JPH10277535A - Seawater-desalting apparatus - Google Patents

Seawater-desalting apparatus

Info

Publication number
JPH10277535A
JPH10277535A JP9091766A JP9176697A JPH10277535A JP H10277535 A JPH10277535 A JP H10277535A JP 9091766 A JP9091766 A JP 9091766A JP 9176697 A JP9176697 A JP 9176697A JP H10277535 A JPH10277535 A JP H10277535A
Authority
JP
Japan
Prior art keywords
seawater
ice
pure
storage tank
pure ice
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.)
Granted
Application number
JP9091766A
Other languages
Japanese (ja)
Other versions
JP3651170B2 (en
Inventor
Naoyuki Sato
尚之 佐藤
Shunei Osono
俊英 大園
Masahide Ichikawa
雅英 市川
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.)
Meidensha Corp
Meidensha Electric Manufacturing Co Ltd
Original Assignee
Meidensha Corp
Meidensha Electric Manufacturing 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 Meidensha Corp, Meidensha Electric Manufacturing Co Ltd filed Critical Meidensha Corp
Priority to JP09176697A priority Critical patent/JP3651170B2/en
Publication of JPH10277535A publication Critical patent/JPH10277535A/en
Application granted granted Critical
Publication of JP3651170B2 publication Critical patent/JP3651170B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/22Treatment of water, waste water, or sewage by freezing
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/08Seawater, e.g. for desalination
    • 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

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Physical Water Treatments (AREA)

Abstract

PROBLEM TO BE SOLVED: To form fresh water while utilizing the cold heat of pure ice precipitating ice lumps containing no impurities from seawater. SOLUTION: A pure ice making apparatus 11 forming ice lumps from seawater operates a freezing device 12 utilizing inexpensive excessive power such as night power and seawater is cooled by an evaporator 121 on a cooling side not only to form pure ice high in purity from seawater but also to separate highly conc. seawater and conc. seawater is sent to a seawater treatment apparatus 13 and pure ice is supplied to an ice storing hot water tank 14. The seawater treatment apparatus 13 forms salt from the supplied conc. seawater and pure ice high in purity is stored in the ice storing hot water tank 14. The stored pure ice is melted by the condensed water from a fresh water storage tank 15 to be stored in the ice storing hot water tank 14. This water is supplied as the cold heat of a refrigerating stocker 16. Condensed water containing waste heat after the utilization of the cold heat in the refrigerating stocker 16 is stored in the fresh water storing tank 15. A condenser 122 on the radiation side of the freezing device 12 is attached to the fresh water storage tank 15.

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】この発明は、海水を処理して
淡水化にする海水淡水化システムに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a seawater desalination system for treating seawater to make it desalinated.

【0002】[0002]

【従来の技術】海水を処理し淡水化を図る方式には、蒸
発法、逆浸透法、電気透析法等が実用化されている。こ
の他に、実用化されていないが、凍結融解法(冷凍
法)、透過気化法等がある。(参考資料:平成8年版
日本の水資源(水資源白書) 国土庁編) 上述した海水淡水化システムの中で蒸発法は、海水を加
熱して蒸発させたり、蒸発器に海水を吹き付けたりして
蒸発させたりすることにより、発生した水蒸気を冷却し
て淡水を得る方式である。また、逆浸透法は、水は透過
するが、塩分は透過させないような半透過膜を用いて、
海水を入れた半透過膜の片側に圧力を加えて水だけを透
過させて淡水を得る方式である。
2. Description of the Related Art Evaporation, reverse osmosis, electrodialysis and the like have been put to practical use as a method for treating seawater to make it desalinated. In addition, although not practically used, there are a freeze-thaw method (freezing method), a pervaporation method, and the like. (Reference material: 1996 edition
Japan's water resources (Water Resources White Paper), National Land Agency) The evaporation method in the above-mentioned seawater desalination system is to evaporate by heating seawater or spraying seawater on an evaporator to evaporate. In this method, generated steam is cooled to obtain fresh water. The reverse osmosis method uses a semi-permeable membrane that allows water to permeate but does not allow salt to permeate,
In this system, fresh water is obtained by applying pressure to one side of a semi-permeable membrane containing seawater to allow only water to permeate.

