JPH0975935A - Reverse osmosis desalting method for sea water making common use of sea water pumping up power plant and equipment - Google Patents

Reverse osmosis desalting method for sea water making common use of sea water pumping up power plant and equipment

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Publication number
JPH0975935A
JPH0975935A JP7271684A JP27168495A JPH0975935A JP H0975935 A JPH0975935 A JP H0975935A JP 7271684 A JP7271684 A JP 7271684A JP 27168495 A JP27168495 A JP 27168495A JP H0975935 A JPH0975935 A JP H0975935A
Authority
JP
Japan
Prior art keywords
seawater
water
pressure
reverse osmosis
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
JP7271684A
Other languages
Japanese (ja)
Inventor
Kunio Muneishi
邦男 宗石
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 JP7271684A priority Critical patent/JPH0975935A/en
Publication of JPH0975935A publication Critical patent/JPH0975935A/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

PROBLEM TO BE SOLVED: To embody a cost effective operation by desalting the sea water by reverse osmosis with a high-pressure pump by utilizing the midnight excess electric power, driving a generator by utilizing a high-pressure water wheel with the residual pressure of the concd. sea water, lifting the water to a sea water storage bond on a mountain and utilizing this sea water for power generation and desalting in the daytime. SOLUTION: The high-pressure pump 5 is driven by utilizing the midnight excess electric power to gather the offshore clean see water by a water intake pipe 15 and is subjected to dust removal by a dust removing machine 13 and, thereafter, the sea water is lifted to the sea water storage pond 1 on the mountain through a water feed pipe 10 and a pressure return pipe 3. At this time, the sea water is desalted by reverse osmosis in a module unit 7 and is stored in a service water tank 11. Further, the high-pressure water wheel 8 is turned by utilizing the residual pressure of the sea water concd. by this module unit 7, by which the generator 8 is driven to generate electricity. Even in the daytime, the sea water is desalted by the reverse osmosis by utilizing the sea water in the sea water storage pond 1 pumped up in the nighttime and the generator 9 is driven by utilizing the high-pressure water wheel 8 to apportion the electric power to the peak time load electric power.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は何年又は何十年に一度の
異常渇水時の水不足対策のため各地方自治体又は電力会
社等が海水揚水発電所の設備と原理を利用した、無限の
海水を飲料水として逆浸透淡水化する都市上水道の供給
方法に関するものである。
BACKGROUND OF THE INVENTION The present invention is an infinite seawater system in which each local government or electric power company utilizes the facilities and principles of a seawater pumped-storage power plant for countermeasures against water shortage during abnormal droughts once every several years or decades. The present invention relates to a method for supplying urban waterworks that reverse osmosis desalination as drinking water.

【0002】[0002]

【従来の技術】海水の逆浸透淡水化装置は近年の異常気
象による長期の渇水対策としてその都度政府自治体で建
設が検討されながら建設期間も短くて技術的にも全く問
題が無く、その水質は純水に近く飲料水として理想的で
あるにもかかわらず主として建設費の大きい事、異常渇
水時以外は設備の遊休期間が長い事、淡水化の電力原単
価が現在の上水道に比較して高い事が欠点となり採用が
見送られてきた。
2. Description of the Related Art A reverse osmosis desalination system for seawater is considered to be constructed by the local government as a measure against long-term drought due to abnormal weather in recent years, but the construction period is short and there is no technical problem. Although it is close to pure water and ideal as drinking water, the construction cost is mainly large, the equipment is idle for a long period except when there is an abnormal drought, and the unit cost of electricity for desalination is higher than the current water supply. The thing became a fault and adoption was put off.

【0003】[0003]

【発明が解決しようとする課題】本発明はこの欠点を解
決する為に海水の逆浸透淡水化装置の建設費を出来るだ
け圧縮すること。渇水時以外にも設備を常時有効に活用
出来る様な構造にして年間を通じて遊休期間を少なくす
ること。異常渇水対策としての径年貯留ダムや専用の海
水の逆浸透淡水化装置の様に長期間遊休になる恐れのあ
る設備を少なくして設備投資効率の向上を図ること。海
水揚水発電所に深夜電力の全面活用・濃縮海水の残圧の
電力回収等を有効に組み合わせて海水淡水化の造水コス
トを引き下げて、近年の上水道原水の水質悪化に伴い発
生する上水道水のカビ臭・不味さとトリハロルメタン等
の発ガン物質の発生等の改善と活性炭・薬品等の大量投
入による浄水処理コストの高騰に悩む既設上水道に代替
出来る様にすることを課題とした。
SUMMARY OF THE INVENTION In order to solve this drawback, the present invention is to reduce the construction cost of a reverse osmosis desalination apparatus for seawater as much as possible. Reduce idle periods throughout the year by creating a structure that allows the equipment to be used effectively at all times, even in times of drought. To improve capital investment efficiency by reducing equipment that may be idle for a long period of time, such as a secular storage dam as a measure against abnormal drought and a dedicated reverse osmosis desalination device for seawater. The total utilization of late-night electricity at seawater pumped-storage power plants and effective power recovery of concentrated seawater residual pressure can be effectively combined to reduce the cost of desalination for seawater desalination, and to reduce the water quality of tap water generated in recent years due to the deterioration of raw water quality. The challenge was to improve the mold odor and taste and the generation of carcinogens such as trihalomethane, and to replace the existing water supply, which suffers from a sharp rise in the cost of clean water treatment by large amounts of activated carbon and chemicals.

