JPH02191586A - Device for desalting sea water - Google Patents

Device for desalting sea water

Info

Publication number
JPH02191586A
JPH02191586A JP1010774A JP1077489A JPH02191586A JP H02191586 A JPH02191586 A JP H02191586A JP 1010774 A JP1010774 A JP 1010774A JP 1077489 A JP1077489 A JP 1077489A JP H02191586 A JPH02191586 A JP H02191586A
Authority
JP
Japan
Prior art keywords
air
seawater
evaporator
water
sea 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.)
Pending
Application number
JP1010774A
Other languages
Japanese (ja)
Inventor
Fumiko Tateishi
立石 文子
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP1010774A priority Critical patent/JPH02191586A/en
Publication of JPH02191586A publication Critical patent/JPH02191586A/en
Pending legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination

Abstract

PURPOSE:To obtain inexpensive and good-quality potable water by supplying the warm sea water on the sea surface to a water contact device, such as cooling column for air conditioning, to bring the sea water into contact with the air and to evaporate the same, and then condensing this air via an air fin cooler by the cold waste sea water or the like used for ocean temp. difference power generation. CONSTITUTION:The warm sea water on the sea surface is supplied to to cooling column for air conditioning or the packed column resembling thereto or other gas-water contact device 103 where the sea water is brought into contact with the air and is evaporated under the atm. pressure. This air is condensed by the cold waste sea water used for the ocean temp. difference power generation or in some cases by the particularly pumped up sea water, via the air tin cooler 20, by which the carbon dioxide, oxygen, etc., separated in an evaporator 1 are again absorbed and the inexpensive and goodquality potable water is obtd.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は主として海洋温度差発電装置に併設し。[Detailed description of the invention] (Industrial application field) The present invention is mainly applied to an ocean temperature difference power generation device.

発tに使用した冷海水になお充分に残されている低温を
利用して温海水から発生する水蒸気を凝縮させ淡水を得
る海水の淡水化装置である。
This is a seawater desalination device that condenses water vapor generated from warm seawater to obtain fresh water by making use of the sufficiently low temperature still remaining in the cold seawater used for the initial steaming.

C従来技術とその問題点) 従来、海水淡水化プラントの主流となって来たのは多段
フラッシュ法であるが、この方法はボイラーにおいて化
石燃料な燃やすので、大気の炭酸ガス濃度を高める恐れ
があり、地球環境上好ましくないこととなる。また、そ
の為の装置も、圧力容器ないし真壁容器であり、かつ耐
海水腐食性の高価な材料を用いるので甚だ高価となる。
C) Conventional technology and its problems) Conventionally, the mainstream method for seawater desalination plants has been the multistage flash method, but since this method burns fossil fuels in the boiler, there is a risk of increasing the carbon dioxide concentration in the atmosphere. This is unfavorable for the global environment. Further, the equipment for this purpose is a pressure vessel or a solid-walled vessel, and is made of expensive materials that are resistant to seawater corrosion, making it extremely expensive.

また調造された淡水のコストもあまり安いとはいえない
Furthermore, the cost of prepared fresh water is not very cheap.

−万、海洋温度差発電には直接温海水を真窒で蒸発させ
てタービンを駆動し、その排気を冷海水で凝縮でせる直
接法と、冷媒を用いる間接法とがある。直接法において
は、電力と同時に淡水が↓造されるが、タービンが過大
となるため、実用化していない。間接法はほぼ実用化の
見通しがついているが、淡水は製造出来ない。
- There are two types of ocean thermal power generation: the direct method, in which warm seawater is directly evaporated with true nitrogen to drive a turbine, and the exhaust gas is condensed with cold seawater, and the indirect method, which uses a refrigerant. In the direct method, fresh water is produced at the same time as electricity, but it has not been put to practical use because the turbine would be too large. The indirect method has almost every prospect of practical application, but it cannot produce fresh water.

