JPH11216459A - Seawater desalting device - Google Patents

Seawater desalting device

Info

Publication number
JPH11216459A
JPH11216459A JP10017490A JP1749098A JPH11216459A JP H11216459 A JPH11216459 A JP H11216459A JP 10017490 A JP10017490 A JP 10017490A JP 1749098 A JP1749098 A JP 1749098A JP H11216459 A JPH11216459 A JP H11216459A
Authority
JP
Japan
Prior art keywords
seawater
reduced
discharge
pressure
evaporator
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
JP10017490A
Other languages
Japanese (ja)
Inventor
Makoto Tanabe
允 田辺
Shinichiro Tochio
信一郎 栃尾
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.)
Toshiba Corp
Nishishiba Electric Co Ltd
Original Assignee
Toshiba Corp
Nishishiba Electric Co Ltd
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 Toshiba Corp, Nishishiba Electric Co Ltd filed Critical Toshiba Corp
Priority to JP10017490A priority Critical patent/JPH11216459A/en
Publication of JPH11216459A publication Critical patent/JPH11216459A/en
Pending legal-status Critical Current

Links

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

Landscapes

  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a highly efficient seawater desalting device by which the quality of the fresh water obtained is improved, the power consumption is reduced with respect to the amt. of the generated water, and energy is saved. SOLUTION: This device has the vacuum evaporator 2 having a seawater inlet 7 and a seawater outlet 10 and evaporating the introduced seawater under vacuum, a vacuum pump 28 for reducing ther pressure below the saturated vapor pressure of seawater, a condenser 19 for cooling and condensing the produced steam to produce fresh water, a means 3 for continuously supplying seawater to the evaporator 19 in excess of the amt. of the water evaporated, a means 4 for discharging the seawater from the evaporator 2 in less than the supply and a means 5 for adjusting the flow rate of the seawater supply means 3 and that of the seawater discharge means 4 and keeping the seawater level in the evaporator 2 constant.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、海水から淡水を得
る技術に関するものであり、特に減圧法により、工業用
水、飲料水および生活用水としての使用に供する淡水を
得る海水淡水化装置の改良に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a technique for obtaining freshwater from seawater, and more particularly to an improvement of a seawater desalination apparatus for obtaining freshwater for use as industrial water, drinking water and domestic water by a decompression method. Things.

【0002】[0002]

【従来の技術】従来、海水から淡水を得る海水淡水化技
術として、例えば逆浸透膜法が知られている。この逆浸
透膜(RO膜)法では、海水を高圧下で高分子膜である
逆浸透膜に通過させ、高圧側に濃縮された塩類溶液の海
水を残し、低圧側に脱塩水である淡水を分離して淡水を
造水する。
2. Description of the Related Art Conventionally, for example, a reverse osmosis membrane method is known as a seawater desalination technique for obtaining freshwater from seawater. In this reverse osmosis membrane (RO membrane) method, seawater is passed under high pressure through a reverse osmosis membrane, which is a polymer membrane, leaving seawater of a concentrated salt solution on the high pressure side, and fresh water as desalinated water on the low pressure side. Separate to produce fresh water.

【0003】しかし、この逆浸透膜法では、海水を高圧
ポンプにより加圧し逆浸透膜によりろ過するため、逆浸
透膜に不純物が詰まり易く、逆浸透膜の逆洗を行う必要
がある。また運転停止時にバクテリアが発生し、逆浸透
膜に穴があくこともあり、運転および維持管理が難しい
という問題があった。
However, in this reverse osmosis membrane method, since seawater is pressurized by a high-pressure pump and filtered by the reverse osmosis membrane, impurities are easily clogged in the reverse osmosis membrane, and it is necessary to perform reverse washing of the reverse osmosis membrane. In addition, when the operation is stopped, bacteria are generated, and a hole is formed in the reverse osmosis membrane, so that there is a problem that operation and maintenance are difficult.

【0004】これに対し、海水を減圧蒸発器に入れ真空
ポンプで減圧することにより海水から水蒸気を取り出
し、取り出した水蒸気を凝縮器で冷却して凝縮させて淡
水を得る減圧法が知られている。この減圧法では逆洗等
の面倒がなく、またバクテリア発生等の問題も生じな
い。
[0004] On the other hand, there is known a decompression method in which seawater is put into a reduced-pressure evaporator and depressurized by a vacuum pump to take out steam from the seawater, and the taken-out steam is cooled and condensed by a condenser to obtain fresh water. . In this decompression method, there is no trouble such as back washing and no problem such as generation of bacteria.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、上記の
減圧法を採用した従来の海水淡水化装置においては、減
圧蒸発器内への海水供給のみを行いながら蒸発作用を行
わせているため、減圧容器内に貯留されている海水が蒸
発潜熱により次第に冷却され、これにより飽和水蒸気圧
も次第に低下し、真空ポンプの負荷が増える傾向があっ
た。そこで、これを防ぐために、電気ヒータなどを設置
して減圧蒸発器内を加温する等の対策がとられている
が、それだけ電力を大量に消費することになり、造水効
率が悪いという問題があった。
However, in the conventional seawater desalination apparatus employing the above-mentioned decompression method, the evaporating action is performed while only supplying seawater into the decompression evaporator. The seawater stored therein was gradually cooled by the latent heat of evaporation, whereby the saturated steam pressure also gradually decreased, and the load on the vacuum pump tended to increase. To prevent this, measures such as installing an electric heater to heat the inside of the decompression evaporator have been taken. However, a large amount of power is consumed, resulting in poor water production efficiency. was there.

