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JPS6317487B2 - - Google Patents
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JPS6317487B2 - - Google Patents

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Publication number
JPS6317487B2
JPS6317487B2 JP54085671A JP8567179A JPS6317487B2 JP S6317487 B2 JPS6317487 B2 JP S6317487B2 JP 54085671 A JP54085671 A JP 54085671A JP 8567179 A JP8567179 A JP 8567179A JP S6317487 B2 JPS6317487 B2 JP S6317487B2
Authority
JP
Japan
Prior art keywords
gas
water
adsorption
condenser
moisture
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
Application number
JP54085671A
Other languages
Japanese (ja)
Other versions
JPS567628A (en
Inventor
Satoru Takeyama
Takekuni Azuma
Akira Ikeda
Toshishige Yamamoto
Shigeo Katsurada
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.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP8567179A priority Critical patent/JPS567628A/en
Priority to DE8080102317T priority patent/DE3064739D1/en
Priority to EP80102317A priority patent/EP0019143B1/en
Priority to US06/147,115 priority patent/US4299599A/en
Publication of JPS567628A publication Critical patent/JPS567628A/en
Publication of JPS6317487B2 publication Critical patent/JPS6317487B2/ja
Granted legal-status Critical Current

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  • Separation Of Gases By Adsorption (AREA)
  • Drying Of Gases (AREA)

Description

【発明の詳細な説明】 この発明は、気体中の水分から水を得る造水装
置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a water generation device that obtains water from moisture in gas.

従来、造水装置としては海水を原料とし、淡水
を作る装置は海水淡水化装置としてよく知られて
いる。また下水などの汚水を高度に処理して、再
利用可能な清澄度の高い水を得る水の再利用処理
装置があるが、これも海水淡水化装置と同じ範疇
の造水装置とみることができる。すなわちこれら
はいづれも水を得るにあたり液体の水を主成分と
する溶液を原料としている。このためにこれらの
造水装置は原料として液体状の水を使用する以
上、当然ながら砂漠のように全く液体状の水が得
られないところでは造水できない。
BACKGROUND ART Conventionally, a device for producing fresh water using seawater as a raw material is well known as a seawater desalination device. There is also a water reuse treatment device that processes wastewater such as sewage to a high degree to produce highly clear water that can be reused, but this can also be considered a water production device in the same category as a seawater desalination device. can. That is, in all of these methods, a solution containing liquid water as a main component is used as a raw material to obtain water. For this reason, since these water generation devices use liquid water as a raw material, they cannot naturally generate water in places such as deserts where liquid water cannot be obtained at all.

そこで砂漠のように液体状の水が得られない地
域でも容易に水を得ることのできる造水装置が要
望されており、このような新規な造水装置が開発
されつつある。
Therefore, there is a need for a water generation device that can easily obtain water even in areas such as deserts where liquid water cannot be obtained, and such new water generation devices are being developed.

すなわち、この新規な造水装置は大気中に存在
する水分から水を得る装置であり、大気が存在す
るかぎり、どこででも造水することができる新規
な造水装置である。勿論、大気中に全く水分がな
ければ造水は不可能であるが、気候に関する統計
データおよび発明者らの調査結果では、アラビア
半島中央部の巨大な砂漠の大気であつても空気1
m3中に3〜4gの水分は存在し、造水は可能であ
る。したがつて、不毛の地に水を得て、人間活動
が可能となり、また、この水を潅水として利用す
ることによつて植物栽培も可能となる。すなわ
ち、この造水装置は人間の生活圏拡大に寄与する
もので、その意義はきわめて大きい。
In other words, this new water generation device is a device that obtains water from moisture present in the atmosphere, and is a new water generation device that can generate water anywhere as long as the atmosphere exists. Of course, it is impossible to create water if there is no moisture in the atmosphere, but statistical data on climate and the results of the inventors' research show that even in the atmosphere of the huge desert in the central Arabian Peninsula, the air
There are 3 to 4 g of water in m 3 and water production is possible. Therefore, human activities can be carried out by obtaining water in barren land, and by using this water as irrigation, it is also possible to cultivate plants. In other words, this water production device contributes to expanding the living area of humans, and its significance is extremely large.

この造水装置の基本原理は、第1の過程として
大気中の水分を吸着剤に吸着させ、ついで第2の
過程としてこの水分を吸着した吸着剤を加熱する
ことによつて吸着されていた水分を水蒸気として
脱着させ、これを凝縮器に導き水にするものであ
る。このとき同時に吸着剤は水を失つて、再び吸
着能力を回復するので、吸着剤は大気中の水分の
吸着にくりかえし使用される。このようにして、
継続的に大気中から液相の水を得ることができ
る。
The basic principle of this water generation device is that the first step is to adsorb moisture in the atmosphere onto an adsorbent, and the second step is to heat the adsorbent that has adsorbed this moisture to remove the adsorbed moisture. is desorbed as water vapor, which is then led to a condenser and converted into water. At this time, the adsorbent simultaneously loses water and regains its adsorption capacity, so that the adsorbent is repeatedly used to adsorb moisture from the atmosphere. In this way,
Liquid phase water can be obtained continuously from the atmosphere.