(発明の目的) 海洋温度差発電は安価な電力を得る他に海面の異常高温
(エルニーニョ現象)?緩和し、且つ深海底の栄養豊富
な海水を汲み上げて酸素の豊富な臨海水と混合するので
、そこにプランクトンが発生し、急場が形成されるとい
う大きなメリットがある。
(Purpose of the invention) In addition to obtaining inexpensive electricity, ocean thermal conversion power generation can also be used to reduce abnormally high temperatures at the sea surface (El Niño phenomenon). It has the great advantage of relaxing, nutrient-rich seawater from the deep seabed is pumped up and mixed with oxygen-rich coastal water, allowing plankton to form there and forming a rapid zone.

なおその上に、発電に使用したあとの冷海水の温度はな
お海面の海水温度より充分に低いので、その温度差を用
いて淡水をつくることが出来る。
Moreover, the temperature of cold seawater after being used for power generation is still sufficiently lower than the seawater temperature at the sea surface, so the temperature difference can be used to create fresh water.

たとえば、温海水と排斥海水の温度差が仮に16℃であ
ったとすると、3段ないし4段の多段フラッシュ蒸発法
が適用出来ることとなる。しかし温度が低いので装置が
高真空となり、設備が高価となる。
For example, if the temperature difference between warm seawater and expelled seawater is 16°C, a three- or four-stage multistage flash evaporation method can be applied. However, since the temperature is low, the device requires a high vacuum, making the equipment expensive.

海洋温度差発電に使用される海水の量は膨大であり、排
海水といえども、その利用出来るエネルギーは巨大であ
るから、多段フラッシュ法のようなエネルギーを高度に
利用する高価なプラントよりは、エネルギー効率は低く
とも、設備費の安いプラントの万が低コストの淡水をつ
くり得ることとなる。何故ならば、エネルギー源は無料
と考えてよいからである。
The amount of seawater used for ocean thermal power generation is enormous, and the amount of energy that can be used even with discharged seawater is enormous. Even if the energy efficiency is low, it is possible to produce fresh water at low cost using a plant with low equipment costs. This is because energy sources can be considered free.

本発明者は海洋温度差発[1C適する高性能な熱交換器
の開発に目処なつげることが出来たので、地球環境の悪
化を患える最近の世論に鑑みその実現を促進する意味に
おいて淡水化ブラットを併設し、従来より遥かに低コス
トで海水から淡水なつくることを検討し成案を得ること
が出来た。
The present inventor was able to reach a goal of developing a high-performance heat exchanger suitable for the ocean temperature difference [1C], and in view of the recent public opinion regarding the deterioration of the global environment, desalination We considered creating freshwater from seawater at a much lower cost than before by installing a BRADT, and were able to come up with a plan.

(発明の構成) すなわち、本発明によれば、海面の温海水を全制用冷却
塔ないしそれに類似の充填塔又はその他気水接触装置に
供給し、大2圧下で空気と接触させて蒸発させ、このを
気を海洋温度差発電に使用された冷たい排海水または場
合によっては特に汲み揚げた海水によりエヤーフィンク
ーラーを介して凝縮させることにより蒸発器で分離され
た炭酸ガス、酸素等を再び吸着させ、安価で良質な飲用
水を得ることを特徴とする海水の淡水化装置、が得られ
る。
(Structure of the Invention) That is, according to the present invention, warm seawater at the sea surface is supplied to an all-control cooling tower, a similar packed tower, or other air-water contact device, and brought into contact with air under two pressures to evaporate it. This air is then condensed via an air fin cooler with cold waste seawater used for ocean thermal power generation or, in some cases, pumped-up seawater, to re-adsorb carbon dioxide, oxygen, etc. separated in the evaporator. Thus, a seawater desalination device is obtained, which is characterized in that it can obtain inexpensive and high-quality drinking water.