【0006】また、通常では減圧容器内への海水供給手
段として給水ポンプを設置しており、このポンプ駆動用
としても電力が消費されることから、このことも造水効
率低下の原因となっている。
[0006] Usually, a water supply pump is installed as a means for supplying seawater to the decompression vessel, and power is also consumed for driving the pump. This also causes a reduction in fresh water production efficiency. I have.

【0007】さらに、従来の構成では減圧蒸発器内での
海水の突沸によって塩水が凝縮器側に流入する等の不具
合を生じることもあった。
[0007] Further, in the conventional configuration, there is also a problem that salt water flows into the condenser side due to bumping of seawater in the reduced-pressure evaporator.

【0008】本発明はこのような問題を解決するために
なされたものであり、減圧法を用いる海水淡水化装置に
おいて、消費電力を節約して省エネルギー化および造水
効率の向上を図り、かつ塩水の凝縮器への流入を防止し
て淡水の水質向上を図ることを目的とする。
The present invention has been made in order to solve such a problem. In a seawater desalination apparatus using a decompression method, power consumption is saved to save energy and improve fresh water production efficiency, and salt water is used. The purpose of the present invention is to improve the quality of fresh water by preventing the flow of water into the condenser.

【0009】[0009]

【課題を解決するための手段】請求項1記載の発明は、
密閉タンク形で、その底部側に海水導入口および海水排
出口を有し、導入した海水を減圧により蒸発させる減圧
蒸発器と、この減圧蒸発器の内部を海水の飽和蒸気圧以
下に減圧する真空ポンプと、前記減圧蒸発器で得られた
水蒸気を冷却凝縮させて淡水を得る凝縮器と、前記減圧
蒸発器に前記海水導入口を介して蒸発水量以上の海水を
連続的に供給する海水供給手段と、前記減圧蒸発器から
前記海水排出口を介して供給量以下の海水を連続的に排
出する海水排出手段と、これら海水供給手段および海水
排出手段の海水流量を調節することにより、前記減圧蒸
発器内の海水の液面を一定に制御する制御手段とを有す
ることを特徴とする。
According to the first aspect of the present invention,
A closed tank type, having a seawater inlet and a seawater outlet at the bottom side, and a reduced-pressure evaporator for evaporating the introduced seawater by reducing pressure, and a vacuum for reducing the pressure inside the reduced-pressure evaporator to below the saturated vapor pressure of seawater. A pump, a condenser for cooling and condensing water vapor obtained by the reduced-pressure evaporator to obtain fresh water, and seawater supply means for continuously supplying seawater having an amount equal to or greater than the amount of evaporated water to the reduced-pressure evaporator via the seawater inlet. A seawater discharging means for continuously discharging seawater of a supply amount or less from the reduced-pressure evaporator through the seawater discharge port, and adjusting a seawater flow rate of the seawater supplying means and the seawater discharging means to reduce the reduced-pressure evaporation. Control means for controlling the level of seawater in the vessel to be constant.

【0010】本発明によれば、海水供給手段と海水排出
手段とを設置し、蒸発水量と比べてより多く海水を供給
して海水量を調節することにより、蒸発潜熱による減圧
蒸発器内の海水の温度低下を防ぎ、比較的低い真空度で
水蒸気を取り出すことが可能である。また真空度が低い
ことから真空ポンプの負荷が減り、真空ポンプをより小
型の物にすることができ、消費電力を節約することが可
能である。
According to the present invention, the seawater supply means and the seawater discharge means are provided, and the amount of the seawater is adjusted by supplying more seawater than the amount of the evaporative water. , And water vapor can be taken out at a relatively low degree of vacuum. In addition, since the degree of vacuum is low, the load on the vacuum pump is reduced, the vacuum pump can be made smaller, and power consumption can be reduced.

【0011】さらに本発明によれば、減圧蒸発器内にお
ける海水の液位を検出して一定に制御する制御手段を設
けたことにより、減圧蒸発器内の蒸気が占める体積を一
定に保つことが可能となり、真空度の変化を防止して運
転の安定化が図れる。
Further, according to the present invention, by providing a control means for detecting and controlling the level of seawater in the reduced-pressure evaporator, the volume occupied by the steam in the reduced-pressure evaporator can be kept constant. It is possible to prevent a change in the degree of vacuum and stabilize the operation.

【0012】請求項2記載の発明は、請求項1記載の海
水淡水化装置において、海水供給手段は、一端が海水中
に挿入され他端が減圧蒸発器の底部に接続された海水供
給管と、この海水供給管に設けられ、海水の供給量を調
節する海水供給量調節バルブと、前記減圧蒸発器内を大
気圧以下に減圧し、その圧力差により前記減圧蒸発器内
に海水を吸引する減圧機構とを有することを特徴とす
る。
According to a second aspect of the present invention, in the seawater desalination apparatus according to the first aspect, the seawater supply means includes a seawater supply pipe having one end inserted into the seawater and the other end connected to the bottom of the vacuum evaporator. A seawater supply control valve provided in the seawater supply pipe to control the supply amount of seawater, and the pressure in the reduced-pressure evaporator is reduced to the atmospheric pressure or less, and the pressure difference suctions seawater into the reduced-pressure evaporator. And a pressure reducing mechanism.

