JPS594725Y2 - Simple water generator - Google Patents

Simple water generator

Info

Publication number
JPS594725Y2
JPS594725Y2 JP4206683U JP4206683U JPS594725Y2 JP S594725 Y2 JPS594725 Y2 JP S594725Y2 JP 4206683 U JP4206683 U JP 4206683U JP 4206683 U JP4206683 U JP 4206683U JP S594725 Y2 JPS594725 Y2 JP S594725Y2
Authority
JP
Japan
Prior art keywords
membrane
water
collection chamber
water collection
permeated water
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
JP4206683U
Other languages
Japanese (ja)
Other versions
JPS58174293U (en
Inventor
輝嘉 塚本
Original Assignee
荏原インフイルコ株式会社
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 荏原インフイルコ株式会社 filed Critical 荏原インフイルコ株式会社
Priority to JP4206683U priority Critical patent/JPS594725Y2/en
Publication of JPS58174293U publication Critical patent/JPS58174293U/en
Application granted granted Critical
Publication of JPS594725Y2 publication Critical patent/JPS594725Y2/en
Expired legal-status Critical Current

Links

Description

【考案の詳細な説明】 本考案は、航空機の海上不時着、船舶の海上遭難時、ヨ
ツト、ボートなどの小型船の就航時などにおける非常用
の簡易造水装置に関するものである。
[Detailed Description of the Invention] The present invention relates to a simple water generating device for emergency purposes such as when an aircraft makes an emergency landing at sea, when a ship is lost at sea, and when a small vessel such as a yacht or boat is put into service.

普通航空機の海上不時着時には、救命ボートが自動的に
用意され、乗客は一時救命されるものの、発見が長びく
と当然のことながら海上滞留を強いられる。
When a normal aircraft makes an emergency landing at sea, a lifeboat is automatically prepared and the passengers are temporarily rescued, but if the aircraft is discovered for a long time, it is naturally forced to stay at sea.

また、外洋を航行する船舶の遭難時においても同様で、
一時的に救命ボート、筏などによって救命されても、長
期にわたる海上滞留を余儀なくされる場合もある。
The same applies when a ship sailing on the open sea is in distress.
Even if a person is temporarily rescued by a lifeboat or raft, they may be forced to stay at sea for a long time.

このような事故において、必要なのは飲料水の確保であ
るが、周囲海水にとりがこまれている中で飲料水を確保
できないことは、死へ直結する危惧がある。
In such accidents, it is necessary to secure drinking water, but there is a risk that not being able to secure drinking water when the surrounding seawater is trapped can lead directly to death.

これと同じことは、事故にかぎらず最近よく行なわれる
ヨツト、ボートによる外洋航海或いは海釣りなどで、こ
のような場合も飲料水の確保は重要且つ必要なことであ
る。
The same thing is true not only for accidents, but also for ocean voyages by yachts and boats, sea fishing, etc., which are often carried out these days, and securing drinking water is important and necessary in such cases as well.

また航空機や船舶には、各乗員、乗客に個々に救命具が
用意されているが、現状では造水装置は何ら用意されて
おらず、やはり救命或いはその他用具に付設する簡易な
遣水装置は必要なものである。
In addition, although aircraft and ships are equipped with individual life preservers for each crew member and passenger, there are currently no water generators available, and a simple water supply device attached to rescue or other equipment is still necessary. It is something.

このような環境下で共通していることは、操作が極めて
容易であること、単純・軽量・小型そして人力以外の動
力源は皆無で電気エネルギー、燃料などを使用する必要
もなく、かつ故障のない、長期に亙って使用し得る遣水
装置が要求されることである。
What these environments have in common is that they are extremely easy to operate, are simple, lightweight, small, require no power source other than human power, do not require the use of electrical energy or fuel, and are highly resistant to breakdowns. However, there is a need for a water supply system that can be used for a long period of time.

本考案は、人力以外の動力源を要せず、軽量、小型で故
障のない、しかも取扱いの極めて簡便な遣水装置を提供
することを目的とするものである。
The object of the present invention is to provide a water dispensing device that does not require any power source other than human power, is lightweight, compact, and trouble-free, and is extremely easy to handle.