本発明はさらに、円筒形蒸発器の両端の鏡板を貫く1本
の中空軸に連続気泡の発泡ガラス、発泡樹脂、焼結粒体
のごとき粗面を有する多孔質素材から成る円板多数なパ
ッキンをそれぞれの中間に挾んで固定し、該中空軸の一
端からは回転接手を介して海水な供給し、該中空軸の周
囲に明けられた小孔から前記円板に圧入して該円板の表
面に滲み出させ、またその他端は減速機付モーターに連
結されてゆるやかに回転させ、且つ該蒸発器の底部には
適当レベルに海水を溜めて前記円板の一部が漬かるよう
にして海水を該中空軸と該円板の周辺の両方から供給す
るとともに空気を流通させて該円板の粗面からの蒸発を
促進させ且つスケールが付かぬようにした蒸発装置を設
けたことを特徴とする海水の淡水化装置、を提供するも
のである。
The present invention further provides a hollow shaft that passes through end plates at both ends of the cylindrical evaporator, and a plurality of disk packings made of a porous material with a rough surface such as open-cell foamed glass, foamed resin, or sintered granules. is sandwiched and fixed in the middle of each, and seawater is supplied from one end of the hollow shaft through a rotary joint, and is press-fitted into the disc through a small hole drilled around the hollow shaft. The other end of the evaporator is connected to a motor with a speed reducer to slowly rotate it, and the bottom of the evaporator is filled with seawater to an appropriate level so that a part of the disc is immersed in the seawater. The method is characterized by being provided with an evaporator that supplies water from both the hollow shaft and the periphery of the disc, and circulates air to promote evaporation from the rough surface of the disc and prevent scale from forming. The present invention provides a seawater desalination device.

自然界における降雨現象は大部分が海水の淡水化に他な
らないが、その本質は空気中における蒸発と凝縮である
。したがって、これらの現象は大気圧下で行なわれる。
Rainfall phenomena in the natural world are mostly nothing but desalination of seawater, but their essence is evaporation and condensation in the air. Therefore, these phenomena take place under atmospheric pressure.

本発明は上述したよ5に、海洋温度差発’[に使用した
冷海水がなおかなりの低温であることに着目し海面の温
海水な9調用冷却塔ないし、それ九類似の充填塔、また
はさらに改良された蒸発装置に供給して蒸発器せるとと
もにその蒸気を海洋温度差発tIC使用した残りのまた
は場合によっては特に汲み揚げた冷海水によって冷却さ
れるエヤーフィンクーラーで凝縮させることにより、殆
ど無料のエネルギーで淡水を安価に製造できる海水の淡
水化装置である。
As mentioned above, the present invention focuses on the fact that the cold seawater used for ocean temperature difference is still at a considerably low temperature, and uses a cooling tower for cooling the warm seawater at the sea surface, or a similar packed tower, or Furthermore, most of the This is a seawater desalination device that can produce fresh water at low cost using free energy.

次に、本発明装置を図面を参照して詳述する。Next, the apparatus of the present invention will be explained in detail with reference to the drawings.

第1図は本発明装置の一笑施例の縦断面図を示すもので
、lは蒸発器、2は凝縮器、3は送風機である。蒸発器
1において、101は海水の入口、102はスプリンク
ラ−103はクーリングタワーの内部に相当する一種の
充填塔である。なるべく少ない圧力損失でなるべく大き
な蒸発面積を与えるように構成された公知の多くのもの
があるが、その中でなるべく飛沫同伴の少ないものを選
択すべきであり、出来れば飛沫同伴の全くないものが望
ましいのであつτ、そのような−例を追って説明する。
FIG. 1 shows a longitudinal cross-sectional view of an embodiment of the apparatus of the present invention, in which 1 is an evaporator, 2 is a condenser, and 3 is a blower. In the evaporator 1, 101 is a seawater inlet, 102 is a sprinkler, and 103 is a kind of packed tower corresponding to the inside of a cooling tower. There are many known devices designed to provide as large an evaporation area as possible with as little pressure loss as possible, but among these, one should choose one that entrains as few droplets as possible, and if possible, one that does not entrain droplets at all. Since it is desirable and τ, such an example will be explained below.

104は空気の入口でありこの空気は充填塔103にお
いてスブリ/クラ−から落下する海水と接触し水分で飽
和てれる、iosはデミスタ−106はブローダウン排
出口である。
Reference numeral 104 is an air inlet, and this air comes into contact with seawater falling from the sublime/clarifier in the packed tower 103 and becomes saturated with moisture. ios is a demister 106 is a blowdown outlet.