【0013】本発明によれば、減圧蒸発器内に海水を供
給するために、減圧蒸発器内に海水供給管を接続して、
この海水供給管の他端を海面下に挿入し、減圧蒸発器内
を大気圧以下に減圧することにより、減圧蒸発器内の負
圧と大気圧との圧力差を利用し海水供給管から減圧蒸発
器内に海水を吸引するものである。
According to the present invention, in order to supply seawater into the reduced-pressure evaporator, a seawater supply pipe is connected in the reduced-pressure evaporator,
The other end of this seawater supply pipe is inserted below the sea surface, and the pressure inside the vacuum evaporator is reduced to the atmospheric pressure or less, so that the pressure difference between the negative pressure in the vacuum evaporator and the atmospheric pressure is used to reduce the pressure from the seawater supply pipe. It sucks seawater into the evaporator.

【0014】請求項3記載の発明は、請求項2記載の海
水吸引用の減圧機構は、請求項1記載の海水蒸発用の真
空ポンプであることを特徴とする。
The invention according to claim 3 is characterized in that the pressure reducing mechanism for suctioning seawater according to claim 2 is the vacuum pump for evaporating seawater according to claim 1.

【0015】本発明によれば、海水を吸引するための真
空ポンプと減圧蒸発器内を減圧するための減圧機構とを
共有することにより、減圧蒸発器内に海水を供給するポ
ンプを省略でき、消費電力を節約することが可能であ
る。
According to the present invention, by sharing a vacuum pump for sucking seawater and a decompression mechanism for depressurizing the inside of the reduced-pressure evaporator, a pump for supplying seawater into the reduced-pressure evaporator can be omitted. It is possible to save power consumption.

【0016】請求項4記載の発明は、請求項1から3ま
でのいずれかに記載の海水淡水化装置において、海水排
出手段は、一端が減圧蒸発器の海水排出口に接続され他
端が海面側に配置された海水排出管と、この海水排出管
に設けられた海水排出ポンプと、この海水排出ポンプの
吐出側に設けられ海水の排出量を調節する海水排出量調
節バルブとを有することを特徴とする。
According to a fourth aspect of the present invention, in the seawater desalination apparatus according to any one of the first to third aspects, the seawater discharge means has one end connected to the seawater discharge port of the vacuum evaporator and the other end connected to the sea surface. Side, a seawater discharge pipe provided on the side, a seawater discharge pump provided on the seawater discharge pipe, and a seawater discharge control valve provided on the discharge side of the seawater discharge pump for controlling the discharge of seawater. Features.

【0017】請求項5記載の発明は、請求項1から4ま
でのいずれかに記載の海水淡水化装置において、海水排
出手段から排出される海水の一部をとり込み、減圧蒸発
器内で散水を連続的に行わせる海水散水手段を有するこ
とを特徴とする。
According to a fifth aspect of the present invention, in the seawater desalination apparatus according to any one of the first to fourth aspects, a part of the seawater discharged from the seawater discharging means is taken in and the water is sprayed in the reduced-pressure evaporator. Characterized by having seawater sprinkling means for continuously performing water spraying.

【0018】本発明によれば、海水排出手段の一部を分
岐させて減圧蒸発器内に海水を散水する海水散水手段を
備えたことにより、海水排出手段から独立して海水散水
手段を設置する必要がなくなる。
According to the present invention, the seawater sprinkling means is provided independently of the seawater discharging means by providing the seawater sprinkling means for branching a part of the seawater discharging means to sprinkle the seawater in the reduced-pressure evaporator. Eliminates the need.

【0019】請求項6記載の発明は、請求項5記載の海
水淡水化装置において、海水散水手段は、一端が前記海
水排出管の海水排出ポンプの吐出側に分岐して接続され
他端が前記減圧蒸発器内の上部に挿入された海水散水管
と、この減圧蒸発器内においてその端部に設けられた散
水ノズルと、前記海水散水管に設けられ海水の散水量を
調節する海水散水量調節バルブとを有することを特徴と
する。
According to a sixth aspect of the present invention, in the seawater desalination apparatus according to the fifth aspect, the seawater sprinkling means has one end branched and connected to the discharge side of the seawater discharge pump of the seawater discharge pipe, and the other end connected to the seawater discharge pipe. A seawater sprinkling pipe inserted into the upper part of the reduced-pressure evaporator, a sprinkling nozzle provided at an end of the reduced-pressure evaporator, and a seawater sprinkling amount control provided in the seawater sprinkling pipe to adjust the sprinkling amount of seawater. And a valve.

【0020】本発明によれば、海水排出手段の一部を分
岐させ、減圧蒸発器の上部位置から海水散水手段である
散水ノズルによりシャワー状の水滴として散水すること
により、海水の蒸発面積を増やし蒸発効率を向上させる
ことができる。また、減圧蒸発器内における海水の突沸
を防止して塩水の凝縮器側への流入を防ぎ、得られる淡
水の水質を向上させることができる。
According to the present invention, a part of the seawater discharging means is branched, and the water is sprayed as shower-like water droplets from the upper position of the reduced-pressure evaporator by the watering nozzle which is the seawater spraying means, thereby increasing the evaporation area of the seawater. Evaporation efficiency can be improved. Also, bumping of seawater in the reduced-pressure evaporator can be prevented to prevent the salt water from flowing into the condenser side, and the quality of fresh water obtained can be improved.

【0021】また本発明によれば、蒸発効率の上昇によ
り真空度が低下し、真空ポンプの負荷が減ることにより
消費電力を節約できる。
Further, according to the present invention, the degree of vacuum is reduced by increasing the evaporation efficiency, and the power consumption can be reduced by reducing the load on the vacuum pump.

