JPH08246811A - Fresh water generation and salt manufacture by waste energy - Google Patents

Fresh water generation and salt manufacture by waste energy

Info

Publication number
JPH08246811A
JPH08246811A JP7091225A JP9122595A JPH08246811A JP H08246811 A JPH08246811 A JP H08246811A JP 7091225 A JP7091225 A JP 7091225A JP 9122595 A JP9122595 A JP 9122595A JP H08246811 A JPH08246811 A JP H08246811A
Authority
JP
Japan
Prior art keywords
salt
fresh water
seawater
water
waste
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
JP7091225A
Other languages
Japanese (ja)
Inventor
Tadayoshi Tomita
忠義 富田
Takashi Nitta
隆 仁田
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 JP7091225A priority Critical patent/JPH08246811A/en
Publication of JPH08246811A publication Critical patent/JPH08246811A/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
    • Y02A20/131Reverse-osmosis

Abstract

PURPOSE: To prevent waste water from causing environmental disruption by generating fresh water and manufacturing salt by the use of waste energy without discharging the waste water. CONSTITUTION: Steam generated in a refuse incinerator heat recovery unit 1 drives a generator 3 through a steam turbine 2. It is condensed by a salt manufacturing unit 6 and fed back to the heat recovery unit. Sea water pressured by a sea water pump 4 is desalinated by a desalination unit 5. Residual sea water is separated into salt and fresh water by the salt manufacturing unit 6.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明が解決しようとする課題】本発明方法は、海水よ
り飲料水、その他の淡水を製造するに際し、廃棄物の焼
却、ガス化により得られる熱及び電気エネルギーを主な
エネルギー源とし、残海水から塩化ナトリウム、その他
の塩を製造し、残海水の排出をしない方法である。
In the method of the present invention, when producing drinking water or other fresh water from seawater, heat and electric energy obtained by incineration and gasification of wastes are used as main energy sources, and residual seawater is used. It is a method of producing sodium chloride and other salts from sewage and not discharging residual seawater.

【0002】廃棄物エネルギーの有効利用は、エネルギ
ー問題と同時に地球温暖化問題対策としても重要な方策
である。廃棄物に含まれる塩化水素、その金属腐蝕性物
質による腐蝕の問題から、通常の材料では熱回収に際し
て蒸気の温度300℃が限度で、それ以上の蒸気を得る
には高価な材料を使用することが必要である。
The effective use of waste energy is an important measure not only as an energy problem but also as a measure against global warming. Due to the problem of corrosion due to hydrogen chloride contained in waste and its corrosive substances, the temperature of steam is usually limited to 300 ° C when recovering heat from ordinary materials, and expensive materials should be used to obtain steam above that level. is necessary.

【0003】廃棄物エネルギーの有効利用の方策のひと
つは、比較的低レベルの温度で仕様されるプロセスに適
用することである。海水の淡水化は比較的低レベルの熱
を大量に必要とするので廃棄物エネルギー有効利用に適
した分野である。
One of the strategies for effective utilization of waste energy is to apply it to processes specified at relatively low levels of temperature. Desalination of seawater is a field suitable for effective use of waste energy because it requires a large amount of heat at a relatively low level.

【0004】[0004]

【従来の技術】近年、渇水により年間を通じて制限給水
をせざるを得ない都市がある。水源の開発には長年月を
必要とするので、海水の淡水化が検討されているが、海
水より淡水を得た後の残海水の排出による生態系の破壊
に虞のために実現していない。また、エネルギー源とし
て化石燃料、電力を用いるので高いコストは避けられな
い。
2. Description of the Related Art In recent years, some cities have been forced to supply limited water throughout the year due to drought. Desalination of seawater is being considered because it takes many years to develop a water source, but it has not been realized due to the fear of destruction of the ecosystem due to the discharge of residual seawater after obtaining freshwater from seawater. . Also, since fossil fuels and electric power are used as energy sources, high costs are inevitable.

【0005】[0005]

【発明の効果】本発明方法によれば、水不足で悩まされ
る都市が、その都市で発生する廃棄物のエネルギーの有
効利用により淡水と共に塩を併産することにより、環境
を破壊することなく、低コストで水道水を得ることがで
きる。
EFFECTS OF THE INVENTION According to the method of the present invention, a city suffering from a water shortage produces salt together with fresh water by effectively utilizing the energy of the waste generated in the city, thereby reducing the environment without destroying the environment. You can get tap water at a cost.

【0006】[0006]

【課題を解決するための手段】本発明方法で使用される
廃棄物エネルギーを得るプロセスは、最も一般的な廃棄
物の焼却熱の回収であるが、廃棄物のガス化、更に発生
するガスの焼却により、発生する熱の回収でも良い。
The process for obtaining waste energy used in the method of the present invention is recovery of incineration heat of waste, which is the most common method. It is also possible to recover the heat generated by incineration.

【0007】海水の淡水化方法としては、フラッシュ蒸
発法、逆浸膜、効用管等、在来の淡水化プロセスのいず
れにも含まれる。残海水より塩を得る方法は、通常の濃
縮、晶析の方法で良い。
[0007] The desalination method of seawater includes any of the conventional desalination processes such as the flash evaporation method, the reverse immersion membrane, the effect tube and the like. The method for obtaining the salt from the residual seawater may be an ordinary concentration and crystallization method.