第1図は以上の基本原理にもとづく造水装置の
配管を簡略化した先行技術による構成の一例を模
式的に示す平面図、第2図は第1図の―線で
の断面図、第3図は第2図の―線での断面図
である。
Fig. 1 is a plan view schematically showing an example of a configuration according to the prior art that simplifies the piping of a fresh water generator based on the above basic principle, Fig. 2 is a cross-sectional view taken along the - line in Fig. 1, and Fig. 3 The figure is a sectional view taken along the line -- in FIG.

図において、1Aおよび1Bはそれぞれ断面形
状が四角形である管状体からなり吸着剤充填層1
aおよび吸着剤充填層1bを収容する第1および
第2の収容部、2aは第1の収容部1Aの両開口
端縁部の上部側板にそれぞれ吸着剤充填層1aを
はさんで設けられた気体の流通口、2bは第2の
収容部1Bの両開口端縁部の上部側板にそれぞれ
吸着剤充填層1bをはさんで設けられた気体の流
通口、3aは第1の収容部1Aの上部側板上に設
けられ流通口2aを通つて導入される気体が加熱
される加熱室、3bは第2の収容部1Bの上部側
板上に設けられ流通口2bを通つて導入される気
体が加熱される加熱室、4aおよび4bはそれぞ
れ加熱室3aおよび加熱室3b内の気体を加熱す
る加熱器、5は第1の収容部1Aの空気の排出側
の開口部と第2の収容部1Bの空気の排出側の開
口部とに連通するように共通に設けられた空気の
通気室、6は通気室5の上部に開けられた空気の
排気口の近傍に設置され第1の収容部1Aまたは
第2の収容部1B内を通して吸着剤充填層1aま
たは吸着剤充填層1bに水分を吸着させる空気を
吸込んで排出する吸込み形の吸着用ブロワであ
る。7は通気室5内に設けられ吸着用ブロワ6に
よつて排出される空気で冷却されるように構成さ
れた凝縮器、8aは吸着用ブロワ6によつて第1
の収容部1A内に空気が吸込まれる吸込み口側の
左右側板の開口端部にそれぞれ取り付けられこの
吸込み口を両開き戸のように開閉する吸込み口側
扉、9aは吸着用ブロワ6によつて第1の収容部
1A内の空気が排出される排出口の左右側板の開
口端部にそれぞれ取り付けられこの排出口を両開
き戸のように開閉する排出口側扉、8bおよび9
bはそれぞれ第1の収容部1Aの吸込み口側扉8
aおよび排出口側扉9aと同様の第2の収容部1
Bの吸込み口側扉および排出口側扉である。10
aは流通口2aに近接して設けられ吸込み口側扉
8aおよび排出口側扉9aを閉じるとによつて流
通口2aを通して第1の収容部1Aと加熱室3a
とで形成される循環路に加熱室3aにおいて加熱
された空気を循環させて吸着剤充填層1aを昇温
させてこの吸着剤充填層1aに吸着された水分を
脱着させる循環用ブロワ、10bは、循環用ブロ
ワ10aと様に、流通口2bに近接して設けられ
吸込み口側扉8bおよび排出口側扉9bを閉じる
ことによつて流通口2bを通して第2の収容部1
Bと加熱室3bとで形成される循環路に加熱室3
bにおいて加熱された空気を循環させて吸着剤充
填層1bを昇温させてこの吸着剤充填層1bに吸
着された水分を脱着させる循環用ブロワである。
11aおよび11bはそれぞれ一端が第1の収容
部1Aと加熱室3aとで形成された循環路および
第2の収容部1Bと加熱室3bとで形成された循
環路に連通するように接続された気体の流路、1
2は流路11aの他端と凝縮器7との接続、およ
び流路11bの他端と凝縮器7との接続を相互に
切換えることができる切換えバルブである。一点
鎖線で機能のみを示す13は凝縮器7で得られた
水を貯わえる大気開放形の受水槽、一点鎖線で示
す14は造水された水である。
In the figure, 1A and 1B are tubular bodies each having a square cross-sectional shape, and the adsorbent packed layer 1
The first and second accommodating portions 2a, which accommodate the adsorbent packed layer 1b and the adsorbent packed layer 1a, are provided on the upper side plates of both opening edges of the first accommodating portion 1A, respectively, with the adsorbent packed layer 1a sandwiched therebetween. Gas communication ports 2b are provided in the upper side plates of both opening edges of the second storage section 1B with the adsorbent packed layer 1b in between, and 3a is a gas communication port of the first storage section 1A. A heating chamber 3b is provided on the upper side plate of the second housing section 1B and heats the gas introduced through the communication port 2a, and a heating chamber 3b is provided on the upper side plate of the second storage section 1B and heats the gas introduced through the communication port 2b. 4a and 4b are heaters that heat the gas in the heating chamber 3a and heating chamber 3b, respectively; 5 is an opening on the air discharge side of the first housing section 1A and an opening on the air discharge side of the second housing section 1B; An air ventilation chamber 6 provided in common so as to communicate with the opening on the air discharge side is installed near the air exhaust port opened in the upper part of the ventilation chamber 5, and is installed in the vicinity of the air exhaust port opened in the upper part of the ventilation chamber 5, and is connected to the first storage section 1A or This is a suction type adsorption blower that sucks and discharges air that causes moisture to be adsorbed to the adsorbent packed bed 1a or the adsorbent packed bed 1b through the second storage part 1B. 7 is a condenser provided in the ventilation chamber 5 and configured to be cooled by air discharged by the adsorption blower 6;
A suction port side door 9a is attached to the opening end of the left and right side plates on the suction port side through which air is sucked into the housing portion 1A, and opens and closes the suction port like a double door. Exhaust side doors 8b and 9 are attached to the opening ends of the left and right side plates of the exhaust outlet through which the air in the first storage section 1A is discharged, and open and close the outlet like a double door.
b is the suction port side door 8 of the first storage section 1A, respectively.
a and a second storage section 1 similar to the discharge port side door 9a.
These are the suction port side door and the discharge port side door of B. 10
A is provided close to the flow port 2a, and when the suction port side door 8a and the discharge port side door 9a are closed, the first housing portion 1A and the heating chamber 3a are connected through the flow port 2a.
A circulation blower 10b circulates the air heated in the heating chamber 3a through the circulation path formed by the heating chamber 3a to raise the temperature of the adsorbent packed bed 1a and desorb the moisture adsorbed on the adsorbent packed bed 1a. , like the circulation blower 10a, by closing the suction port side door 8b and the discharge port side door 9b, which are provided close to the circulation port 2b, the second housing part 1 is passed through the circulation port 2b.
The heating chamber 3 is in the circulation path formed by the heating chamber 3b and the heating chamber 3b.
This is a circulation blower that circulates the heated air in b to raise the temperature of the adsorbent packed bed 1b and desorbs the moisture adsorbed on the adsorbent packed bed 1b.
11a and 11b were connected at one end to communicate with a circulation path formed by the first storage section 1A and the heating chamber 3a and a circulation path formed by the second storage section 1B and the heating chamber 3b. Gas flow path, 1
Reference numeral 2 denotes a switching valve that can mutually switch the connection between the other end of the flow path 11a and the condenser 7 and the connection between the other end of the flow path 11b and the condenser 7. Reference numeral 13, whose function is indicated by a dashed line, is an air-open water tank for storing water obtained in the condenser 7, and reference numeral 14, which is indicated by a dashed line, is produced water.