凝縮器2において、201は凝縮を起させるフィン群で
あって、それらは管群202によって貫かれτ居り、管
群202内な前記の冷海水が流れ蒸発器lから送風機3
&Cよって送り込まれた湿った空気な冷却し、水分の凝
縮な起させる。
In the condenser 2, 201 is a group of fins that cause condensation, and these are penetrated by a group of tubes 202, and the cold seawater in the group of tubes 202 flows from the evaporator l to the blower 3.
The moist air introduced by &C cools and causes moisture to condense.

凝縮した水分は凝縮器2の底に溜り出口203から淡水
として取り出される。204は空気の出口である。この
を気は冷海水に冷やされて非常に冷いので、冷房などに
一部利用比来るが、この冷風の量は美大であり、むしろ
その付近−帯を涼しくするのに有効であると考えられ、
乾燥した熱い砂漠の気候なその付近に限られるとしても
改善し、砂漠緑化の一部にもなると考えられる。
The condensed water accumulates at the bottom of the condenser 2 and is taken out from the outlet 203 as fresh water. 204 is an air outlet. This air is cooled by the cold seawater and is very cold, so it is sometimes used for air conditioning, but the amount of cold air is large, and it is said to be effective in cooling the surrounding area. considered,
Even if it is limited to areas with dry, hot desert climates, it is thought that it will improve and become part of desert greening.

第2図は本発明の異なる5N施例の縦断面図で飛沫同伴
の恐れのない蒸発装置の長平方向の断fを示し、第3図
はそれに直角な方向の断面な示す。
FIG. 2 is a longitudinal cross-sectional view of a different 5N embodiment of the present invention, showing a cross-section f in the longitudinal direction of an evaporator without the risk of entrainment of droplets, and FIG. 3 shows a cross-section in a direction perpendicular thereto.

第2図の蒸発器lにおいて、海水の入口は101Aとl
0IBの二つに分れている。蒸発器1の本体は水平な円
筒から成り、その両端の鏡板には密封式軸受107があ
り、それによって中窒の軸108を支えている。中窒軸
108の左端は密封式接手109を介して海水の一つの
入口101Aと連結されて居り、右端は減速器付モータ
ー1010に接続され、これによつτゆつ(りと回転さ
れる。
In the evaporator l in Figure 2, the seawater inlets are 101A and l.
It is divided into two parts: 0IB. The main body of the evaporator 1 consists of a horizontal cylinder, and sealed bearings 107 are provided on the head plates at both ends, thereby supporting a shaft 108 of the inner nitrogen. The left end of the inner shaft 108 is connected to one seawater inlet 101A via a sealed joint 109, and the right end is connected to a motor 1010 with a speed reducer, which rotates the shaft at a slow rate of τ. .

軸10gには連続気泡の発泡ガラス、発泡樹脂。The 10g shaft is made of open-cell foamed glass and foamed resin.

v8結粒体のような多孔質素材から成る円板1011多
数がパツキン1012&はさんで軸108と同軸に固定
され、軸108と共に回転するようになっている。この
円板1011は一部分蒸発器1本体の底部に一定のレベ
ルを保って溜っている海水に漬かって居り海水をその毛
細管現象で吸い上げ乍ら回転する。蒸発器1本体の底部
には前述の海水入口101Bから新しい海水が補給され
る一万一部は出口106から少しずつ排出され蒸発によ
る濃縮ケ防ぐ。これはボイラーのブローダウンに相当す
る。入口101Aから軸108に入った海水は軸108
の周囲にあけられた孔1013から円[1011に押し
込まれ円板10110表面に滲み出し周囲に広がり蒸発
する。円板1011の中心付近は新しい海水によって常
に洗われているのでスケールは付かない。円板1011
の周辺はその回転によって蒸発器lの底部の海水に漬か
り順次洗われるのでやはりスケールの付着は防止される
。104.1014は空気の入口と出口である。
A large number of disks 1011 made of a porous material such as V8 granules are fixed coaxially with the shaft 108 through gaskets 1012 and rotated together with the shaft 108. This disk 1011 is partially immersed in the seawater that has accumulated at a constant level at the bottom of the evaporator 1 body, and rotates while sucking up the seawater by its capillary action. New seawater is replenished to the bottom of the evaporator 1 body from the seawater inlet 101B, and some of it is gradually discharged from the outlet 106 to prevent concentration due to evaporation. This corresponds to boiler blowdown. Seawater entering the shaft 108 from the inlet 101A flows through the shaft 108.
It is pushed into the circle [1011] through a hole 1013 made around the disk, oozes out onto the surface of the disk 10110, spreads around it, and evaporates. The area around the center of the disk 1011 is constantly washed with fresh seawater, so no scale is attached. Disk 1011
As the area around the evaporator 1 is rotated, it is immersed in the seawater at the bottom of the evaporator 1 and washed successively, so that scale adhesion is also prevented. 104.1014 are air inlets and outlets.