【0003】上記の方式は実用化された海水淡水化方式
であるが、非実用化の方式の中で凍結融解法は、海水中
で純氷の結晶を成長させ、海水中に浮遊する氷結晶だけ
を分離融解するものである。この方式は、LNGの冷熱
を利用して海水を淡水と濃縮海水に分離するシステムで
ある。
The above-mentioned method is a seawater desalination method that has been put into practical use. Among the methods that have not been put into practical use, the freeze-thaw method involves growing pure ice crystals in seawater and then floating ice crystals in the seawater. Only to separate and melt. This system is a system that separates seawater into freshwater and concentrated seawater using the cold heat of LNG.

【0004】[0004]

【発明が解決しようとする課題】上述した実用化された
海水淡水化方式の中で、蒸発法は海水を加熱蒸発させた
りして水蒸気を発生させ、その水蒸気を冷却するため
に、エネルギー消費コストが大きいので、造水コストが
高くつく問題がある。逆浸透法のように、半透過膜を用
いた海水淡水化方式は、造水コストは安くなるが、プラ
ントの敷地面積を多く必要とし、維持費等を多く必要と
するとともに、造水純度が悪く2段階の脱塩工程が必要
となる問題がある。また、非実用化方式である凍結融解
法は、夜間電力、自家発電電力等の余剰電力を利用し
て、安価に海水を純氷と濃縮海水に分離する方式ではな
く、単にLNGの冷熱を利用するだけであるとともに、
単に海水を凍結させると次のような問題が発生する。
Among the above-mentioned seawater desalination systems put into practical use, the evaporation method heats and evaporates seawater to generate steam, and the steam is cooled to reduce the energy consumption cost. Therefore, there is a problem that desalination cost is high. The seawater desalination method using a semi-permeable membrane, like the reverse osmosis method, reduces the cost of freshwater, but requires a lot of plant area, maintenance costs, etc. There is a problem that a two-step desalination process is required. In addition, the freeze-thaw method, which is an impractical method, does not use the surplus power such as nighttime power or private power generation to inexpensively separate seawater into pure ice and concentrated seawater, but simply uses the cold heat of LNG. Just do
Simply freezing seawater causes the following problems.

【0005】通常、水は液体である限り、各種の気体、
液体、固体を十分に溶解し、また、各種の液体、固体と
混合し、各物質を非常によく溶解または、混合するけれ
ども、氷になるときには、分子レベルの大きさではすべ
ての溶質、混合物を排除して、純粋な氷分子の結晶とし
て成長することが知られている。しかし、氷塊のレベル
の大きさでは、氷分子の結晶と結晶の間に海水を含んで
いた溶質、混合物を内包している氷塊になり、純氷だけ
を結晶として大きく成長させることは大変に難しい問題
がある。
[0005] Usually, as long as water is a liquid, various gases,
It dissolves liquids and solids sufficiently, mixes with various liquids and solids, and dissolves or mixes each substance very well, but when it comes to ice, it dissolves all solutes and mixtures at the molecular level. It is known to eliminate and grow as crystals of pure ice molecules. However, at the level of an ice block, it becomes very difficult to grow pure ice as a crystal, because it becomes an ice block containing a solute and a mixture containing seawater between ice crystal crystals. There's a problem.

【0006】この発明は上記の事情に鑑みてなされたも
ので、海水から不純物を含まない氷塊を析出させた純氷
の冷熱を利用しながら淡水を生成するようにした海水淡
水化システムを提供することを課題とする。
The present invention has been made in view of the above circumstances, and provides a seawater desalination system that generates freshwater while utilizing the cold heat of pure ice in which ice blocks containing no impurities are precipitated from seawater. That is the task.