【0008】[0008]

【実施例】図−1において焼却炉熱回収設備の能力は2
00T/Dのごみ(発熱量2,700kcal/kg)
を処理する能力を持ち、最大限の発電を行う。原料海水
はポンプで昇圧され、逆浸膜に入り、淡水18,000
T/Dと濃縮22,000T/Dは電気透析設備で濃厚
食塩水と残海水に分離され、濃厚食塩水より食塩550
T/Dが得られた。残海水20,000T/Dは、原料
海水に混合されポンプで昇圧される。
[Example] In Figure 1, the capacity of incinerator heat recovery equipment is 2
Waste of 00T / D (heat value 2,700kcal / kg)
It has the ability to process and generate maximum power. The raw seawater is pumped up, enters the reverse osmosis membrane, and reaches 18,000 fresh water.
T / D and concentrated 22,000 T / D were separated into concentrated saline solution and residual seawater in an electrodialysis facility.
T / D was obtained. The residual seawater of 20,000 T / D is mixed with the raw seawater and the pressure is increased by a pump.

【0009】[0009]

【発明の効果】本発明方法によれば、残海水の排出によ
る環境破壊の恐れは全くない。また、目的の淡水を得る
に必要な原海水の量は、従来法の約30〜50%とな
り、排水管は不要で原海水採取、排水関係の設備費、動
力費が大きく低減される。また、淡水化設備で副生する
高濃度の残海水より得られた塩類は純度が高く、食用、
薬用に用いることが出来、高い付加価値が得られる。
According to the method of the present invention, there is no risk of environmental damage due to discharge of residual seawater. Further, the amount of raw seawater required to obtain the target fresh water is about 30 to 50% of that in the conventional method, and a drainage pipe is not required, so that raw seawater collection, drainage-related equipment costs, and power costs are greatly reduced. In addition, the salt obtained from the high-concentration residual seawater produced as a byproduct in the desalination facility has high purity and is edible.
It can be used for medicinal purposes and has high added value.

【0010】本発明方法は、通常エネルギーの価格とし
て事実上、評価されていない廃棄物のエネルギーより発
生する熱、蒸気、電力を利用することにより、低コスト
の淡水を得ることが出来る。補助的に廃棄物エネルギー
以外の電力、化石燃料を用いた場合も、本発明に属する
ことは言うまでもない。
The method of the present invention makes it possible to obtain low-cost fresh water by utilizing the heat, steam, and electric power generated from the energy of waste which is not evaluated as the price of ordinary energy. Needless to say, the present invention also applies to the case where electric power or fossil fuel other than waste energy is used supplementarily.

【0011】[0011]

【図1】において、廃棄物焼却炉熱回収設備(1)で発
生した蒸気は、蒸気タービン(2)で発電機(3)を駆
動し、造塩設備(6)で復水し、熱回収設備に戻る。発
電機(3)で発生した電力で、海水ポンプ(4)が駆動
される。海水ポンプで昇圧された海水は、淡水化設備で
淡水化される。残海水は造塩設備で塩と淡水に分離され
る。造塩設備で発生する残海水は、海水ポンプの入口で
海水と混合され、淡水化設備に送られる。
[Fig. 1] In Fig. 1, the steam generated in the waste incinerator heat recovery equipment (1) drives the generator (3) in the steam turbine (2) and is condensed in the salt making equipment (6) to recover the heat. Return to equipment. Electric power generated by the generator (3) drives the seawater pump (4). Seawater that has been boosted by the seawater pump is desalinated by the desalination facility. The residual seawater is separated into salt and fresh water by a salt-making facility. Residual seawater generated in the salt production equipment is mixed with seawater at the inlet of the seawater pump and sent to the desalination equipment.

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

【図1】廃棄物エネルギーによる造水、造塩システムの
フロー図である。
FIG. 1 is a flow diagram of a water / salt making system using waste energy.

【符号の説明】[Explanation of symbols]

1 焼却炉熱回収設備 2 蒸気タービン 3 発電機 4 海水ポンプ 5 淡水化設備 6 造塩設備 1 Incinerator heat recovery facility 2 Steam turbine 3 Generator 4 Seawater pump 5 Desalination facility 6 Salt production facility

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 海水を淡水化して飲料水、その他の淡水
を製造するに際し、そのエネルギーとして廃棄物の焼
却、又はガス化により得られる熱及び電気エネルギーを
用い、残海水より塩化ナトリウム、その他の塩を製造
し、残海水を排出することなく淡水を製造することを特
徴とする淡水及び塩の製造方法。
1. When desalinating seawater to produce drinking water or other fresh water, heat and electric energy obtained by incineration of waste or gasification are used as the energy, and sodium chloride or other A method for producing fresh water and salt, which comprises producing salt and producing fresh water without discharging residual seawater.
JP7091225A 1995-03-14 1995-03-14 Fresh water generation and salt manufacture by waste energy Pending JPH08246811A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7091225A JPH08246811A (en) 1995-03-14 1995-03-14 Fresh water generation and salt manufacture by waste energy

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7091225A JPH08246811A (en) 1995-03-14 1995-03-14 Fresh water generation and salt manufacture by waste energy

Publications (1)

Publication Number Publication Date
JPH08246811A true JPH08246811A (en) 1996-09-24

Family

ID=14020489

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7091225A Pending JPH08246811A (en) 1995-03-14 1995-03-14 Fresh water generation and salt manufacture by waste energy

Country Status (1)

Country Link
JP (1) JPH08246811A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101506312B1 (en) * 2014-06-26 2015-03-27 유대형 Using solar and magnetron for salt production and seawater desalination method
KR101506315B1 (en) * 2014-06-26 2015-03-27 유대형 Using magnetron for salt production methods and power system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101506312B1 (en) * 2014-06-26 2015-03-27 유대형 Using solar and magnetron for salt production and seawater desalination method
KR101506315B1 (en) * 2014-06-26 2015-03-27 유대형 Using magnetron for salt production methods and power system

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