次に、動作について説明する。 Next, the operation will be explained.

この先行技術による造水装置では、収容部を2
基設けているので、一方の収容部が吸着過程(第
1の過程)を行つているときに、他方の収容部で
脱着過程(第2の過程)を行い、これらの過程が
終了した後に、これらの過程を交互に切りかえ
て、繰り返すことによつて造水を連続的に行うこ
とができる。以下の説明では、第1の収容部1A
が吸着過程にあり、第2の収容部1Bが脱着過程
にあるものとして述べる。
In this prior art freshwater generating device, there are two storage parts.
Since the base is provided, when one storage part is performing the adsorption process (first process), the other storage part is performing the desorption process (second process), and after these processes are completed, By alternating and repeating these processes, water generation can be performed continuously. In the following description, the first accommodating section 1A
The following description will be made assuming that the second housing section 1B is in the adsorption process and the second storage part 1B is in the desorption process.

第1の収容部1Aにおける吸着過程において
は、まず、第1の収容部1Aの吸込み口側扉8a
および排出口側扉9aを開き、第2の収容部1B
の吸込み口側扉8bおよび排出口側扉9bを閉じ
るとともに、切換えバルブ12を流路11bと凝
縮器7とが接続するように切換える。次に、吸着
用ブロワ6を作動させて、吸着用空気を第1の収
容部1Aの吸込口から内部に吸込み、これに収容
された吸着剤充填層1aと接触させて吸着過程が
行われる。このとき、吸着剤充填層1aに水分が
吸着されて乾燥した空気は通気室5内を通つて外
部へ排出される。一方、第1の収容部1Aが吸着
過程にあるとき、第2の収容部1Bにおける脱着
過程が行われることが望ましい。この第2の収容
部1Bの脱着過程においては、第2の収容部1B
の吸込み口側扉8bおよび排出口側扉9bを閉じ
た状態で、循環用ブロワ10bを作動させて、加
熱室3b内の空気を、加熱室4bで加熱しなが
ら、流通口2bを通して第2の収容部1Bと加熱
室3bとで形成された循環路を循環させる。そう
して、加熱室3b内で加熱された空気によつて、
第2の収容部1B内の吸着剤充填層1bを加熱
し、この吸着剤充填層1bに予め吸着されていた
水分を水蒸気にして脱着させようとするものであ
る。このように、吸着剤充填層1bから水蒸気が
脱着されると、脱着による水蒸気の発生と高温に
なつたことによつて、上記循環路内の気体の体積
が増加し、この循環路内で体積増加した気体は、
脱着された水蒸気とともに流路11b、切換えバ
ルブ12および凝縮器7を通つて大気中に放出さ
れる。このとき、上記循環路から流出する気体中
の水蒸気は、凝縮器7で凝縮し、受水槽13に貯
わえられるが、この凝縮器7の温度で決まる飽和
蒸気圧に相当する水蒸気は空気とともに大気中に
放出され損失となる。しかし、第2の収容部1B
および加熱室3bの中に当初入つていた空気は、
脱着する水蒸気量に比べ、わずかであり、勿論そ
の量が限られているので、次々に発生する水蒸気
によつて全部排出されて、実質的に水蒸気のみが
上記循環路内を循環する状態になる。この水蒸気
のみとなつた状態では、上記循環路内の圧力は、
凝縮器7を介して大気に開放されているので、常
に約1気圧である。また、上記循環路内を循環し
ている気体は水蒸気のみであり、脱着した水蒸気
に相当する量の水蒸気は凝縮器7に押し出され、
ここで水となつて、受水槽13内に貯わえられ
る。このようにして、吸着剤充填層1bの水分が
充分脱着された段階で脱着過程が完了する。
In the suction process in the first storage section 1A, first, the suction port side door 8a of the first storage section 1A is
and open the discharge port side door 9a, and open the second storage section 1B.
The suction port side door 8b and the discharge port side door 9b are closed, and the switching valve 12 is switched so that the flow path 11b and the condenser 7 are connected. Next, the adsorption blower 6 is operated to draw adsorption air into the first storage section 1A from the suction port, and the adsorption air is brought into contact with the adsorbent packed bed 1a accommodated therein to perform an adsorption process. At this time, air that has been dried due to adsorption of moisture by the adsorbent packed layer 1a is discharged to the outside through the ventilation chamber 5. On the other hand, when the first accommodating part 1A is in the adsorption process, it is desirable that the desorption process in the second accommodating part 1B is performed. In this process of attaching and detaching the second accommodating part 1B, the second accommodating part 1B
With the suction port side door 8b and the discharge port side door 9b closed, the circulation blower 10b is operated to heat the air in the heating chamber 3b in the heating chamber 4b while passing the air through the second air circulation port 2b. A circulation path formed by the housing portion 1B and the heating chamber 3b is circulated. Then, by the air heated in the heating chamber 3b,