本考案は、膜透過水と濃縮液とに分離し得る透過膜を装
着したセルの膜透過水側と隔壁をもって隔離された膜透
過水集水室を設け、前記膜透過水側と該膜透過水集水室
とは隔壁に設けた連通口をもって連通し、かつ該連通口
に膜透過が進行中は前記膜透過水集水室側に開となる逆
止弁を設けると共に、前記膜透過水集水室は大気に開放
連通せしめたことを特徴とする簡易造水装置で、該セル
を水中に沈降せしめることによって水圧が分離の駆動力
となって、膜透過側に清水を得んとするものである。
The present invention provides a membrane-permeated water collection chamber separated by a partition wall from the membrane-permeated water side of a cell equipped with a permeable membrane capable of separating membrane-permeated water and concentrated liquid, and the membrane-permeated water side and the membrane-permeated water side are separated from each other by a partition wall. The water collection chamber communicates with the water collection chamber through a communication port provided in the partition wall, and the communication port is provided with a check valve that opens to the membrane permeation water collection chamber side while membrane permeation is in progress, and the membrane permeation water is connected to the water collection chamber. This is a simple water production device characterized by a water collection chamber that is open to the atmosphere, and by allowing the cell to settle in water, the water pressure becomes the driving force for separation, and fresh water is obtained on the membrane permeation side. It is something.

本考案においては、膜透過の駆動力は水圧であって、膜
を装着したセルを海中、水中へ投入することによって容
易に得られる天然のエネルギーであり、何ら動力源を必
要としないから、そのための設備を要せず、極めて軽量
・小型化した装置となり得る。
In this invention, the driving force for membrane permeation is water pressure, which is a natural energy that can be easily obtained by inserting a cell equipped with a membrane into the sea, and does not require any power source. The device does not require any additional equipment and can be extremely lightweight and compact.

とくに本考案の一失特徴は、前記したように膜透過水集
水室が大気に開放連通せしめられ、しかも前記隔壁に設
けた連通口に、正常な膜透過が進行中は膜透過水集水室
側に開となる逆止弁を設けたことである。
Particularly, the disadvantageous feature of the present invention is that the membrane permeated water collection chamber is opened to the atmosphere as described above, and furthermore, the membrane permeated water collection chamber is connected to the communication port provided in the partition wall during normal membrane permeation. A check valve that opens on the room side was installed.

このようにしたことによって、次の実施例において述べ
る如く、極めて大きな効果を得ることが出来るのである
By doing so, extremely large effects can be obtained, as will be described in the next embodiment.

本考案の実施例を図面について説明すれば、第1図示例
において、膜透過水と濃縮水とに分離し得る平板構造の
浸透膜1を耐圧性透水性支持体2で支持装着したセル3
内には、膜透過水側4に連通ずる膜透過水集水室5が設
けられ、これら連通部6には膜透過水集水室5側へのみ
開く逆止弁7が付設されている。
To explain the embodiment of the present invention with reference to the drawings, in the first illustrated example, a cell 3 has a permeable membrane 1 with a flat plate structure capable of separating membrane permeated water and concentrated water supported by a pressure-resistant water-permeable support 2.
A membrane permeated water collection chamber 5 communicating with the membrane permeated water side 4 is provided inside, and a check valve 7 that opens only to the membrane permeated water collection chamber 5 side is attached to these communication parts 6.

また、膜透過水集水室5に開口するセル3の接続部8に
は耐圧性の連通管9の一端を接続し、十分な長さとして
他端を大気に開放しである。
Further, one end of a pressure-resistant communication pipe 9 is connected to the connection part 8 of the cell 3 that opens into the membrane permeated water collection chamber 5, and the other end is made of sufficient length and opened to the atmosphere.

図中10は浸透膜1を保護する網体、11は鎖、12は
セル沈降用の重錘である。
In the figure, 10 is a net that protects the permeable membrane 1, 11 is a chain, and 12 is a weight for cell sedimentation.

しかして、海水から淡水を得たとする場合について説明
すると、海水の塩分濃度は3.5%程度で、その浸透圧
は約25kgf/cm2である。
Assuming that fresh water is obtained from seawater, the salinity of seawater is about 3.5%, and the osmotic pressure is about 25 kgf/cm2.