【0007】[0007]

【課題を解決するための手段】この発明は、上記の課題
を達成するために、第1発明は、海水を冷却し、冷却さ
れた海水から純氷と濃縮海水とを生成する純氷製氷装置
と、この純氷製氷装置により生成された純氷を貯蔵する
とともに、貯蔵される純氷を融解して冷水として蓄えら
れる氷蓄熱水槽と、この氷蓄熱水槽に蓄えられた冷水を
冷熱として利用し終わった廃熱を含んだ復水を貯水する
とともに、淡水として蓄える淡水貯水槽とを含むもので
ある。
SUMMARY OF THE INVENTION In order to achieve the above object, a first invention is a pure ice making apparatus for cooling seawater and producing pure ice and concentrated seawater from the cooled seawater. And storing the pure ice generated by the pure ice making apparatus, melting the stored pure ice and storing it as cold water, and utilizing the cold water stored in the ice thermal storage tank as cold heat. The tank includes a condensed water containing waste heat that has ended, and a freshwater storage tank that stores the condensed water as freshwater.

【0008】第2発明は、純氷製氷装置により生成され
た濃縮海水が導入され、この濃縮海水から食塩を生成す
る海水処理装置を設けたものである。
In a second aspect of the present invention, a concentrated seawater generated by a pure ice making device is introduced, and a seawater treatment device for generating salt from the concentrated seawater is provided.

【0009】第3発明は、余剰電力で運転される冷凍装
置を設け、この冷凍装置の蒸発器側で純氷製氷装置に供
給される海水を冷却し、凝縮器側で淡水貯水槽の淡水を
暖めるようにしたものである。
According to a third aspect of the present invention, there is provided a refrigerating apparatus which is operated with surplus electric power, the seawater supplied to the pure ice making apparatus is cooled on the evaporator side of the refrigerating apparatus, and the freshwater in the freshwater storage tank is cooled on the condenser side. It is intended to warm up.

【0010】第4発明は、氷蓄熱水槽には、淡水貯水槽
の淡水を復水として供給して純氷を融解させることを含
むものである。
[0010] A fourth aspect of the present invention is to supply the ice heat storage tank with fresh water from the fresh water storage tank as condensate to melt the pure ice.

【0011】[0011]

【発明の実施の形態】以下この発明の実施の形態を図面
に基づいて説明する。図1において、11は詳細を後述
する海水から氷塊を生成する純氷製氷装置で、この純氷
製氷装置11は、夜間電力や自家発電電力等の安価な余
剰電力を利用して冷凍装置12を運転し、冷却側である
蒸発器121で海水を冷却して、海水から純度の高い純
氷を生成するとともに、高濃度に濃縮された濃縮海水と
を生成する。そして、生成した濃縮海水は海水処理装置
13に送られるとともに、純氷は氷蓄熱水槽14に供給
される。
Embodiments of the present invention will be described below with reference to the drawings. In FIG. 1, reference numeral 11 denotes a pure ice making device for generating ice blocks from seawater, which will be described in detail later. The pure ice making device 11 uses a cheap surplus electric power such as nighttime electric power or privately generated electric power to form a refrigeration apparatus 12. In operation, the seawater is cooled by the evaporator 121 on the cooling side, and pure ice having high purity is generated from the seawater, and concentrated seawater concentrated at a high concentration is generated. Then, the generated concentrated seawater is sent to the seawater treatment device 13, and the pure ice is supplied to the ice heat storage water tank 14.

【0012】海水処理装置13は供給された濃縮海水か
ら、食塩を生成し、塩分として回収する。一方、氷蓄熱
水槽14には純度の高い純氷が貯蔵される。この氷蓄熱
水槽14の純氷は、淡水貯水槽15からの復水で融解さ
れ、一定温度(約4℃)の冷水として氷蓄熱水槽14に
貯水される。この冷水は冷蔵倉庫16の冷熱用として供
給される。なお、この冷水は冷蔵倉庫16に限らず各種
冷却に利用される。
The seawater treatment device 13 generates salt from the supplied concentrated seawater and recovers it as salt. On the other hand, pure ice of high purity is stored in the ice heat storage water tank 14. The pure ice in the ice storage water tank 14 is melted by condensing water from the fresh water storage tank 15 and stored in the ice storage water tank 14 as cold water at a constant temperature (about 4 ° C.). This cold water is supplied for cooling the cold storage 16. This cold water is used not only for the refrigerated warehouse 16 but also for various types of cooling.