The purpose is to heat the adsorbent-filled layer 1b in the second housing portion 1B to convert moisture previously adsorbed into the adsorbent-filled layer 1b into water vapor and desorb it. In this way, when water vapor is desorbed from the adsorbent packed bed 1b, the volume of gas in the circulation path increases due to the generation of water vapor due to desorption and the high temperature, and the volume of gas in this circulation path increases. The increased gas is
The desorbed water vapor is discharged into the atmosphere through the flow path 11b, the switching valve 12, and the condenser 7. At this time, the water vapor in the gas flowing out from the circulation path is condensed in the condenser 7 and stored in the water receiving tank 13, but the water vapor corresponding to the saturated vapor pressure determined by the temperature of the condenser 7 is together with the air. It is released into the atmosphere and becomes a loss. However, the second storage section 1B
And the air that was initially in the heating chamber 3b is
Since the amount of water vapor is small compared to the amount of water vapor that is desorbed, and of course the amount is limited, it is all exhausted by the water vapor that is generated one after another, and essentially only water vapor circulates in the above circulation path. . In this state where there is only water vapor, the pressure in the above circulation path is
Since it is open to the atmosphere via the condenser 7, the pressure is always about 1 atmosphere. Further, the gas circulating in the circulation path is only water vapor, and the amount of water vapor equivalent to the desorbed water vapor is pushed out to the condenser 7.
Here, it becomes water and is stored in the water receiving tank 13. In this way, the desorption process is completed when the water content of the adsorbent packed bed 1b is sufficiently desorbed.

以上説明した吸着過程と脱着過程とを、第1、
第2の収容部1A,1Bに交互に行わせることに
よつて、連続的に空気中の水分から水を得ること
ができる。
The adsorption process and desorption process explained above are explained as follows:
By making the second accommodating parts 1A and 1B perform this process alternately, water can be continuously obtained from the moisture in the air.

このような先行技術による造水装置では、水分
吸着用空気を第1の収容部1Aまたは第2の収容
部1B内へ吸込み外部へ排出するまでの流通路に
は、圧損を増大させるような配管やバルブを使用
していないので、省エネルギー化と小形化とを図
る上では望ましい構造である。ところで、運転休
止時に積載容積に制限のあるコンテナ、トレーラ
などによつて運搬できるような形状にし、しかも
造水能力をできるだけ大きくしようとすれば、第
1,第2の収容部1A,1B、吸着用ブロワ6お
よび凝縮器7の形状は造水能力に応じた大きさに
保持しつつ、流気室5のみの形状を小さくする必
要がある。そうすると、吸着用ブロワ6と凝縮器
7とが通気室5内に占める容積が大きくなり、通
気室5内を通る排出空気の流れに乱れが生じて圧
損が増大するようになり、造水能力の増大を図る
ことは容易ではないという問題があつた。
In such a fresh water generation device according to the prior art, the flow path from which air for moisture adsorption is sucked into the first storage section 1A or the second storage section 1B and discharged to the outside is equipped with piping that increases pressure loss. Since it does not use any valves or valves, it is a desirable structure in terms of energy saving and miniaturization. By the way, if you want to make the shape so that it can be transported by a container, trailer, etc. with a limited loading capacity when the operation is stopped, and also to increase the water production capacity as much as possible, the first and second storage parts 1A, 1B, adsorption It is necessary to keep the shape of the blower 6 and the condenser 7 to a size corresponding to the fresh water generation capacity, while reducing the shape of only the flow chamber 5. As a result, the volume occupied by the adsorption blower 6 and the condenser 7 in the ventilation chamber 5 becomes large, causing turbulence in the flow of discharged air passing through the ventilation chamber 5, increasing pressure loss, and reducing the water production capacity. The problem was that it was not easy to increase the number of people.

