JPS6145520B2 - - Google Patents

Info

Publication number
JPS6145520B2
JPS6145520B2 JP53113858A JP11385878A JPS6145520B2 JP S6145520 B2 JPS6145520 B2 JP S6145520B2 JP 53113858 A JP53113858 A JP 53113858A JP 11385878 A JP11385878 A JP 11385878A JP S6145520 B2 JPS6145520 B2 JP S6145520B2
Authority
JP
Japan
Prior art keywords
seawater
desalination
heat
heat pump
shell
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
JP53113858A
Other languages
Japanese (ja)
Other versions
JPS5539286A (en
Inventor
Makoto Sano
Hiroyoshi Kusakabe
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.)
Tokyo Sanyo Electric Co Ltd
Sanyo Denki Co Ltd
Original Assignee
Tokyo Sanyo Electric Co Ltd
Sanyo Denki 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 Tokyo Sanyo Electric Co Ltd, Sanyo Denki Co Ltd filed Critical Tokyo Sanyo Electric Co Ltd
Priority to JP11385878A priority Critical patent/JPS5539286A/en
Publication of JPS5539286A publication Critical patent/JPS5539286A/en
Publication of JPS6145520B2 publication Critical patent/JPS6145520B2/ja
Granted 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
    • 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
    • Y02A20/138Water desalination using renewable energy
    • Y02A20/142Solar thermal; Photovoltaics
    • 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
    • Y02A20/20Controlling water pollution; Waste water treatment
    • Y02A20/208Off-grid powered water treatment
    • Y02A20/212Solar-powered wastewater sewage treatment, e.g. spray evaporation

Landscapes

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

Description

【発明の詳細な説明】 本発明は、海水から淡水を得る海水淡水化装置
に関し、特に、熱効率良く、低コストで淡水を得
ることを目的とする。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a seawater desalination apparatus for obtaining fresh water from seawater, and in particular, an object of the present invention is to obtain fresh water with high thermal efficiency and at low cost.

以下に吸収式のヒートポンプ式冷凍機を用いた
実施例を示す図面に従い説明すると、1は発生器
2,凝縮器3,蒸発器4,吸収器5等から構成さ
れた公知の吸収式のヒートポンプ式冷凍機、6
は、海水の蒸発室7と水蒸気の凝縮室8とを有す
る淡水化胴であり、ヒートポンプ式冷凍機1の駆
動熱源には、循環ポンプ9によつて循環する熱媒
を加熱して発生器2に供給する太陽熱集熱器10
および発生器2における加熱熱量の不足を適宜補
なう高温水加熱器11または、太陽熱に関係のな
いその他の、例えば排熱等100℃以上の温水を得
ることができる熱源12が用いられる。
Below, an explanation will be given with reference to the drawings showing an example using an absorption type heat pump type refrigerator. 1 is a known absorption type heat pump type refrigerator consisting of a generator 2, a condenser 3, an evaporator 4, an absorber 5, etc. Freezer, 6
is a desalination shell having a seawater evaporation chamber 7 and a water vapor condensation chamber 8, and the driving heat source of the heat pump type refrigerator 1 is a generator 2 which heats a heat medium circulated by a circulation pump 9. Solar heat collector 10 that supplies
A high-temperature water heater 11 that appropriately compensates for the lack of heating heat in the generator 2, or another heat source 12 that can obtain hot water of 100° C. or higher, such as exhaust heat, is used, which is not related to solar heat.