【0013】冷蔵倉庫16での冷熱利用が終わった廃熱
を含んだ復水は淡水貯水槽15に貯水される。淡水貯水
槽15には、冷凍装置12の放熱側である凝縮器122
が装着され、貯水槽15の淡水を暖めるとともに、凝縮
器122の冷却を行って冷凍装置12の効率を向上させ
るようにしている。なお、淡水貯水槽15の淡水は、各
種用水に利用したり、前述したように氷蓄熱水槽14の
純氷を融解するための復水として利用される。
Condensed water containing waste heat that has been used in the cold storage 16 is stored in a fresh water storage tank 15. The freshwater storage tank 15 has a condenser 122 on the heat radiation side of the refrigerating device 12.
Is mounted to warm the fresh water in the water storage tank 15 and to cool the condenser 122 to improve the efficiency of the refrigerating device 12. Note that the fresh water in the fresh water storage tank 15 is used for various types of water or used as condensate for melting the pure ice in the ice heat storage water tank 14 as described above.

【0014】次に、上述した純氷製氷装置11の概略構
成を図2により述べる。図2において、31は図示しな
い海水供給管から海水41が導入される槽で、この槽3
1の内底部には散気管32が配置される。散気管32に
はエアポンプ33からエアが供給され、散気管32から
は気泡42が連続的に吹き出される。34は回転ベルト
で、この回転ベルト34は一部分が海水中に没し、他の
部分は槽31の水面上部に出ている。35a、35b、
35cはローラで、そのローラの内、少なくとも1つは
駆動ローラとして形成される。
Next, a schematic configuration of the pure ice making apparatus 11 will be described with reference to FIG. In FIG. 2, reference numeral 31 denotes a tank into which seawater 41 is introduced from a seawater supply pipe (not shown).
An air diffuser 32 is disposed at the inner bottom of the unit 1. Air is supplied to the air diffuser 32 from an air pump 33, and bubbles 42 are continuously blown out from the air diffuser 32. Numeral 34 denotes a rotating belt. Part of the rotating belt 34 is submerged in seawater, and the other part is exposed above the water surface of the tank 31. 35a, 35b,
35c is a roller, at least one of which is formed as a drive roller.

【0015】回転ベルト34の内側には冷却部36とヒ
ータ部37が配設され、冷却部36は、海水中に没する
回転ベルト34の内側に、またヒータ部37は槽31の
上部の回転ベルト34の内側にそれぞれ配設される。3
8は温風ヒータ、39は純氷である氷塊、40は氷生成
部、121は冷凍装置12の蒸発器であり、この蒸発器
121により海水は冷却される。
A cooling section 36 and a heater section 37 are disposed inside the rotating belt 34. The cooling section 36 is provided inside the rotating belt 34 submerged in seawater. Each is disposed inside the belt 34. 3
8 is a hot air heater, 39 is an ice block made of pure ice, 40 is an ice generator, 121 is an evaporator of the refrigeration system 12, and the evaporator 121 cools seawater.

【0016】上記のように構成された純氷製氷装置にお
いて、エアポンプ33を回転させて散気管32により気
泡42を連続的に吹き出させる。この気泡42により海
水は撹拌されると同時に、過冷却状態にはならず0℃を
保持する。冷却部36の表面では、連続的な気泡42の
吹き付けにより不純物を排除しながら、氷の結晶が成長
して行く。成長した氷の結晶は回転ベルト34で搬送さ
れ、ヒータ部37の位置に到達すると、ヒータ部37と
温風ヒータ38により氷が暖められ、特に氷の表面の一
部が融けて水となり、氷の表面に付着した不純物はその
水で洗われて流れ去ってしまう。このため、純粋な氷塊
39となって回転ベルト34から外れて氷塊39が連続
的に生成される。このようにして生成された氷塊39が
図1に示した氷蓄熱水槽14に貯蔵される。
In the pure ice making apparatus constructed as described above, the air pump 33 is rotated so that the air bubbles 42 are continuously blown out by the air diffuser 32. At the same time as the seawater is agitated by the bubbles 42, the seawater is kept at 0 ° C. without being supercooled. Ice crystals grow on the surface of the cooling unit 36 while removing impurities by continuous blowing of bubbles 42. The grown ice crystals are conveyed by the rotating belt 34, and when they reach the position of the heater 37, the ice is warmed by the heater 37 and the hot air heater 38. In particular, a part of the surface of the ice is melted into water, The impurities adhering to the surface are washed away by the water and flow off. As a result, pure ice blocks 39 are removed from the rotating belt 34, and the ice blocks 39 are continuously generated. The ice blocks 39 thus generated are stored in the ice heat storage water tank 14 shown in FIG.