この発明は、上述の問題点に鑑みてなされたも
ので、装置の運転休止時には吸着用ブロワと凝縮
器とを通気室内に格納できるようにするととも
に、運転時にはこれらの吸着用ブロワと凝縮器と
を通気室内から引出せるようにすることによつ
て、運転休止時における形状を小さくするととも
に造水能力の大きい造水装置を提供することを目
的とする。
This invention was made in view of the above-mentioned problems, and allows the adsorption blower and condenser to be stored in the ventilation chamber when the device is not in operation, and also allows the adsorption blower and condenser to be stored in the ventilation chamber when the device is not in operation. It is an object of the present invention to provide a water generating device which has a small size during suspension of operation and has a large fresh water generating capacity by making it possible to draw out the water from the ventilation chamber.

第4図はこの発明の一実施例の運転休止時にお
ける状態を模式的に示す平面図、第5図は第4図
の―線での断面図、第6図は第5図の―
線での断面図、第7図は第5図の―線での断
面図、第8図はこの実施例の運転時における状態
を模式的に示す平面図、第9図は第8図の―
線での断面図である。この実施例では通気室の両
側に外へ引出せる吸着用ブロワおよび凝縮器を1
組ずつ計2組設けられている。
FIG. 4 is a plan view schematically showing the state of an embodiment of the present invention when the operation is stopped, FIG. 5 is a cross-sectional view taken along the line --- in FIG.
7 is a cross-sectional view taken along line - of FIG. 5, FIG. 8 is a plan view schematically showing the state of this embodiment during operation, and FIG. 9 is a cross-sectional view taken along line - of FIG. 8.
FIG. In this embodiment, one adsorption blower and one condenser are installed on both sides of the ventilation chamber.
There are two sets in total.

図において、15mは一方の吸着用ブロワ6m
および凝縮器7mを取り囲んで保持し通気室5の
一方の側板外へ引出せるように構成された筒状の
第1の保持体、15nは他方の吸着用ブロワ6n
および凝縮器7nを取り囲んで保持し通気室5の
他方の側板外へ引出せるように構成された筒状の
第2の保持体、16mは筒状の第1の保持体15
mの底板に設けられ、この第1の保持体15mを
案内する第1の案内レール、16nは筒状の第2
の保持体15nの底板に設けられ、この第2の保
持体15nを案内する第2の案内レール、17m
および17nはそれぞれ第1の案内レール16m
および第2の案内レール16nの案内溝に挿入さ
れこれらの第1,第2の案内レール16m,16
nを容易に移動可能にするためのローラ、18m
および18nはそれぞれ通気室5の底板に固定さ
れローラ17mおよびローラ17nを支持する第
1および第2のローラ受けである。なお、吸込み
口側扉8aおよび排出口側扉9aはそれぞれ第1
の収容部1Aの吸込み口および排出口を、それぞ
れの上下側板の開口端部の各中央部を支点して開
閉し、吸込み口側扉8bおよび排出口側扉9bは
それぞれ第2の収容部1Bの吸込み口および排出
口を、それぞれの上下側板の開口端部の各中央部
を支点として開閉するようになつている。また、
流路11amおよび11bmはそれぞれの一端が第
1の収容部1Aと加熱室3aとで形成された循環
路および第2収容部1Bと加熱室3bとで形成さ
れた循環路に連通するように接続され、それぞれ
の他端が切換えバルブ12mを介して凝縮器7m
に自在導管で接続されるとともに、流路11an
および11bnはそれぞれの一端が第1の収容部
1Aと加熱室3aとで形成された循環路および第
2の収容部1Bと加熱室3bとで形成された循環
路に連通するように接続され、それぞれの他端が
切換えバルブ12nを介して凝縮器7nに自在導
管で接続されている。
In the figure, 15m is 6m for one adsorption blower.
and a cylindrical first holder configured to surround and hold the condenser 7m and be pulled out from one side plate of the ventilation chamber 5; 15n is the other adsorption blower 6n;
and a cylindrical second holder configured to surround and hold the condenser 7n and be drawn out of the other side plate of the ventilation chamber 5; 16m is a cylindrical first holder 15;
A first guide rail 16n is provided on the bottom plate of the first holding body 15m and guides the first holding body 15m, and a second cylindrical guide rail 16n is provided on the bottom plate of the first holding body 15m.
A second guide rail 17m is provided on the bottom plate of the second holder 15n and guides the second holder 15n.
and 17n are the first guide rails 16m, respectively.
and inserted into the guide groove of the second guide rail 16n, and these first and second guide rails 16m, 16
Roller to make n easily movable, 18m
and 18n are first and second roller supports fixed to the bottom plate of the ventilation chamber 5 and supporting the rollers 17m and 17n, respectively. Note that the suction port side door 8a and the discharge port side door 9a are the first
The suction port and the discharge port of the storage section 1A are opened and closed using the central portions of the opening ends of the upper and lower side plates as supporting points, and the suction port side door 8b and the discharge port side door 9b are respectively connected to the second storage section 1B. The suction port and the discharge port are opened and closed using the central portions of the opening ends of the upper and lower side plates as fulcrums. Also,
The channels 11am and 11bm are connected such that one end thereof communicates with a circulation path formed by the first storage section 1A and the heating chamber 3a and a circulation path formed by the second storage section 1B and the heating chamber 3b. and the other end of each is connected to the condenser 7m via the switching valve 12m.
is connected to the flow path 11an by a flexible conduit.
and 11bn are connected such that one end thereof communicates with a circulation path formed by the first storage section 1A and the heating chamber 3a and a circulation path formed by the second storage section 1B and the heating chamber 3b, The other end of each is connected via a switching valve 12n to a condenser 7n via a flexible conduit.