セルには高脱塩率、約99.9〜98%程度の逆浸透膜
を装着し、それを水深280〜300 m以上の所へ沈
めることによって、その水圧が浸透圧以上になるために
はじめて逆浸透現象が起こり、浸透膜1により脱塩が進
行し淡水が支持体2を透過して膜透過水側4に至って、
さらに逆止弁7を経て膜透過水集水室5内に至り、該集
水室5内が満杯になると連通管9内にも入ってゆく。
The cell is equipped with a reverse osmosis membrane with a high salt removal rate of about 99.9 to 98%, and by submerging it to a depth of 280 to 300 m or more, the water pressure becomes higher than the osmotic pressure. A reverse osmosis phenomenon occurs, desalination progresses through the osmotic membrane 1, and fresh water permeates through the support 2 and reaches the permeated water side 4 of the membrane.
Furthermore, the permeated water flows through the check valve 7 into the membrane-permeated water collection chamber 5, and when the water collection chamber 5 is full, it also enters the communication pipe 9.

かくて、所定の時間経過後、セル3を水面上に引きあげ
るが、水圧によって膜透過がおこっている内は逆止弁7
は膜透過水集水室5側へ開いているが、水面上に引き上
げるにつれて膜面への水圧が減少し、海水の浸透圧に相
当する深度的250m程度に至れば逆浸透現象は実質的
に停止し、これよりも深度が小さいところでは膜透過水
側4から正浸透が起こり、膜透過水は浸透膜1を経て外
部へ浸透をはじめるから水の移動が生じ、ここで逆止弁
7は自然に閉じることとなってセル3内の淡水の支持体
2、浸透膜1を経由する浸透が阻止されるためにセル3
内の膜透過水の可成りの量は水面上に引きあげられる。
Thus, after a predetermined period of time has elapsed, the cell 3 is pulled up above the water surface, but while membrane permeation is occurring due to water pressure, the check valve 7 is closed.
is open to the membrane permeated water collection chamber 5 side, but the water pressure on the membrane surface decreases as it is raised above the water surface, and when it reaches a depth of about 250 m, which corresponds to the osmotic pressure of seawater, the reverse osmosis phenomenon becomes virtually impossible. At a depth smaller than this, forward osmosis occurs from the membrane permeated water side 4, and the membrane permeated water begins to permeate to the outside through the osmotic membrane 1, causing water movement, and here the check valve 7 The cell 3 closes naturally and prevents the fresh water in the cell 3 from permeating through the support 2 and the osmotic membrane 1.
A significant amount of the water that permeates through the membrane is pulled up to the surface of the water.

また、第2図示例は、膜透過水集水室5をセル3と別個
に耐圧性に形成し、これとセル3の膜透過水側4と逆止
弁7を介して連通させたもので、その作用は第1図示例
と同様である。
In the second illustrated example, a membrane permeate water collection chamber 5 is formed separately from the cell 3 to be pressure resistant, and is communicated with the membrane permeate water side 4 of the cell 3 via a check valve 7. , its operation is similar to the first illustrated example.

第3図示例は、浸透膜1として外圧穴管型膜を使用した
例で、管内の支持体2内に膜透過水集水管4′を内装し
、この集水管4′を逆止弁7を介して膜透過水集水室5
に連通させたもので、その作用は第1図示例と同様であ
る。
The example shown in the third figure is an example in which an external pressure hole tube type membrane is used as the permeable membrane 1. A membrane permeate water collection tube 4' is installed inside the support 2 inside the tube, and the water collection tube 4' is connected to a check valve 7. Through the membrane permeate water collection chamber 5
The operation is the same as in the first illustrated example.

また、第3図示例の集水管4′と膜透過水集水室5は、
第4図示例の如く、膜透過水集水室5の底部で連通させ
ることもできる。
In addition, the water collection pipe 4' and membrane permeated water collection chamber 5 in the third illustrated example are as follows:
As shown in the fourth illustrated example, communication can also be made at the bottom of the membrane permeated water collection chamber 5.

このように本考案においては、膜透過側と集水室間の連
絡通路に、膜透過が進行しているときには集水室側へ開
となる逆止弁を設けることによって、膜透過水と水位が
浸透膜装着部位よりも高くなって浸透膜が完全に膜透過
水に浸漬された状態になっても、前記第1図実施例に示
したように、引き揚げ時に逆止弁が働いて海水側へ逆流
することが無いために、透過水のほぼ全量を引き上げ利
用することができ、しかも、膜透過側が浸透膜を浸漬す
る、しないに全く無関係であるために、浸透膜の配置が
極めて任意に遂行でき、膜面積を十分に大きくすること
ができるので、非常に効率よく遣水が可能である。
In this way, in the present invention, by providing a check valve in the communication passage between the membrane permeation side and the water collection chamber that opens to the water collection chamber side when membrane permeation is progressing, the membrane permeation water and water level can be controlled. Even if the osmotic membrane becomes higher than the osmotic membrane installation site and the osmotic membrane is completely immersed in the membrane-permeated water, the check valve operates at the time of salvage, and the seawater side Because there is no backflow to the membrane, almost the entire amount of permeated water can be pulled up and used. Moreover, since the permeate side has no relation to whether or not the permeate membrane is immersed, the arrangement of the permeate membrane can be extremely arbitrary. Since the membrane area can be made sufficiently large, it is possible to spray water very efficiently.