【0022】請求項7記載の発明は、請求項2、4およ
び6記載の海水淡水化装置において、制御手段は、減圧
蒸発器内の海水の液位を検出する液位検出計と、この液
位検出計の検出値に基づいて海水供給量調節バルブ、海
水排出量調節バルブ、海水排出ポンプおよび海水散水量
調節バルブの少くとも1以上を制御する制御器とを有す
ることを特徴とする。
According to a seventh aspect of the present invention, in the seawater desalination apparatus according to the second, fourth and sixth aspects, the control means comprises: a liquid level detector for detecting the level of seawater in the reduced-pressure evaporator; A controller controls at least one of a seawater supply amount adjustment valve, a seawater discharge amount adjustment valve, a seawater discharge pump, and a seawater sprinkling amount adjustment valve based on a detection value of the position detector.

【0023】[0023]

【発明の実施の形態】以下において、本発明の実施形態
を図1を参照して説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to FIG.

【0024】図1は、本実施形態による海水淡水化装置
を示す図であり、この海水淡水化装置は、海浜に設置さ
れるものである。
FIG. 1 is a view showing a seawater desalination apparatus according to the present embodiment, and this seawater desalination apparatus is installed on a beach.

【0025】図1に示すように、海水淡水化装置1に
は、海水を減圧するための容器である減圧蒸発器2が設
置されている。減圧蒸発器2は密閉タンク形で、この減
圧蒸発器2には減圧蒸発器2に海水を供給する海水供給
手段3と、減圧蒸発器2から海水を排出する海水排出手
段4とが設けられている。そして、これら海水供給手段
3および海水排出手段4には、海水量を調節する制御手
段5が設けられ、減圧蒸発器2内における海水の液位を
一定に制御している。
As shown in FIG. 1, the seawater desalination apparatus 1 is provided with a decompression evaporator 2 which is a container for decompressing seawater. The reduced-pressure evaporator 2 is a closed tank type. The reduced-pressure evaporator 2 is provided with seawater supply means 3 for supplying seawater to the reduced-pressure evaporator 2 and seawater discharging means 4 for discharging seawater from the reduced-pressure evaporator 2. I have. The seawater supply means 3 and the seawater discharge means 4 are provided with a control means 5 for adjusting the amount of seawater, and control the level of seawater in the reduced-pressure evaporator 2 to be constant.

【0026】詳述すると、この減圧蒸発器2には、海水
を減圧蒸発器2内に供給する海水供給手段3としての海
水供給管6が、一端が減圧蒸発器2底部に設けられた海
水導入口7を介して接続され、他端が海面側に配置され
ており、減圧蒸発器2内に蒸発水量以上の海水を連続的
に供給する構成となっている。そして、この海水供給管
6には、海水量を調節する海水供給量調節バルブ8が設
けられている。
More specifically, the reduced-pressure evaporator 2 includes a seawater supply pipe 6 serving as seawater supply means 3 for supplying seawater into the reduced-pressure evaporator 2, and a seawater introduction pipe having one end provided at the bottom of the reduced-pressure evaporator 2. The evaporator 2 is connected via the port 7, and the other end is disposed on the sea surface side. The seawater supply pipe 6 is provided with a seawater supply amount adjustment valve 8 for adjusting the amount of seawater.

【0027】また減圧蒸発器2には、減圧蒸発器2内の
海水を排出する海水排出手段4としての海水排出管9
が、一端が減圧蒸発器2側部に設けられた海水排出口1
0を介して接続され、他端が海面側に配置されており、
減圧蒸発器2内の海水を排出できるようになっている。
この海水排出管9には、海水排出ポンプ11が設置され
ており、この海水排出ポンプ11の吐出側には海水排出
量調節バルブ12が接続されている。一方、この海水排
出ポンプ10の吐出側の海水排出管9は分岐されて海水
散水手段13としての海水散水管14が接続されてい
る。この海水散水管14の他端は減圧蒸発器2内の上部
に挿入されており、この減圧蒸発器2内においてその端
部には、減圧蒸発器2内に海水を散水する散水ノズル1
5が設けられている。また、海水散水管14には、海水
の散水量を調節する海水散水量調節バルブ16が設けら
れている。
The reduced-pressure evaporator 2 has a seawater discharge pipe 9 as a seawater discharge means 4 for discharging seawater in the reduced-pressure evaporator 2.
Is a seawater outlet 1 having one end provided on the side of the vacuum evaporator 2.
0, and the other end is located on the sea surface side,
The seawater in the reduced-pressure evaporator 2 can be discharged.
The seawater discharge pipe 9 is provided with a seawater discharge pump 11, and the discharge side of the seawater discharge pump 11 is connected to a seawater discharge control valve 12. On the other hand, the seawater discharge pipe 9 on the discharge side of the seawater discharge pump 10 is branched and connected to a seawater sprinkling pipe 14 as seawater sprinkling means 13. The other end of the seawater sprinkling pipe 14 is inserted into the upper part of the reduced-pressure evaporator 2. In the reduced-pressure evaporator 2, an end thereof is provided with a watering nozzle 1 for spraying seawater into the reduced-pressure evaporator 2.
5 are provided. The seawater sprinkling pipe 14 is provided with a seawater sprinkling amount control valve 16 for adjusting the amount of seawater sprinkling.