また、ヒートポンプ式吸収冷凍機1の加熱熱源
には循環ポンプ13によつて海14から蒸発器4
に供給される海水が用いられる一方、別の循環ポ
ンプ15により淡水化胴6の冷却器16を経て吸
収器5および凝縮器3に流入する海水は、このヒ
ートポンプ式冷凍機1の吸収ヒートポンプ機能に
より発生器2および蒸発器4において汲み上げた
熱言い代えればこの熱と同じ量だけ吸収器5およ
び凝縮器3から放出される熱で昇温され、蒸発室
7に流入散布し、フラツシユされることにより、
水滴が沸騰し、海水中の水分が蒸気となつて気化
分解される。このように、海水を吸収式のヒート
ポンプ式冷凍機1で昇温することにより、蒸発器
7において海水を沸騰させるための熱源として水
蒸気の分離される海水と同温もしくはそれ以下の
温度の流体すなわち海水の熱を活用することが可
能となり、その分、海水の単位量当りの水蒸気の
分離量を増やすことができる。
In addition, the heating heat source of the heat pump absorption refrigerator 1 is supplied from the sea 14 to the evaporator 4 by means of a circulation pump 13.
On the other hand, the seawater that flows into the absorber 5 and condenser 3 via the cooler 16 of the desalination shell 6 by another circulation pump 15 is processed by the absorption heat pump function of the heat pump refrigerator 1. In other words, the same amount of heat pumped up in the generator 2 and evaporator 4 is heated by the heat released from the absorber 5 and condenser 3, flows into the evaporation chamber 7, is dispersed, and is flushed. ,
The water droplets boil, and the water in the seawater turns into steam and is vaporized and decomposed. In this way, by raising the temperature of seawater with the absorption type heat pump refrigerator 1, a fluid having the same temperature or lower temperature as the seawater from which water vapor is separated is used as a heat source for boiling the seawater in the evaporator 7. It becomes possible to utilize the heat of seawater, and the amount of water vapor separated per unit amount of seawater can be increased accordingly.

蒸発室7の水蒸気は、凝縮室8に流入し、冷却
器16を流れる海水で冷却凝縮されて真水17と
なり、開閉弁18を適宜、開放して淡水槽19に
真水を貯え、必要に応じて外部に供給される。
The water vapor in the evaporation chamber 7 flows into the condensation chamber 8, where it is cooled and condensed by the seawater flowing through the cooler 16 to become fresh water 17. The on-off valve 18 is opened as appropriate to store fresh water in the fresh water tank 19, and the fresh water is stored as needed. Supplied externally.

また、水蒸気が分離され濃縮された海水は液排
出のできる真空ポンプ20を介して海14に戻さ
れる。
Further, the seawater from which water vapor has been separated and concentrated is returned to the sea 14 via a vacuum pump 20 capable of liquid discharge.

真空ポンプ20はこのようにして淡水化胴6の
内部の圧力を50℃程度の海水が沸騰できるような
低い圧力、(例えば30mmHg)に保つ。
In this way, the vacuum pump 20 maintains the pressure inside the desalination shell 6 at a low pressure (for example, 30 mmHg) at which seawater at about 50° C. can be boiled.

尚、図中に表示した温度は、以上の実施例によ
る場合の各部の液温の概略の値を示したものであ
る。
It should be noted that the temperatures shown in the figure indicate approximate values of the liquid temperature at each part in the case of the above embodiment.

このように、本発明の海水淡水化装置において
は、ヒートポンプ式冷凍機の駆動機構として太陽
熱温水器のような低温(90℃以上)の熱源を用
い、加熱熱源として海水を用いる一方、真水を得
るための水蒸気凝縮用の冷却水として海水を用
い、かつ、かかる冷却時に予熱された冷却用海水
をヒートポンプ式冷凍機に導びいて昇温すること
により装置外への熱損失を減じたので、極く僅か
な運転費用で海水から真水が得られるのみなら
ず、太陽熱源や排熱等の駆動熱源の熱量が不足
し、補助熱源に燃料を用いる場合でも、熱効率の
良い淡水化装置として少にい燃料消費で運転がで
き、かつまた、淡水化する海水をこれより温度の
高い熱源のみで昇温する場合とくらべて淡水化さ
れる海水よりも低温の海の熱を活用した分だけ海
水の単位量当りの真水取得量を増大させることが
できる。
As described above, in the seawater desalination apparatus of the present invention, a low-temperature (90°C or higher) heat source such as a solar water heater is used as the drive mechanism of the heat pump type refrigerator, and while seawater is used as the heating heat source, fresh water is obtained. By using seawater as the cooling water for water vapor condensation during cooling, and by guiding the preheated cooling seawater to a heat pump type refrigerator to raise its temperature, heat loss to the outside of the equipment is reduced. Not only can fresh water be obtained from seawater with very little operating cost, but even when the driving heat source such as solar heat source or waste heat is insufficient and fuel is used as an auxiliary heat source, it is a desalination device with high thermal efficiency. It can be operated by consuming fuel, and compared to heating the seawater to be desalinated using only a heat source with a higher temperature, the unit of seawater is reduced by utilizing the heat of the sea, which is lower in temperature than the seawater to be desalinated. The amount of fresh water obtained per unit amount can be increased.