また、本考案においては、膜透過水側4と連通ずる集水
室5は連通管9によって大気圧に開放されており、その
ために、被処理水中へ投入した際の水圧を極めて有効に
利用できる。
Furthermore, in the present invention, the water collection chamber 5 that communicates with the membrane permeated water side 4 is open to atmospheric pressure through the communication pipe 9, so that the water pressure when introduced into the water to be treated can be used extremely effectively. .

このようなことから本考案においては、装置容積当りの
有効膜面積の増水、水圧の有効利用がはかれるので、効
率良く清水の膜透過を遂行することができ、かつ引き揚
げ時においても膜透過によって得られた膜透過水を無駄
なく、はぼ全量回収利用することができる。
For this reason, in the present invention, the effective membrane area per unit volume is increased and water pressure is used effectively, so that fresh water can be efficiently permeated through the membrane, and even during salvage, the benefits can be obtained through membrane permeation. Almost all of the membrane-permeated water can be recovered and used without any waste.

なお、本考案において使用する浸透膜としては、アセチ
ルセルローズ、芳香族ポリアミド系膜をはじめ、多くの
有機、無機質の膜を利用し得るが、海水から飲料水を造
水するとき等脱塩を目的とするときは逆浸透膜を利用し
、濁りの分離のみを目的とするときはマイクロポーラス
膜乃至限外濾過膜でよい。
Note that many organic and inorganic membranes, including acetyl cellulose and aromatic polyamide membranes, can be used as the permeable membrane used in this invention, but it is not suitable for desalination purposes such as when producing drinking water from seawater. When the purpose is to remove turbidity, a reverse osmosis membrane is used, and when the purpose is only to separate turbidity, a microporous membrane or an ultrafiltration membrane may be used.

また膜の構造は、平板膜、内圧あるいは外圧式の管型膜
、糸状膜、中空糸膜、ロッド型、のりまき型等各種のも
のが使用される。
Various types of membrane structures are used, such as a flat plate membrane, an internal pressure or external pressure type tube membrane, a filament membrane, a hollow fiber membrane, a rod type, and a glue-type membrane.

また、海水から飲料に適する水を得る場合に使用する膜
は高い塩除去率の膜を使用するとよく、この場合の圧力
は少なくとも28〜30kgf/cm2を必要とするか
ら、約280〜300 m以上の水深にセルを沈める必
要があり、単なる懸濁性成分の除去の場合には、浸透膜
はマイクロポーラス膜乃至限外濾過膜でよく、水深も数
m乃至数10mで十分である。
In addition, when obtaining drinkable water from seawater, it is best to use a membrane with a high salt removal rate.In this case, the pressure needs to be at least 28 to 30 kgf/cm2, so it is better to use a membrane that has a high salt removal rate. In the case of simply removing suspended components, the permeation membrane may be a microporous membrane or an ultrafiltration membrane, and a water depth of several meters to several tens of meters is sufficient.

湖水の場合には、その溶解塩分量によっても異なるが、
脱塩水を得るには数10mでよい。
In the case of lake water, it varies depending on the amount of dissolved salt in the water, but
To obtain desalinated water, a distance of several tens of meters is sufficient.

何れにしてもその水深は、溶液の浸透圧のみでなく、膜
の特性によっても異なるから、これら両者を考慮して決
定し、溶液の浸透圧と膜透過水の浸透圧との差以上の圧
力が得られる水深が必要である。
In any case, the water depth depends not only on the osmotic pressure of the solution but also on the characteristics of the membrane, so it should be determined taking both of these factors into account, and the water depth should be determined at a pressure that is at least the difference between the osmotic pressure of the solution and the osmotic pressure of the water that permeates through the membrane. The depth of the water must be such that this can be achieved.