【0028】減圧蒸発器2内には、制御手段5である海
水の液位検出する液位検出計17が設置されている。こ
の液位検出計17は、制御器18に接続されており、こ
の液位検出計17で得られた信号を制御器18に送出す
るようになっている。そしてこの制御器18は、海水供
給手段3としての海水供給量調節バルブ8、海水排出手
段4としての海水排出量調節バルブ12および海水散水
手段13としての海水排出ポンプ11および海水散水量
調節バルブ16に各々接続されており、液位検出計17
からの信号により各バルブの開閉およびポンプの起動・
停止を行うことにより減圧蒸発器2内の海水量を調節し
ている。
In the reduced-pressure evaporator 2, a liquid level detector 17 for detecting the liquid level of seawater, which is the control means 5, is provided. The liquid level detector 17 is connected to a controller 18, and sends a signal obtained by the liquid level detector 17 to the controller 18. The controller 18 includes a seawater supply control valve 8 as the seawater supply means 3, a seawater discharge control valve 12 as the seawater discharge means 4, and a seawater discharge pump 11 and a seawater spray control valve 16 as the seawater sprinkler 13. And the liquid level detector 17
Signal to open and close each valve and start pump
By stopping, the amount of seawater in the reduced-pressure evaporator 2 is adjusted.

【0029】また減圧蒸発器2には、発生した水蒸気を
凝縮器19に導入するための水蒸気流路20が接続され
ている。そして、凝縮器19内に導入された水蒸気は、
冷凍機22から冷媒供給管21を介して供給される低温
の冷媒により凝縮して液体化(淡水化)する。一方、水
蒸気と熱交換して温度の上昇した冷媒は冷媒戻り管23
を通って再度冷凍機22に戻り冷却される。
The reduced-pressure evaporator 2 is connected to a steam flow path 20 for introducing the generated steam into the condenser 19. Then, the steam introduced into the condenser 19 is
The refrigerant is condensed and liquefied (desalinated) by a low-temperature refrigerant supplied from the refrigerator 22 via the refrigerant supply pipe 21. On the other hand, the refrigerant whose temperature has increased due to the heat exchange with the water vapor is supplied to the refrigerant return pipe 23.
, And returns to the refrigerator 22 to be cooled.

【0030】凝縮器19には、淡水供給量調節バルブ2
4を設けた淡水供給管25が接続されており、この淡水
供給管25を介して淡水タンク26に淡水が送水され
る。さらに、この凝縮器19には排気管27が接続され
ており、この排気管27に真空ポンプ28が接続され、
この真空ポンプ28の吐出側に排気が排出されるように
なっている。
The condenser 19 has a fresh water supply adjusting valve 2.
The fresh water supply pipe 25 provided with the fresh water supply pipe 4 is connected thereto, and fresh water is supplied to the fresh water tank 26 via the fresh water supply pipe 25. Further, an exhaust pipe 27 is connected to the condenser 19, and a vacuum pump 28 is connected to the exhaust pipe 27,
Exhaust gas is discharged to the discharge side of the vacuum pump 28.

【0031】本実施形態の海水淡水化装置1では、真空
ポンプ28を運転し減圧蒸発器2内を減圧し、制御器1
8からの信号により、海水供給量調節バルブ8が開か
れ、海水中に挿入されている海水供給管6から減圧蒸発
器2内に海水が供給される。このとき減圧蒸発器2内は
真空ポンプ28により減圧されるため、減圧蒸発器2内
と大気との圧力差により海水はポンプを使うことなく減
圧蒸発器2に流入する。
In the seawater desalination apparatus 1 of this embodiment, the vacuum pump 28 is operated to reduce the pressure in the decompression evaporator 2 and the controller 1
The seawater supply amount control valve 8 is opened by the signal from 8, and seawater is supplied into the reduced-pressure evaporator 2 from the seawater supply pipe 6 inserted into the seawater. At this time, since the pressure inside the reduced-pressure evaporator 2 is reduced by the vacuum pump 28, the seawater flows into the reduced-pressure evaporator 2 without using a pump due to the pressure difference between the inside of the reduced-pressure evaporator 2 and the atmosphere.

【0032】減圧蒸発器2内における海水の液位が適当
な高さになったことを液位検出計17により検出した
後、制御器18からの信号により海水排出ポンプ11を
起動し、海水排出量調節バルブ12を開いて海水を排出
する。また、制御器18からの信号により海水供給バル
ブ8を開き連続的に減圧蒸発器2内に海水を供給して、
減圧蒸発器2内の海水量を調節して海水の液面を一定に
保つ。
After the liquid level detector 17 detects that the level of the seawater in the reduced-pressure evaporator 2 has reached an appropriate level, the seawater discharge pump 11 is activated by a signal from the controller 18 to discharge the seawater. The amount adjusting valve 12 is opened to discharge seawater. Further, the seawater supply valve 8 is opened by a signal from the controller 18 to continuously supply seawater into the reduced-pressure evaporator 2,
The seawater level in the reduced-pressure evaporator 2 is adjusted to keep the seawater level constant.

