減湿槽内への処
理空気の導入口と、導入した処理空気を槽外へと排出す
る排出口とを設け、これら導入口と排出口は夫々閉塞自
在に構成したことを特徴とする、減湿システム。4. A storage tank for storing a lithium chloride liquid, a cool storage / humidification tank containing a cool storage material provided with a spraying device above, a refrigerant of a refrigerator and a liquid in the cool storage / humidification tank. A heat exchanger for heat exchange, and a concentrator for concentrating the lithium chloride solution in the storage tank outside the storage tank, and spraying the lithium chloride solution in the storage tank in the cool storage / humidification tank. The apparatus is configured to be capable of being supplied to the apparatus, and configured to be able to transfer the liquid in the cool storage / humidification tank to the liquid storage tank. Further, an inlet for processing air into the cool storage / humidification tank, and the introduced processing air. A discharge port for discharging the water to the outside of the tank, and the introduction port and the discharge port are each configured to be freely closed.
に噴霧装置が配された蓄冷材を収納した蓄冷・減湿槽
と、冷凍機の冷媒と蓄冷・減湿槽内の液体とを熱交換さ
せる熱交換器と、貯液槽内の塩化リチウム液を当該貯液
槽外部で濃縮させる濃縮機とを有し、前記貯液槽の塩化
リチウム液を前記蓄冷・減湿槽内の噴霧装置に供給自在
に構成すると共に、前記蓄冷・減湿槽内の液体を貯液槽
に移送自在に構成し、さらに前記蓄冷・減湿槽内への処
理空気の導入口と、導入した処理空気を槽外へと排出す
る排出口とを設け、これら導入口と排出口は夫々閉塞自
在に構成し、さらにまた前記冷凍機の冷媒が、昼間時に
前記処理空気の前処理冷却用冷媒としても使用自在とな
るように、冷媒配管されていることを特徴とする、減湿
システム。5. A storage tank for storing a lithium chloride liquid, a cool storage / dehumidification tank containing a cool storage material provided with a spraying device above, a refrigerant of a refrigerator and a liquid in the cool storage / dehumidification tank. A heat exchanger for heat exchange, and a concentrator for concentrating the lithium chloride solution in the storage tank outside the storage tank, and spraying the lithium chloride solution in the storage tank in the cool storage / humidification tank. The apparatus is configured to be capable of being supplied to the apparatus, and configured to be able to transfer the liquid in the cool storage / humidification tank to the liquid storage tank. Further, an inlet for processing air into the cool storage / humidification tank, and the introduced processing air. And a discharge port for discharging the gas to the outside of the tank.The inlet and the discharge port are each configured to be able to be closed.Furthermore, the refrigerant of the refrigerator is also used as a refrigerant for pre-processing and cooling the processing air in the daytime. A dehumidification system characterized by being provided with a refrigerant pipe so as to be free.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14847294A JP3302833B2 (en) | 1994-06-07 | 1994-06-07 | Dehumidification method and dehumidification system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14847294A JP3302833B2 (en) | 1994-06-07 | 1994-06-07 | Dehumidification method and dehumidification system |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH07328376A JPH07328376A (en) | 1995-12-19 |
JP3302833B2 true JP3302833B2 (en) | 2002-07-15 |
Family
ID=15453518
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14847294A Expired - Fee Related JP3302833B2 (en) | 1994-06-07 | 1994-06-07 | Dehumidification method and dehumidification system |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3302833B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000274735A (en) * | 1999-03-19 | 2000-10-06 | Ngk Insulators Ltd | Drying device, cooling and/or heating device incorporating it |
ES2746254T3 (en) * | 2011-09-16 | 2020-03-05 | Daikin Ind Ltd | Humidity control device |
EP2631549B1 (en) * | 2012-02-21 | 2016-04-13 | Watergy GmbH | System for regulating the temperature in an enclosure |
-
1994
- 1994-06-07 JP JP14847294A patent/JP3302833B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH07328376A (en) | 1995-12-19 |
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