【0017】上記のように構成されたこの発明の実施の
形態においては、純氷だけが成長する部分を設置して、
そこに大きな氷塊を析出させることができるとともに、
LNGの冷熱は勿論、夜間電力や自家発電電力などの余
剰電力を利用した冷凍装置による冷熱を用いることがで
きる。また、分離した純氷は氷蓄熱水槽に貯蔵され、そ
の冷熱を大型業務用冷蔵庫や空調設備に利用した後の冷
水を、淡水として利用でき、さらに、濃縮海水から海水
処理装置により食塩を生成することができる。
In the embodiment of the present invention configured as described above, a portion where only pure ice grows is provided,
A large ice block can be precipitated there,
It is possible to use not only the cold heat of the LNG but also the cold heat generated by a refrigerating apparatus that uses surplus power such as nighttime power or private power generation. In addition, the separated pure ice is stored in an ice heat storage water tank, and after using the cold heat in a large commercial refrigerator or an air conditioner, the cold water can be used as fresh water, and further, salt is generated from the concentrated seawater by a seawater treatment device. be able to.

【0018】[0018]

【発明の効果】以上述べたように、この発明によれば、
海水を純氷と濃縮海水とに分離して、純氷の冷熱を利用
しながら淡水を生成し、一方では濃縮海水から食塩を生
成することができる効果がある。また、この発明によれ
ば、冷熱と淡水が同時に利用できるため、例えば地域冷
暖房を導入するような地域では、省エネルギーだけでな
く、水の有効利用も図ることができる。
As described above, according to the present invention,
There is an effect that seawater is separated into pure ice and concentrated seawater, and freshwater is generated using the cold heat of the pure ice, while salt can be generated from the concentrated seawater. Further, according to the present invention, since cold heat and fresh water can be used simultaneously, in an area where district heating and cooling is introduced, for example, not only energy saving but also effective use of water can be achieved.

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

【図1】この発明の実施の形態を示す海水淡水化システ
ムのシステム構成図。
FIG. 1 is a system configuration diagram of a seawater desalination system showing an embodiment of the present invention.

【図2】純氷製氷装置の概略構成図。FIG. 2 is a schematic configuration diagram of a pure ice making apparatus.

【符号の説明】[Explanation of symbols]

11…純氷製氷装置 12…冷凍装置 13…海水処理装置 14…氷蓄熱水槽 15…淡水貯水槽 16…冷蔵倉庫 DESCRIPTION OF SYMBOLS 11 ... Pure ice making equipment 12 ... Refrigeration equipment 13 ... Seawater treatment equipment 14 ... Ice heat storage water tank 15 ... Fresh water storage tank 16 ... Refrigerated warehouse

─────────────────────────────────────────────────────
────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成10年1月8日[Submission date] January 8, 1998

【手続補正1】[Procedure amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0015[Correction target item name] 0015

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【0015】回転ベルト34の内側には冷却部36とヒ
ータ部37が配設され、図1に示す冷凍装置12の蒸発
器121により冷却される冷却部36は、海水中に没す
る回転ベルト34の内側に、またヒータ部37は槽31
の上部の回転ベルト34の内側にそれぞれ配設される。
38は温風ヒータ、39は純氷である氷塊、40は氷生
成部である
A cooling section 36 and a heater section 37 are disposed inside the rotating belt 34, and the evaporating section of the refrigerating apparatus 12 shown in FIG.
The cooling unit 36 cooled by the heater 121 is inside the rotating belt 34 submerged in seawater, and the heater unit 37 is
Are respectively disposed inside the rotating belt 34 on the upper side.
38 warm air heater, 39 is a pure ice ice mass, 40 is the ice generating unit.