【0033】減圧蒸発器2内が真空ポンプ28の運転に
より海水の飽和水蒸気圧よりも小さくなると、減圧蒸発
器2内の海水は沸騰し水蒸気を発生する。このとき、制
御器18は海水の液位を検出して、制御器18からの信
号が海水供給量調節バルブ8に送られてこの海水供給量
調節バルブ8が開かれ、減圧蒸発器2内に蒸発水量以上
の海水が供給される。また海水排出ポンプ11を起動
し、海水排出量調節バルブ8を開いて、海水を減圧蒸発
器2内から排出を行うことにより、減圧蒸発器2内にお
ける海水の液位が一定に保持される。またこの時、排出
される海水の一部は制御器18からの信号により海水散
水量調節バルブ16により流量調整された後、減圧蒸発
器2の上部から散水ノズル15によりシャワー状の水滴
として散水され、海水が蒸発される。
When the pressure inside the reduced-pressure evaporator 2 becomes lower than the saturated water vapor pressure of the seawater due to the operation of the vacuum pump 28, the seawater in the reduced-pressure evaporator 2 boils to generate steam. At this time, the controller 18 detects the level of the seawater, and a signal from the controller 18 is sent to the seawater supply control valve 8, which opens the seawater supply control valve 8, and enters the inside of the reduced-pressure evaporator 2. Seawater more than the amount of evaporated water is supplied. In addition, the seawater discharge pump 11 is started, the seawater discharge control valve 8 is opened, and the seawater is discharged from the reduced-pressure evaporator 2, so that the level of the seawater in the reduced-pressure evaporator 2 is kept constant. At this time, a part of the discharged seawater is adjusted in flow rate by a seawater spraying amount adjusting valve 16 according to a signal from the controller 18, and then is sprayed from the upper part of the reduced-pressure evaporator 2 as a shower-like water droplet by the spray nozzle 15. , The seawater is evaporated.

【0034】このようにして、減圧蒸発器2内で発生し
た水蒸気は水蒸気流路20を通り凝縮器19に導かれ
る。凝縮器19は冷却媒体により冷却されており、この
冷却媒体は冷凍機22から供給される。凝縮器19に導
かれた蒸気は凝縮器19により冷却凝縮され塩類などが
除去された淡水となり、淡水タンク26に送水され貯蔵
される。
Thus, the steam generated in the reduced-pressure evaporator 2 is guided to the condenser 19 through the steam channel 20. The condenser 19 is cooled by a cooling medium, and the cooling medium is supplied from a refrigerator 22. The steam guided to the condenser 19 is cooled and condensed by the condenser 19 to become fresh water from which salts and the like have been removed, and is sent to the fresh water tank 26 for storage.

【0035】以上に述べたように本実施形態によれば、
減圧蒸発器2に海水供給手段3と海水排出手段4とを設
置して、制御手段5により減圧蒸発器2内の海水の液位
を検知して、蒸発水量以上の海水を供給しながら排出す
ることで蒸発潜熱による減圧蒸発器2内の海水温度の低
下を防止し、水蒸気を発生させ易くして、真空ポンプ2
8の電力消費量を少なくすることができる。また、海水
供給量と海水排出量とを調節して、減圧蒸発器2内と大
気との圧力差を利用することにより海水供給用のポンプ
を省略でき省エネルギー化を図ることができる。
As described above, according to the present embodiment,
A seawater supply means 3 and a seawater discharge means 4 are installed in the reduced-pressure evaporator 2, and the control means 5 detects the liquid level of the seawater in the reduced-pressure evaporator 2 and discharges while supplying more than the amount of seawater. This prevents the seawater temperature in the decompression evaporator 2 from lowering due to the latent heat of evaporation, facilitates the generation of water vapor,
8 can be reduced. Further, by adjusting the supply amount of seawater and the discharge amount of seawater and utilizing the pressure difference between the inside of the reduced-pressure evaporator 2 and the atmosphere, a pump for supplying seawater can be omitted, and energy saving can be achieved.

【0036】さらに、減圧蒸発器2から排出する海水の
一部を減圧蒸発器2の上部に設置した散水ノズル15か
ら散水してシャワー状の水滴とすることで蒸発面積を増
やして蒸発し易くして海水の蒸発効率の向上を図るとと
もに、減圧蒸発器2内の突沸を防止し、塩水が水蒸気と
一緒に凝縮器19へ到達しないようにすることで淡水の
水質向上を図っている。
Further, a part of the seawater discharged from the reduced-pressure evaporator 2 is sprinkled from a sprinkling nozzle 15 provided on the upper part of the reduced-pressure evaporator 2 to form shower-like water droplets, thereby increasing the evaporation area and facilitating evaporation. In addition to improving the evaporation efficiency of seawater, bumping in the reduced-pressure evaporator 2 is prevented, and the quality of freshwater is improved by preventing salt water from reaching the condenser 19 together with water vapor.

【0037】従って本実施形態によれば、減圧蒸発器2
内の海水の温度低下を防止し、海水の液位を一定に制御
することで、海水を送水するための動力を不要にし、蒸
発効率を向上させるとともに、得られる淡水の水質を向
上させることができ、造水量に対する消費電力を少なく
して省エネルギー化を図り、運転および維持管理が簡単
な海水淡水化装置1を提供することができる。
Therefore, according to the present embodiment, the reduced pressure evaporator 2
By preventing the temperature of seawater from dropping inside and controlling the level of seawater to a constant level, it eliminates the need for power to send seawater, improving the evaporation efficiency and improving the quality of freshwater obtained. It is possible to provide the seawater desalination apparatus 1 that can reduce the power consumption with respect to the amount of fresh water, save energy, and operate and maintain easily.

【0038】[0038]

【発明の効果】以上述べたように、本発明によれば、得
られる淡水の水質を向上させるとともに、造水量に対す
る消費電力を節約して省エネルギー化を図り、造水効率
の良い海水淡水化装置を提供することができる。
As described above, according to the present invention, the quality of fresh water obtained is improved, the power consumption relative to the amount of fresh water is saved, energy is saved, and a seawater desalination apparatus with good fresh water efficiency is obtained. Can be provided.