この構造は既存のクーリングタワーよりは高価であるが
、その代り飛沫の同拌は起らず、デミスーー105を省
略することが出来、ブロワ−の圧損が小さくなる上に、
非常に純度の高い淡水が得られる。なお蒸発器lの本体
は当然円筒形にして円板面以外での空気のバイパスな防
ぎ、且つ円板間の隙間は適当に小さくして、空気の流速
を高め、蒸発を促進する。また、本発明装置においては
、蒸発器lにおいて発生した酸素、炭酸ガス等の不凝縮
ガスも水蒸気と−しよに運ばれて凝縮の除に再び吸収さ
れるので飲用としての適性の上からも好ましいものであ
る。
Although this structure is more expensive than existing cooling towers, it does not cause droplet agitation, the Demi-105 can be omitted, the pressure loss of the blower is reduced, and
Very pure fresh water can be obtained. The main body of the evaporator I is naturally cylindrical to prevent air from bypassing other than the disk surface, and the gap between the disks is appropriately small to increase the air flow rate and promote evaporation. In addition, in the device of the present invention, non-condensable gases such as oxygen and carbon dioxide generated in the evaporator 1 are also transported along with the water vapor and are absorbed again after condensation, making it suitable for drinking. This is preferable.

本発明装置は海洋温度差発電に使用された冷海水を再利
用することを主眼としているが、冷海水が容易に安価に
得られる場合は@抜海から動力を用いて汲み上げてもよ
いことは勿論である。たとえば、海洋温度発電以外の風
力とか波力あるいは全く別の安価なりリーンエネルギー
が利用可能となった場合はそのエネルギーで直接海水を
汲み揚げてもよいことは勿論である。
The main purpose of the device of the present invention is to reuse the cold seawater used for ocean temperature difference power generation, but if cold seawater can be obtained easily and inexpensively, it is of course possible to pump it up from @Nakkai using power. It is. For example, if wind power, wave power, or another type of cheap or lean energy other than ocean thermal power generation becomes available, it is of course possible to use that energy to directly pump up seawater.

(発明の効果) 本発明は上記の41m成をとることによって次の効(1
)低コストで且つ高純度の淡水を得ることが出来る。
(Effects of the Invention) The present invention has the following effects (1) by adopting the above 41m configuration.
) High purity freshwater can be obtained at low cost.

(2)得られた淡水中には一旦海水より蒸発した酸素、
炭酸ガス等が再吸収されているので飲用水としての適性
上好ましい。
(2) The obtained fresh water contains oxygen that has evaporated from seawater,
Since carbon dioxide gas etc. are reabsorbed, this water is suitable for drinking water.

(3)  大量の冷風が得られる。(3) A large amount of cold air can be obtained.