【手続補正2】[Procedure amendment 2]

【補正対象書類名】図面[Document name to be amended] Drawing

【補正対象項目名】図2[Correction target item name] Figure 2

【補正方法】変更[Correction method] Change

【補正内容】[Correction contents]

【図 2】 FIG. 2

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 海水を冷却し、冷却された海水から純氷
と濃縮海水とを生成する純氷製氷装置と、この純氷製氷
装置により生成された純氷を貯蔵するとともに、貯蔵さ
れる純氷を融解して冷水として蓄えられる氷蓄熱水槽
と、この氷蓄熱水槽に蓄えられた冷水を冷熱として利用
し終わった廃熱を含んだ復水を貯水するとともに、淡水
として蓄える淡水貯水槽とを含む海水淡水化システム。
1. A pure ice making device that cools seawater to produce pure ice and concentrated seawater from the cooled seawater, and stores pure ice generated by the pure ice making device and stores the pure ice stored therein. An ice storage tank that melts ice and is stored as cold water, and a freshwater storage tank that stores condensate containing waste heat that has finished using cold water stored in this ice storage tank as cold heat and stores it as fresh water. Including seawater desalination system.
【請求項2】 前記純氷製氷装置により生成された濃縮
海水が導入され、この濃縮海水から食塩を生成する海水
処理装置を設けた請求項1記載の海水淡水化システム。
2. The seawater desalination system according to claim 1, wherein a concentrated seawater generated by the pure ice making device is introduced, and a seawater treatment device for generating salt from the concentrated seawater is provided.
【請求項3】 余剰電力で運転される冷凍装置を設け、
この冷凍装置の蒸発器側で純氷製氷装置に供給される海
水を冷却し、凝縮器側で淡水貯水槽の淡水を暖めるよう
にした請求項1記載の海水淡水化システム。
3. A refrigeration unit operated by surplus electric power is provided.
The seawater desalination system according to claim 1, wherein seawater supplied to the pure ice making device is cooled on an evaporator side of the refrigerating device, and freshwater in a freshwater storage tank is warmed on a condenser side.
【請求項4】 前記氷蓄熱水槽には、淡水貯水槽の淡水
を復水として供給して純氷を融解させることを含む請求
項1及び3記載の海水淡水化システム。
4. The seawater desalination system according to claim 1, further comprising supplying pure water from the freshwater storage tank to the ice heat storage tank as condensate to melt the pure ice.
JP09176697A 1997-04-10 1997-04-10 Seawater desalination system Expired - Fee Related JP3651170B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP09176697A JP3651170B2 (en) 1997-04-10 1997-04-10 Seawater desalination system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP09176697A JP3651170B2 (en) 1997-04-10 1997-04-10 Seawater desalination system

Publications (2)

Publication Number Publication Date
JPH10277535A true JPH10277535A (en) 1998-10-20
JP3651170B2 JP3651170B2 (en) 2005-05-25

Family

ID=14035692

Family Applications (1)

Application Number Title Priority Date Filing Date
JP09176697A Expired - Fee Related JP3651170B2 (en) 1997-04-10 1997-04-10 Seawater desalination system

Country Status (1)

Country Link
JP (1) JP3651170B2 (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100470246B1 (en) * 2002-07-30 2005-02-05 가부시키가이샤 캉꾜 간리 센타 Method of producing desalinized ice from deep seawater
JP2008274130A (en) * 2007-04-27 2008-11-13 Mitsui Zosen Akishima Kenkyusho:Kk Gas hydrate production system
CN102173476A (en) * 2011-03-17 2011-09-07 杜文娟 Method for making ice and desalinating sea water by using beach, tide and cold
CN102320673A (en) * 2011-06-17 2012-01-18 冯静 Method for seawater desalination by utilizing solar energy, natural cold and sea surface
CN102328965A (en) * 2011-06-24 2012-01-25 南京师范大学 Solar seawater desalination plant and operation method thereof
CN102452693A (en) * 2011-03-17 2012-05-16 杜文娟 Facility for desalting seawater with ice preparation by using beach, tide and cold
CN103214052A (en) * 2013-05-15 2013-07-24 广西玉林宏江能源科技有限公司 Energy-saving new scheme for producing fresh water by precooling sea tide pressure seawater
WO2016142075A1 (en) * 2015-03-11 2016-09-15 Siemens Aktiengesellschaft Desalination of saltwater
KR20200064507A (en) * 2018-11-29 2020-06-08 주식회사 자동기 Seawater concentration tank, apparatus for producing snow removal using sea water and the driving method thereof