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

【図1】本実施形態における海水淡水化装置を示す全体
構成図。
FIG. 1 is an overall configuration diagram showing a seawater desalination apparatus according to an embodiment.

【符号の説明】[Explanation of symbols]

1 海水淡水化装置 2 減圧蒸発器 3 海水供給手段 4 海水排出手段 5 制御手段 6 海水供給管 7 海水導入口 8 海水供給量調節バルブ 9 海水排出管 10 海水排出口 11 海水排出ポンプ 12 海水排出量調節バルブ 13 海水散水手段 14 海水散水管 15 散水ノズル 16 海水散水量調節バルブ 17 液位検出計 18 制御器 19 凝縮器 20 水蒸気流路 21 冷媒供給管 22 冷凍機 23 冷媒戻り管 24 淡水供給量調節バルブ 25 淡水供給管 26 淡水タンク 27 排気管 28 真空ポンプ DESCRIPTION OF SYMBOLS 1 Seawater desalination apparatus 2 Decompression evaporator 3 Seawater supply means 4 Seawater discharge means 5 Control means 6 Seawater supply pipe 7 Seawater inlet 8 Seawater supply control valve 9 Seawater discharge pipe 10 Seawater outlet 11 Seawater discharge pump 12 Seawater discharge Control valve 13 Seawater sprinkling means 14 Seawater sprinkling pipe 15 Sprinkling nozzle 16 Seawater sprinkling amount adjustment valve 17 Liquid level detector 18 Controller 19 Condenser 20 Steam flow path 21 Refrigerant supply pipe 22 Refrigerator 23 Refrigerant return pipe 24 Freshwater supply control Valve 25 Fresh water supply pipe 26 Fresh water tank 27 Exhaust pipe 28 Vacuum pump

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 密閉タンク形で、その底部側に海水導入
口および海水排出口を有し、導入した海水を減圧により
蒸発させる減圧蒸発器と、この減圧蒸発器の内部を海水
の飽和蒸気圧以下に減圧する真空ポンプと、前記減圧蒸
発器で得られた水蒸気を冷却凝縮させて淡水を得る凝縮
器と、前記減圧蒸発器に前記海水導入口を介して蒸発水
量以上の海水を連続的に供給する海水供給手段と、前記
減圧蒸発器から前記海水排出口を介して供給量以下の海
水を連続的に排出する海水排出手段と、これら海水供給
手段および海水排出手段の海水流量を調節することによ
り、前記減圧蒸発器内の海水の液面を一定に制御する制
御手段とを有することを特徴とする海水淡水化装置。
1. A closed tank type having a seawater inlet and a seawater outlet on the bottom side thereof, and a reduced-pressure evaporator for evaporating the introduced seawater under reduced pressure. A vacuum pump for reducing the pressure below, a condenser for cooling and condensing steam obtained by the reduced-pressure evaporator to obtain fresh water, and continuously supplying seawater having an amount of evaporated water or more to the reduced-pressure evaporator through the seawater inlet. Seawater supply means for supplying, seawater discharge means for continuously discharging seawater of a supply amount or less from the reduced-pressure evaporator through the seawater discharge port, and adjusting the seawater flow rate of these seawater supply means and seawater discharge means. And control means for controlling the level of seawater in the reduced-pressure evaporator to be constant.
【請求項2】 請求項1記載の海水淡水化装置におい
て、海水供給手段は、一端が海水中に挿入され他端が減
圧蒸発器の底部に接続された海水供給管と、この海水供
給管に設けられ、海水の供給量を調節する海水供給量調
節バルブと、前記減圧蒸発器内を大気圧以下に減圧し、
その圧力差により前記減圧蒸発器内に海水を吸引する減
圧機構とを有することを特徴とする海水淡水化装置。
2. The seawater desalination apparatus according to claim 1, wherein the seawater supply means includes a seawater supply pipe having one end inserted into the seawater and the other end connected to the bottom of the vacuum evaporator; Provided, a seawater supply control valve for controlling the supply of seawater, and the pressure in the reduced-pressure evaporator is reduced to an atmospheric pressure or less,
A seawater desalination apparatus having a pressure reducing mechanism for sucking seawater into the reduced pressure evaporator by the pressure difference.
【請求項3】 請求項2記載の海水吸引用の減圧機構
は、請求項1記載の海水蒸発用の真空ポンプであること
を特徴とする海水淡水化装置。
3. The seawater desalination apparatus according to claim 2, wherein the seawater suction pressure reducing mechanism is the seawater evaporation vacuum pump according to claim 1.
【請求項4】 請求項1から3までのいずれかに記載の
海水淡水化装置において、海水排出手段は、一端が減圧
蒸発器の海水排出口に接続され他端が海面側に配置され
た海水排出管と、この海水排出管に設けられた海水排出
ポンプと、この海水排出ポンプの吐出側に設けられ海水
の排出量を調節する海水排出量調節バルブとを有するこ
とを特徴とする海水淡水化装置。
4. The seawater desalination apparatus according to claim 1, wherein the seawater discharge means has one end connected to a seawater discharge port of the reduced-pressure evaporator and the other end disposed on the sea surface side. A seawater desalination comprising: a discharge pipe; a seawater discharge pump provided in the seawater discharge pipe; and a seawater discharge control valve provided on a discharge side of the seawater discharge pump to control a discharge amount of seawater. apparatus.
【請求項5】 請求項1から4までのいずれかに記載の
海水淡水化装置において、海水排出手段から排出される
海水の一部をとり込み、減圧蒸発器内で散水を連続的に
行わせる海水散水手段を有することを特徴とする海水淡
水化装置。
5. The seawater desalination apparatus according to claim 1, wherein a part of the seawater discharged from the seawater discharging means is taken in and the water is continuously sprayed in the reduced-pressure evaporator. A seawater desalination apparatus comprising seawater sprinkling means.
【請求項6】 請求項5記載の海水淡水化装置におい
て、海水散水手段は、一端が前記海水排出管の海水排出
ポンプの吐出側に分岐して接続され他端が前記減圧蒸発
器内の上部に挿入された海水散水管と、この減圧蒸発器
内においてその端部に設けられた散水ノズルと、前記海
水散水管に設けられ海水の散水量を調節する海水散水量
調節バルブとを有することを特徴とする海水淡水化装
置。
6. The seawater desalination apparatus according to claim 5, wherein one end of the seawater sprinkling means is branched and connected to the discharge side of the seawater discharge pump of the seawater discharge pipe, and the other end is an upper part in the decompression evaporator. A seawater sprinkler pipe inserted into the seawater sprinkler, a sprinkler nozzle provided at an end thereof in the reduced-pressure evaporator, and a seawater sprinkler amount control valve provided in the seawater sprinkler pipe for adjusting the amount of seawater sprinkler. Characterized seawater desalination equipment.
【請求項7】 請求項2、4および6記載の海水淡水化
装置において、制御手段は、減圧蒸発器内の海水の液位
を検出する液位検出計と、この液位検出計の検出値に基
づいて海水供給量調節バルブ、海水排出量調節バルブ、
海水排出ポンプおよび海水散水量調節バルブの少くとも
1以上を制御する制御器とを有することを特徴とする海
水淡水化装置。
7. The seawater desalination apparatus according to claim 2, wherein the control means comprises: a liquid level detector for detecting the level of seawater in the reduced-pressure evaporator; and a detection value of the liquid level detector. Seawater supply control valve, seawater discharge control valve, based on
A controller for controlling at least one of a seawater discharge pump and a seawater sprinkling amount regulating valve.
JP10017490A 1998-01-29 1998-01-29 Seawater desalting device Pending JPH11216459A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10017490A JPH11216459A (en) 1998-01-29 1998-01-29 Seawater desalting device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10017490A JPH11216459A (en) 1998-01-29 1998-01-29 Seawater desalting device