この実施例の造水装置では、運転休止時におい
ては、吸着用ブロワ6mおよび凝縮器7mを保持
する筒状の第1の保持体15m、並びに吸着用ブ
ロワ6nおよび凝縮器7nを保持する筒状の第2
の保持体15nを通気室5内に格納し、運転時に
おいては、これらの第1、第2の保持体15m,
15nを通気室5内から引出して使用するが、こ
の運転時における動作については、第1図〜第3
図に示した先行技術による造水装置の動作から容
易に理解できるので、ここではその説明を省略す
る。
In the fresh water generating apparatus of this embodiment, when the operation is stopped, a cylindrical first holder 15m that holds an adsorption blower 6m and a condenser 7m, and a cylindrical first holder 15m that holds an adsorption blower 6n and a condenser 7n are used. the second of
The holding bodies 15n are stored in the ventilation chamber 5, and during operation, these first and second holding bodies 15m,
15n is pulled out from inside the ventilation chamber 5, and its operation during this operation is shown in Figures 1 to 3.
Since it can be easily understood from the operation of the prior art water generating apparatus shown in the figure, the explanation thereof will be omitted here.

このように、この実施例の造水装置では、通気
室5の形状を小さくして、吸着用ブロワ6m,6
nおよび凝縮器7m,7nの通気室5内に占める
容積が大きくなつた場合においても、運転時に
は、吸着用ブロワ6m,6nおよび凝縮器7m,
7nを通気室5内から引出して使用するので、先
行技術による装置のように、通気室5内を通る排
出空気の流れに乱れが生じて圧損が増大するよう
なことがなく、造水能力の増大を図ることができ
る。また、運転休止時には、吸着用ブロワ6m,
6nおよび凝縮器7m,7nを通気室5内に格納
することができるので、装置全体の形状を小さく
することができる。従つて、造水能力の増大を図
りながら、積載容積に制限のあるコンテナ、トレ
ーラなどによる運搬に適した形状にすることがで
きる。
In this way, in the fresh water generator of this embodiment, the shape of the ventilation chamber 5 is made small, and the adsorption blowers 6m, 6
Even if the volume occupied in the ventilation chamber 5 by the adsorption blowers 6m, 6n and the condensers 7m, 7n increases during operation, the adsorption blowers 6m, 6n and the condensers 7m, 7n
7n is drawn out from inside the ventilation chamber 5 and used, so there is no turbulence in the flow of discharged air passing through the ventilation chamber 5 and an increase in pressure drop, unlike in devices according to the prior art, and the fresh water production capacity is reduced. It is possible to increase the amount. In addition, when the operation is stopped, a 6m adsorption blower,
6n and the condensers 7m, 7n can be housed in the ventilation chamber 5, so the overall size of the device can be reduced. Therefore, it is possible to increase the water generation capacity while making the shape suitable for transportation by a container, trailer, etc. that has a limited loading capacity.

この実施例では、吸着用ブロワ6mおよび凝縮
器7mを保持する第1の保持体15mと吸着用ブ
ロワ6nおよび凝縮器7nを保持する第2の保持
体15nとを設けたが、必ずしも第1の保持体1
5mと第2の保持体15nとの両方を設ける必要
がなく、これらの第1、第2の保持体15m,1
5nのいずれか一方を設けるようにしてもよい。
また、この実施例では、第1の収容部1Aおよび
第2の収容部1Bのそれぞれの断面形状を四角形
にしたが、必ずしも四角形にする必要がなく、そ
の他の形状にしてもよい。
In this embodiment, a first holder 15m that holds an adsorption blower 6m and a condenser 7m and a second holder 15n that holds an adsorption blower 6n and a condenser 7n are provided. Holder 1
It is not necessary to provide both the first and second holding bodies 15m and 15n.
5n may be provided.
Further, in this embodiment, each of the first accommodating part 1A and the second accommodating part 1B has a rectangular cross-sectional shape, but it is not necessarily necessary to make it a rectangular shape, and other shapes may be used.