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103241789A (en) * 2013-05-28 2013-08-14 广西玉林宏江能源科技有限公司 Novel energy-saving method and device for conveying seawater to desalinator to produce fresh water after pressing seawater to deep sea for cooling through sea waves
CN106629951B (en) * 2016-12-06 2019-05-10 房诗宏 Solid-liquid inversion of phases brine concentration device
CN106629952B (en) * 2016-12-06 2019-05-10 宋世果 Solid-liquid inversion of phases brine concentration method
CN107128993B (en) * 2017-05-04 2020-08-07 国家海洋局天津海水淡化与综合利用研究所 Power plant flue gas waste heat direct evaporation type desalination system with flue gas reheating function

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100470246B1 (en) * 2002-07-30 2005-02-05 가부시키가이샤 캉꾜 간리 센타 Method of producing desalinized ice from deep seawater
JP2008274130A (en) * 2007-04-27 2008-11-13 Mitsui Zosen Akishima Kenkyusho:Kk Gas hydrate production system
CN102173476A (en) * 2011-03-17 2011-09-07 杜文娟 Method for making ice and desalinating sea water by using beach, tide and cold
CN102452693A (en) * 2011-03-17 2012-05-16 杜文娟 Facility for desalting seawater with ice preparation by using beach, tide and cold
CN102320673A (en) * 2011-06-17 2012-01-18 冯静 Method for seawater desalination by utilizing solar energy, natural cold and sea surface
CN102328965A (en) * 2011-06-24 2012-01-25 南京师范大学 Solar seawater desalination plant and operation method thereof
CN103214052A (en) * 2013-05-15 2013-07-24 广西玉林宏江能源科技有限公司 Energy-saving new scheme for producing fresh water by precooling sea tide pressure seawater
WO2016142075A1 (en) * 2015-03-11 2016-09-15 Siemens Aktiengesellschaft Desalination of saltwater
KR20200064507A (en) * 2018-11-29 2020-06-08 주식회사 자동기 Seawater concentration tank, apparatus for producing snow removal using sea water and the driving method thereof

Also Published As

Publication number Publication date
JP3651170B2 (en) 2005-05-25

Similar Documents

Publication Publication Date Title
JPH10277535A (en) Seawater-desalting apparatus
JP4062374B2 (en) Ice maker
CN107585936B (en) Zero-emission treatment process and device for high-salinity wastewater
US4406748A (en) Liquid purification system
US5417084A (en) Vacuum concentrating plant
JP2001276808A (en) Process for separating water, and water separator for the same
US4420318A (en) Vacuum freezing process with multiple phase transformations of low pressure vapor
CN109110853A (en) A kind of wastewater treatment method and system
US4318772A (en) Saturated liquor cooling tower
JP2001526959A (en) Desalination method and desalination apparatus
FI81501C (en) Procedure for icing
JP3635847B2 (en) Pure ice making machine
RU2315002C2 (en) Thermoelectric apparatus used for continuous production of the sweet water by the method of the sea water freezing-out
US4019951A (en) Magma cooling tower
JP3584671B2 (en) Cooling system in production process
GB2304296A (en) Distillation process
JPH0379041B2 (en)
JPH01160819A (en) Simultaneous production of table salt and freshwater
JP2000325941A (en) Device for desalting salt water
FI73818B (en) FOERFARANDE FOER VAERMEUPPTAGNING UR TILLFRYSANDE VAETSKA.
RU2142329C1 (en) Method of inverse-osmotic separation of crystals from mineralized water (versions)
JPH046333A (en) Method and apparatus for adjusting concentration of circulation liquid in open type heating tower
Chang et al. Freeze Desalination-Membrane Distillation Hybrid Systems
JPS6377587A (en) steam generator
CN108455779A (en) A kind of ADD efficient cryogenics low consumption desalination process and its device

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20041027

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20041109

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20041222

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20050201

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20050214

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080304

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090304

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090304

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100304

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110304

Year of fee payment: 6

LAPS Cancellation because of no payment of annual fees