Publications (1)

Publication Number Publication Date
JPH11216459A true JPH11216459A (en) 1999-08-10

Family

ID=11945458

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10017490A Pending JPH11216459A (en) 1998-01-29 1998-01-29 Seawater desalting device

Country Status (1)

Country Link
JP (1) JPH11216459A (en)

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US6505948B2 (en) 2001-03-28 2003-01-14 Fusion Uv Systems, Inc. Method of modifying the spectral distribution of high-intensity ultraviolet lamps
JP4621955B2 (en) * 2001-08-16 2011-02-02 Necファシリティーズ株式会社 Method and apparatus for sterilizing infectious wastewater
JP2003053326A (en) * 2001-08-16 2003-02-25 Nec Ameniplantex Ltd Sterilization treatment method for infectious waste water and equipment for the same
WO2003066528A1 (en) * 2002-02-07 2003-08-14 Sang-Beom Kim Multi-effect concentrating system and method
WO2004108860A1 (en) * 2003-06-09 2004-12-16 Hitachi, Ltd. Novel fuel production plant and seawater desalination system for use therein
JPWO2004108860A1 (en) * 2003-06-09 2006-07-20 株式会社日立製作所 New fuel production plant and seawater desalination equipment used therefor
JP2007512953A (en) * 2003-12-02 2007-05-24 シルバン ソース、 インク. Fully automated water treatment control system
WO2006056026A1 (en) * 2004-11-29 2006-06-01 Aquamill Five Star Pty Ltd Liquid treatment device and method
EP1914614B1 (en) * 2006-09-28 2012-08-15 Taichi Inada Proportional pressure control valve
CN100462282C (en) * 2006-11-14 2009-02-18 何诺 Super conducting energy saving desalination drinking water making system of ocean ship
US9873618B2 (en) 2012-12-27 2018-01-23 Panasonic Intellectual Property Management Co., Ltd. Measurement system included in desalination system, desalination system, and desalination method
US9822019B2 (en) 2013-01-18 2017-11-21 Panasonic Intellectual Property Management Co., Ltd. Desalination system and desalination method
CN105776384A (en) * 2014-12-15 2016-07-20 哈尔滨市三和佳美科技发展有限公司 Negative-pressure solar-energy seawater desalination device
CN113371771A (en) * 2020-02-25 2021-09-10 笹仓机械工程有限公司 Control device, control method, and recording medium for recording control program for controlling vacuum evaporation type water producing device
CN114537634A (en) * 2022-03-14 2022-05-27 中国船舶科学研究中心 Special fresh water preparation system for ice region sailing ship and control method
CN114537634B (en) * 2022-03-14 2022-12-30 中国船舶科学研究中心 Special fresh water preparation system for ice region sailing ship and control method
CN117228909A (en) * 2023-11-16 2023-12-15 烟台市弗兰德电子科技有限公司 Seawater desalination system
CN117228909B (en) * 2023-11-16 2024-02-09 烟台市弗兰德电子科技有限公司 Seawater desalination system

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