【0004】[0004]

【問題を解決する手段】上記課題を達成するために、本
発明は海水の逆浸透淡水化装置と海水揚水発電所の設備
を共用する事によって建設費と運転維持管理費の大半を
海水揚水発電所と分担する。従って常時は大部分の設備
を海水揚水発電所として運転し、異常渇水時にのみ海水
揚水発電所の発電に必要な海水の全部又は一部を海水の
逆浸透淡水化装置に供給することによって異常渇水時以
外の遊休設備を少なくする。更に長期の異常渇水時には
海水貯留池の海水の全量を逆浸透淡水化するために深夜
電力で昼間の淡水化に必要な海水の分まで揚水して深夜
電力を24時間活用し淡水化の電力原単価を引き下げ淡
水の供給量を増やすこともできる。
In order to achieve the above object, the present invention uses seawater reverse osmosis desalination equipment and equipment of a seawater pumped storage power plant in common so that most of the construction cost and operation and maintenance costs are seawater pumped power generation. Share with the office. Therefore, most of the equipment is operated as a seawater pumped-storage power station at all times, and all or part of the seawater required for power generation at the seawater pumped-storage power station is supplied to the seawater reverse osmosis desalination plant only during an abnormal drought. Reduce idle equipment other than time. In addition, in the case of long-term abnormal drought, in order to reverse osmosis desalination of the total amount of seawater in the seawater reservoir, the nighttime electricity is pumped up to the amount of seawater required for desalination in the daytime, and the nighttime electricity is used for 24 hours to generate the desalination power source. It is also possible to reduce the unit price and increase the supply of fresh water.

【0005】[0005]

【作用】本発明はこのように海水の逆浸透淡水化装置と
海水揚水発電所の設備とを共用する事により発電の為の
山上の海水貯留池の海水を異常渇水時には逆浸透淡水化
の原海水としてそのまま利用できる。海水揚水発電所の
設備の内、海水取水管・除塵機・送水管・高圧ポンプ・
発電機・電動機・圧力送返水管・海水貯留池・高圧水車
・排水管等大半の海水揚水発電設備を海水の逆浸透淡水
化に共用できる上に発電機でそのまま逆浸透後の濃縮海
水の残圧を電力として回収しピーク時負荷電力に充当す
る事もできる。従って常時は海水揚水発電所として運転
し異常渇水の期間のみ海水の逆浸透淡水化の追加専用設
備として、図1の実施例では砂濾過装置・圧力返水管・
逆浸透膜のモジュールユニット・上水タンク等のみで良
く、図2の実施例では更に高圧ポンプと高圧水車・電動
機と発電機の各1台及び圧力返水管を省略出来る。また
海水の逆浸透水の水質はほぼそのままで水道法水質基準
を満足していて、PH調整・硬度処理等の簡単な後処理
のみで使用出来る上にカビ臭やトリハロルメタンの様な
発ガン物質は全く含有せず活性炭投入等の高度処理が必
要ないので淡水化の電力原単価が既設の上水道の電力原
単価に近づけば全面的に上水道に使用する事もできる。
更にその建設期間も海岸に近い適当なT.P+500m
級の高さの山を利用すれば径年貯留ダム等に比較しては
るかに短期間に低コストで環境問題、水没住民対策等を
避けて建設ができる。
According to the present invention, the reverse osmosis desalination apparatus for power generation is used as a source of reverse osmosis desalination at the time of abnormal drought by sharing the seawater reverse osmosis desalination apparatus and the equipment of the seawater pumping power plant. Can be used as is as seawater. Among the facilities of the seawater pumped storage power plant, seawater intake pipe, dust remover, water pipe, high pressure pump,
Most of the seawater pumped-storage power generation equipment such as generators, electric motors, pressure transmission and return pipes, seawater reservoirs, high-pressure water turbines, and drainage pipes can be used for reverse osmosis desalination of seawater. It is also possible to recover the pressure as electric power and use it for peak load power. Therefore, it is operated as a seawater pumped-storage power plant at all times, and as a special facility for adding reverse osmosis desalination of seawater only during an abnormal drought period, in the embodiment of FIG.
Only the module unit of reverse osmosis membrane, clean water tank, etc. are required, and in the embodiment of FIG. 2, a high pressure pump, a high pressure water turbine, an electric motor, a generator, and a pressure return pipe can be omitted. In addition, the quality of reverse osmosis water of seawater is almost the same, and it satisfies the water quality standards of the Waterworks Law. It can be used only by simple post-treatment such as pH adjustment and hardness treatment, and it also causes cancer such as mold odor and trihalomethane. Since it does not contain any substances and does not require advanced treatment such as activated carbon input, it can be used for water supply entirely if the unit price of electricity for desalination approaches the unit price of electricity for existing waterworks.
Furthermore, its construction period is also a suitable T. P + 500m
If you use a high-grade mountain, you can construct it in a much shorter period of time at a lower cost and avoid environmental problems, measures against submerged residents, etc.