なお、この実施例はこの発明の一例を示したも
のに過ぎず、この発明の趣旨を逸脱することな
く、種々の変形が可能である。例えば、(イ)加熱室
3a,3bを第1,第2の収容部1A,1Bの上
部側板以外の側板に設けること、(ロ)吸着用ブロワ
6m,6nを押込み形にすること、(ハ)吸込み口側
扉8a,8bおよび排出口側扉9a,9bを引き
戸のようにすること、(ニ)吸着用ブロワ6m,6n
と凝縮器7m,7nとの位置関係を入れ換えるこ
と、(ホ)吸着剤充填層1a,1bを円筒形にするこ
となどいずれも支障なく実施することができる。
また、この実施例で用いる吸着剤充填層1a,1
bの吸着剤は、モレキユラーシーブ3A,同4
A,同5A,同10X,同13Xなどのゼオライ
ト、シリカゲル、アルミナゲル、シリカアルミ
ナ、活性アルミナ、活性炭、活性ボーキサイト、
活性白土など一般に固体吸着剤として用いられる
ものであればよい。また、臭化リチウム、塩化リ
チウムなど一般に水溶液として用いられる吸収剤
は、アルミナ、アスベストなどの適当な担体に担
持させて吸着剤として使用することができる。こ
れら吸着剤の形状は、粒、球、ペレツトダブレツ
トなど支障なく使用できる。更に、蜂の巣状など
の吸着剤を使用したいわゆるパラレルパツセージ
形充填層とすることもできる。これらの吸着剤の
選択は、その吸着特性と気温や湿度とを勘案して
行い、これらの吸着剤の吸着および脱着の操作条
件は、用いる吸着剤に応じて、適宜選択され、特
に制約はない。
Note that this embodiment is merely an example of the invention, and various modifications can be made without departing from the spirit of the invention. For example, (a) providing the heating chambers 3a and 3b on a side plate other than the upper side plate of the first and second housing parts 1A and 1B; (b) making the suction blowers 6m and 6n push-type; ) Make the suction port side doors 8a, 8b and the discharge port side doors 9a, 9b like sliding doors, (d) Adsorption blowers 6m, 6n.
It is possible to exchange the positional relationship between the adsorbent and the condensers 7m and 7n, and (e) to make the adsorbent packed beds 1a and 1b cylindrical, etc., without any problem.
In addition, the adsorbent packed layers 1a, 1 used in this example
The adsorbent for b is Molecular Sieve 3A, Molecular Sieve 4
Zeolites such as A, 5A, 10X, 13X, silica gel, alumina gel, silica alumina, activated alumina, activated carbon, activated bauxite,
Any material that is generally used as a solid adsorbent such as activated clay may be used. Further, absorbents such as lithium bromide and lithium chloride that are generally used in the form of aqueous solutions can be used as adsorbents by being supported on a suitable carrier such as alumina or asbestos. These adsorbents can be used in any shape such as granules, spheres, pellet doublets, etc. without any problem. Furthermore, it is also possible to form a so-called parallel passage type packed bed using a honeycomb-like adsorbent or the like. These adsorbents are selected by taking into consideration their adsorption characteristics, temperature and humidity, and the operating conditions for adsorption and desorption of these adsorbents are selected as appropriate depending on the adsorbent used, and there are no particular restrictions. .

この実施例では、受水槽13が開放されている
ものについて述べたが、密閉されているもの、も
しくは当初開放されていて循環路内の空気が実質
的に駆逐され脱着水蒸気で置換された後に密閉す
るもの、あるいはその他の変形のいずれにも、こ
の発明は適用できる。
In this embodiment, the case where the water receiving tank 13 is open has been described, but the case where the water receiving tank 13 is closed is closed, or it is opened initially and the air in the circulation path is substantially expelled and replaced with desorbed water vapor, and then the tank is closed. The present invention can be applied to any of the following.

なお、上記説明では、この発明を大気中の水分
を原料として水を得る場合について述べたが、必
ずしも大気に限定されるものではない。
In the above description, the present invention has been described with respect to the case where water is obtained using moisture in the atmosphere as a raw material, but it is not necessarily limited to the atmosphere.