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

第1図は本発明装置の一実施例の縦断面図、第2図は本
発明装置の異なる実施例の縦断面図、第3図は第2図の
横断面図である。 図において 1−一一一蒸発器 2−一一一凝縮器 3−一一一送風機 101、101人、 l0IB−−−一海水の入口10
2−−−−スプリンクラ− 103−−−一充填塔 104−−−一空気の入口 105−−−−デミスタ− 106−−−−ブローダウン排出口 202−−一− 密封式軸受 中空軸 密封式接手 フィン群 管群 淡水溝り出口 空気の出口 減速器付モーター 円   板 パツキン 孔 空気の出口
1 is a longitudinal cross-sectional view of one embodiment of the apparatus of the present invention, FIG. 2 is a longitudinal cross-sectional view of a different embodiment of the apparatus of the present invention, and FIG. 3 is a cross-sectional view of FIG. 2. In the figure: 1-111 evaporator 2-111 condenser 3-111 blower 101, 101 people, l0IB----1 seawater inlet 10
2---Sprinkler 103---1 Packed column 104---1 Air inlet 105---Demister 106---Blowdown outlet 202---1- Sealed bearing hollow shaft sealed type Joint fin group Fresh water groove outlet Air outlet Motor circle with reducer Plate seal hole Air outlet

Claims (2)

【特許請求の範囲】[Claims] (1)海面の温海水を空調用冷却塔ないしそれに類似の
充填塔又はその他気水接触装置に供給し、大気圧下で空
気と接触させて蒸発させ、この空気を海洋温度差発電に
使用された冷たい排海水または場合によつては特に汲み
揚げた冷海水によりエヤーフィンクーラーを介して凝縮
させることにより蒸発器で分離された炭酸ガス、酸素等
を再び吸収させ、安価で良質な飲用水を得ることを特徴
とする海水の淡水化装置。
(1) Warm seawater at the sea surface is supplied to an air conditioning cooling tower, similar packed tower, or other air-water contact device, and is brought into contact with air under atmospheric pressure to evaporate, and this air is used for ocean thermal power generation. The carbon dioxide, oxygen, etc. separated in the evaporator are reabsorbed by condensing the cooled discharged seawater or, in some cases, pumped-up cold seawater through an air fin cooler, thereby producing inexpensive, high-quality drinking water. A seawater desalination device characterized by:
(2)円筒形蒸発器の両端の鏡板を貫く1本の中空軸に
連続気泡の発泡ガラス、発泡樹脂、焼結粒体のごとき粗
面を有する多孔質素材から成る円板多数をパッキンをそ
れぞれの中間に挾んで固定し、該中空軸の一端からは回
転接手を介して海水を供給し、該中空軸の周囲に明けら
れた小孔から前記円板に圧入して該円板の表面に滲み出
させ、またその他端は減速機付モーターに連結されてゆ
るやかに回転させ、且つ該蒸発器の底部には適当レベル
に海水を溜めて前記円板の一部が漬かるようにして海水
を該中空軸と該円板の周辺の両方から供給するとともに
空気を流通させて該円板の粗面からの蒸発を促進させ且
つスケールが付かぬようにした蒸発装置を設けたことを
特徴とする海水の淡水化装置。
(2) A large number of disks made of porous materials with rough surfaces such as open-cell foamed glass, foamed resin, and sintered granules are packed on one hollow shaft that passes through the head plates at both ends of the cylindrical evaporator. Seawater is supplied from one end of the hollow shaft via a rotary joint, and is press-fitted into the disc through a small hole drilled around the hollow shaft to coat the surface of the disc. The other end of the evaporator is connected to a motor with a speed reducer to slowly rotate it, and seawater is collected at an appropriate level at the bottom of the evaporator so that a part of the disk is immersed in the seawater. Seawater is provided with an evaporator that supplies air from both the hollow shaft and the periphery of the disk, circulates air to promote evaporation from the rough surface of the disk, and prevents scale from forming. desalination equipment.
JP1010774A 1989-01-19 1989-01-19 Device for desalting sea water Pending JPH02191586A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1010774A JPH02191586A (en) 1989-01-19 1989-01-19 Device for desalting sea water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1010774A JPH02191586A (en) 1989-01-19 1989-01-19 Device for desalting sea water

Publications (1)

Publication Number Publication Date
JPH02191586A true JPH02191586A (en) 1990-07-27

Family

ID=11759678

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1010774A Pending JPH02191586A (en) 1989-01-19 1989-01-19 Device for desalting sea water

Country Status (1)

Country Link
JP (1) JPH02191586A (en)

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