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

図は吸収式のヒートポンプ式冷凍機を用いた本
発明の一実施例を示す海水淡水化装置の回路構成
図である。 1……吸収式のヒートポンプ式冷凍機、2……
発生器、3……凝縮器、4……蒸発器、5……吸
収器、7……蒸発室、8……凝縮室、10……太
陽熱集熱器、16……冷却器。
The figure is a circuit configuration diagram of a seawater desalination apparatus showing an embodiment of the present invention using an absorption heat pump type refrigerator. 1... Absorption heat pump refrigerator, 2...
Generator, 3... Condenser, 4... Evaporator, 5... Absorber, 7... Evaporation chamber, 8... Condensation chamber, 10... Solar heat collector, 16... Cooler.

Claims (1)

【特許請求の範囲】[Claims] 1 海からの海水を淡水化胴の凝縮室、ヒートポ
ンプ式吸収冷凍機の吸収器および凝縮器の順に流
しつつ昇温させた後淡水化胴の蒸発室に導きここ
で沸騰させることにより濃縮して海へ戻す海水用
流路を介して淡水化胴とヒートポンプ式吸収冷凍
機とを組み合わせ、このヒートポンプ式吸収冷凍
機の熱源として蒸発器には海からの海水を供給す
るよう海水の供給路を配備すると共に発生器には
太陽熱利用温水あるいはこれを同温レベルもしく
はそれ以上の温度レベルの流体を供給するよう熱
源流体の供給路を配備し、かつ、淡水化胴の蒸発
室で海水から分離された水蒸気を凝縮室で液化し
て真水として取出すよう真水の取出し口を淡水化
胴に設けて構成した海水淡水化装置。
1 Seawater from the ocean is passed through the condensation chamber of the desalination shell, the absorber of the heat pump absorption refrigerator, and the condenser in order to raise its temperature, and then guided to the evaporation chamber of the desalination shell where it is boiled and concentrated. The desalination shell is combined with a heat pump type absorption refrigerator via a seawater flow path that returns to the sea, and a seawater supply path is installed to supply seawater from the sea to the evaporator as a heat source for the heat pump type absorption refrigerator. At the same time, the generator is equipped with a heat source fluid supply path to supply solar hot water or a fluid at the same or higher temperature level, and is separated from seawater in the evaporation chamber of the desalination cylinder. A seawater desalination device is constructed by providing a fresh water outlet in the desalination cylinder so that water vapor is liquefied in a condensation chamber and extracted as fresh water.
JP11385878A 1978-09-13 1978-09-13 Sea water desalting apparatus Granted JPS5539286A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11385878A JPS5539286A (en) 1978-09-13 1978-09-13 Sea water desalting apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11385878A JPS5539286A (en) 1978-09-13 1978-09-13 Sea water desalting apparatus

Publications (2)

Publication Number Publication Date
JPS5539286A JPS5539286A (en) 1980-03-19
JPS6145520B2 true JPS6145520B2 (en) 1986-10-08

Family

ID=14622833

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11385878A Granted JPS5539286A (en) 1978-09-13 1978-09-13 Sea water desalting apparatus

Country Status (1)

Country Link
JP (1) JPS5539286A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109721122A (en) * 2019-01-18 2019-05-07 湖南铁道职业技术学院 A kind of small-sized solar absorption refrigeration production water installations and production water method of freezing
CN117185389A (en) * 2020-12-16 2023-12-08 淄博环能海臣环保技术服务有限公司 Concentrated crystallization desalination water treatment facilities of high salt waste water will contain through lithium bromide unit
CN117164037A (en) * 2020-12-16 2023-12-05 淄博环能海臣环保技术服务有限公司 Concentrated crystallization of high salt wastewater contains salt desalination water processing apparatus through heat pump
CN115010200B (en) * 2022-08-10 2022-10-21 山东天瑞重工有限公司 System for utilize sea water source heat pump to carry out sea water desalination

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5265772A (en) * 1975-11-28 1977-05-31 Kazuo Uema Method of manufacturing water by temperature difference using solar heat collector

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5265772A (en) * 1975-11-28 1977-05-31 Kazuo Uema Method of manufacturing water by temperature difference using solar heat collector

Also Published As

Publication number Publication date
JPS5539286A (en) 1980-03-19

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