以上述べたように、この発明による造水装置に
よれば、気体送給装置と凝縮器とを一体に保持す
る保持体と、運転休止時には上記保持体を2基の
収容部の間に設けられた通気室内に格納し、運転
時には上記保持体を上記通気室外へ引出し得る引
出し機構を設けたので、通気室を小さくしても、
運転時においては気体送給装置および凝縮器が通
気室外へ引出されるので、従来の装置のように通
気室内の圧損が増大するようなことはなく、また
運転休止時においては装置全体の形状を小さくす
ることができ積載容積に制限のあるコンテナ、ト
レーラ等による運搬に適した形状とすることが出
来る。
As described above, according to the fresh water generating apparatus according to the present invention, there is provided a holder that holds the gas supply device and the condenser together, and a holder that is provided between the two accommodating parts when the operation is stopped. The holding body is stored in the ventilation chamber, and a pull-out mechanism is provided that can pull the holding body out of the ventilation chamber during operation, so even if the ventilation chamber is made smaller,
During operation, the gas supply device and condenser are pulled out of the ventilation chamber, so the pressure drop inside the ventilation chamber does not increase as in conventional devices, and the shape of the entire device can be changed when the system is out of operation. It can be made small and has a shape suitable for transportation by containers, trailers, etc. with limited loading capacity.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は先行技術による造水装置の一例を模式
的に示す平面図、第2図は第1図の―線での
断面図、第3図は第2図の―線での断面図、
第4図はこの発明の一実施例の運転休止時におけ
る状態を模式的に示す平面図、第5図は第4図の
―線での断面図、第6図は第5図の―線
での断面図、第7図は第5図の―線での断面
図、第8図は上記実施例の運転時における状態を
模式的に示す平面図、第9図は第8図の―線
での断面図である。 図において、1Aおよび1Bは第1および第2
の収容部、1aおよび1bはそれぞれ吸着剤充填
層、3aおよび3bはそれぞれ加熱室、5は通気
室、6,6mおよび6nはそれぞれ吸着用ブロワ
(気体送給装置)、7,7mおよび7nはそれぞれ
凝縮器、8aおよび8bはそれぞれ吸込み口側扉
(開閉手段)、9aおよび9bはそれぞれ排出口側
扉(開閉手段)、10aおよび10bはそれぞれ
循環用ブロワ(循環装置)、15mは吸着用ブロ
ワ6mおよび凝縮器7mを保持する第1の保持
体、15nは吸着用ブロワ6nおよび凝縮器7n
を保持する第2の保持体である。なお、図中同一
符号はそれぞれ同一もしくは相当部分を示す。
FIG. 1 is a plan view schematically showing an example of a water generation device according to the prior art, FIG. 2 is a cross-sectional view taken along the line - in FIG. 1, and FIG. 3 is a cross-sectional view taken along the line - in FIG.
FIG. 4 is a plan view schematically showing the state of an embodiment of the present invention when the operation is stopped, FIG. 5 is a sectional view taken along the line --- in FIG. 4, and FIG. FIG. 7 is a sectional view taken along line - in FIG. 5, FIG. 8 is a plan view schematically showing the state of the above embodiment during operation, and FIG. 9 is taken along line - in FIG. FIG. In the figure, 1A and 1B are the first and second
1a and 1b are adsorbent packed beds, 3a and 3b are heating chambers, 5 is a ventilation chamber, 6, 6m and 6n are adsorption blowers (gas supply devices), and 7, 7m and 7n are adsorption chambers. 8a and 8b are each a suction port side door (opening/closing means), 9a and 9b are each a discharge port side door (opening/closing means), 10a and 10b are each a circulation blower (circulation device), and 15m is an adsorption blower. 6m and a first holding body holding a condenser 7m; 15n is an adsorption blower 6n and a condenser 7n;
This is the second holder that holds the . Note that the same reference numerals in the figures indicate the same or corresponding parts.

Claims (1)

【特許請求の範囲】[Claims] 1 内部に水分吸着用の吸着剤充填層を収容しこ
の吸着剤充填層をはさんでその両側にそれぞれ気
体の吸込み口および排出口を有し、交互に吸着過
程と脱着過程とを繰り返す2基の収容部と、上記
吸込み口および排出口をそれぞれ開閉する開閉手
段と、この開閉手段が開かれて吸着過程にある上
記収容部に水分を含んだ気体を送給する気体送給
装置と、上記収容部と連通するよう設けられ内部
の気体を加熱する加熱室と、上記開閉手段が閉じ
られて脱着過程にある上記収容部と上記加熱室と
で形成される循環路を通つて上記加熱された気体
を循環させて上記吸着剤充填層に吸着された水分
を脱着させる循環装置と、上記気体送給装置によ
り冷却されるよう構成され上記脱着された水分を
凝縮させる凝縮器とを備えた造水装置において、
上記気体送給装置と上記凝縮器とを一体に保持す
る保持体と、運転休止時には上記保持体を上記2
基の収容部の間に設けられた通気室内に格納し、
運転時には上記保持体を上記通気室外へ引出し得
る引出し機構を設けたことを特徴とする造水装
置。
1 Two units that contain an adsorbent packed bed for moisture adsorption inside, have a gas suction port and a gas discharge port on both sides of the adsorbent packed bed, and repeat the adsorption process and desorption process alternately. an accommodating section, an opening/closing means for respectively opening and closing the suction port and the exhaust port, a gas feeding device for supplying a moisture-containing gas to the accommodating section in the adsorption process when the opening/closing means is opened; The heated gas is heated through a circulation path formed by a heating chamber that is provided to communicate with the housing section and heats the gas inside, and the heating chamber and the housing section that is in the desorption process when the opening/closing means is closed. A water production system comprising: a circulation device that circulates gas to desorb moisture adsorbed by the adsorbent packed bed; and a condenser that is configured to be cooled by the gas supply device and condenses the desorbed moisture. In the device,
A holder that holds the gas supply device and the condenser together; and a holder that holds the gas supply device and the condenser together;
It is stored in a ventilation chamber provided between the storage parts of the base,
A freshwater generating device characterized in that a drawer mechanism is provided that can draw the holding body out of the ventilation chamber during operation.
JP8567179A 1979-05-09 1979-07-03 Water making apparatus Granted JPS567628A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP8567179A JPS567628A (en) 1979-07-03 1979-07-03 Water making apparatus
DE8080102317T DE3064739D1 (en) 1979-05-09 1980-04-29 Water producing apparatus
EP80102317A EP0019143B1 (en) 1979-05-09 1980-04-29 Water producing apparatus
US06/147,115 US4299599A (en) 1979-05-09 1980-05-06 Water producing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8567179A JPS567628A (en) 1979-07-03 1979-07-03 Water making apparatus

Publications (2)

Publication Number Publication Date
JPS567628A JPS567628A (en) 1981-01-26
JPS6317487B2 true JPS6317487B2 (en) 1988-04-14

Family

ID=13865281

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8567179A Granted JPS567628A (en) 1979-05-09 1979-07-03 Water making apparatus

Country Status (1)

Country Link
JP (1) JPS567628A (en)

Also Published As

Publication number Publication date
JPS567628A (en) 1981-01-26

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