なお、膜透過水集水室と大気との連通管は耐圧性とし、
該連通管をセルの懸吊用網と独立もしくは束ねるか、連
通管自体を懸吊用網の役目を兼ねさせるようにしてもよ
いし、前記浸透膜1及び膜透過水側4は第1図のように
一側に限らず両側若しくはそれ以上に設けたり或いは全
周にわたるリング状に設けることもできる。
In addition, the communication pipe between the membrane permeated water collection chamber and the atmosphere should be pressure resistant.
The communication pipe may be independent from or bundled with the cell suspension network, or the communication pipe itself may also serve as the suspension network. It can be provided not only on one side but also on both sides or more, or in a ring shape covering the entire circumference.

本考案により、海水にとりかこまれている中でも必要な
飲料水の確保が容易にでき故障も少なく安全性の高い用
具とすることが可能であり、しかも何等外部からの動力
源を必要としないで単に水中に沈めるのみの極めて簡単
な操作によって容易に必要な飲料水等を得ることができ
るし、得られた清水の系外への流出を阻止し的確に収容
した状態で水中から引き揚げることが、極めて簡単な構
成によって実現でき、優れた遣水装置とすることか゛で
きる。
With this invention, it is possible to easily secure the necessary drinking water even when surrounded by seawater, and it is possible to create a highly safe tool with fewer breakdowns, and moreover, it does not require any external power source. The necessary drinking water can be easily obtained by simply submerging the water into the water, and the fresh water obtained can be pulled out of the water while being properly contained and prevented from flowing out of the system. It can be realized with an extremely simple configuration and can be an excellent water dispensing device.

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

第1図は本考案の一実施例を示す縦断面図、第2図は他
の実施例を示す縦断面図、第3図はさらに他の実施例を
示す縦断面図、第4図は第3図例の集水管4′と集水室
5との連通部の実施例を示す縦断面図の一部である。 1・・・・・・浸透膜、2・・・・・・支持体、3・・
・・・・セル、4・・・・・・膜透過水側、4′・・・
・・・集水管、5・・・・・・集水室、6・・・・・・
連通部、7・・・・・・逆止弁、9・・・・・・連通管
Fig. 1 is a longitudinal sectional view showing one embodiment of the present invention, Fig. 2 is a longitudinal sectional view showing another embodiment, Fig. 3 is a longitudinal sectional view showing still another embodiment, and Fig. 4 is a longitudinal sectional view showing another embodiment. 3 is a part of a vertical cross-sectional view showing an embodiment of the communication portion between the water collection pipe 4' and the water collection chamber 5 in the example shown in FIG. 1... Permeable membrane, 2... Support, 3...
...Cell, 4...Membrane permeated water side, 4'...
...Water collection pipe, 5...Water collection room, 6...
Communication portion, 7...Check valve, 9...Communication pipe.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 膜透過水と濃縮液とに分離し得る透過膜を装着したセル
の膜透過水側と隔壁をもって隔離された膜透過水集水室
を設け、前記膜透過水側と該膜透過水集水室とは隔壁に
設けた連通口をもって連通し、かつ該連通口に膜透過が
進行中は前記膜透過水集水室側に開となる逆止弁を設け
ると共に、前記膜透過水集水室は大気に開放連通せしめ
たことを特徴とする簡易造水装置。
A membrane-permeated water collection chamber is provided, which is separated by a partition wall from the membrane-permeated water side of a cell equipped with a permeable membrane capable of separating membrane-permeated water and concentrated liquid, and the membrane-permeated water side and the membrane-permeated water collection chamber are separated from each other by a partition wall. communicates with the membrane through a communication port provided in the partition wall, and a check valve is provided in the communication port that opens toward the membrane permeation water collection chamber while membrane permeation is in progress, and the membrane permeation water collection chamber A simple water generating device characterized by being open to the atmosphere.
JP4206683U 1983-03-25 1983-03-25 Simple water generator Expired JPS594725Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4206683U JPS594725Y2 (en) 1983-03-25 1983-03-25 Simple water generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4206683U JPS594725Y2 (en) 1983-03-25 1983-03-25 Simple water generator

Publications (2)

Publication Number Publication Date
JPS58174293U JPS58174293U (en) 1983-11-21
JPS594725Y2 true JPS594725Y2 (en) 1984-02-13

Family

ID=30053226

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4206683U Expired JPS594725Y2 (en) 1983-03-25 1983-03-25 Simple water generator

Country Status (1)

Country Link
JP (1) JPS594725Y2 (en)

Also Published As

Publication number Publication date
JPS58174293U (en) 1983-11-21

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