【0006】[0006]

【実施例】以下添付図を参照して、本発明を具体化した
実施例に付き説明する但し、以下の実施例は、本発明の
技術的範囲を限定する性格のものではない。ここに、図
1、は本発明の一実施例に係る海水揚水発電所と設備を
共用した海水の逆浸透淡水化装置のフローシートを示
す。図1において矢印→は海水又は淡水の流れの方向を
示し、矢印←→は流れが往復することを示すがこれをフ
ローシートで流れの順に説明すると、異常渇水時に本発
明の海水の逆浸透淡水化装置の運転には、先ず海岸に近
いT.P+500m級の山頂に設置されている海水貯留
池(1)に海水を揚水するがその量は仮に福岡市程度の
都市の上水道の一日の基準水量を46万トンとして、そ
の10%(平均的な都市の夜間給水量で夜間断水を回避
出来る)を供給する場合、海水の逆浸透膜の透過回収率
を40%とすれば(46万トン×0.1/0.4)約1
2万トンの海水量が必要になり海水貯留池(1)の規模
を仮に数字で表せば長さ100m×幅60m×深さ20
m程度となる、もし逆浸透淡水化装置を昼夜フル稼働す
る場合は常に揚水しつつ逆浸透淡水化するので大きさは
半分の長さ60m×幅50m×深さ20mの6万トン程
度でも充分である。この海水は昼間に山頂の砂濾過装置
(2)で濾過後に圧力返水管(4)で圧送流下され、山
麓の逆浸透膜のモジュールユニット(7)で海水の40
%は逆浸透淡水化されて上水タンク(11)に貯留さ
れ、モジュールユニット(7)で60%に濃縮された海
水の残圧は高圧水車(8)に直結されている発電機
(9)を駆動し発電されて昼間のピーク時負荷電力に充
当されるが、この場合でも逆浸透淡水化に使用された海
水の約60%は発電出来る、次に高圧水車(8)で残圧
を回収された濃縮海水は大気圧まで減圧されて最終的に
排水管(12)より近海(14)に放流拡散される。夜
間に海水貯留池(1)に海水を揚水するには近海(1
4)の沖合いの清澄な海水を取水管(15)で集めて除
塵機(13)で除塵し、送水管(10)で高圧ポンプ
(5)に供給し電動機(6)を深夜電力で運転して圧力
送返水管(3)から海水貯留池(1)に揚水される。こ
の様にして異常渇水期間を乗り切ればその後、この設備
は通常の海水揚水発電所として夜間の余剰電力を利用し
て海水を海水貯留池(1)に揚水し昼間のピーク電力に
備えて海水の全量を発電に使用することが出来る。上記
の様に本設備を異常渇水時以外に通常の海水揚水発電所
として運転する場合は海水の逆浸透淡水化の専用設備で
ある砂濾過装置(2)圧力返水管(4)モジュールユニ
ット(7)上水タンク(11)を各付属バルブで遮断休
止させて、夜の間に深夜電力で電動機(6)を駆動して
高圧ポンプ(5)を使って海水を海水貯留池(1)に揚
水し貯留しておく。昼間はこの海水を圧力送返水管
(3)から夜間とは逆に流下して高圧水車(8)で発電
機(9)を駆動して発電し、昼間のピーク時負荷電力を
補充する。以上の実施例は既設の地元電力会社の所有す
る海水揚水発電所に海水の逆浸透淡水化装置を付随させ
て置き、何年に一回の異常渇水時のみ海水揚水発電所の
能力の一部又は全部を各自治体の水道局が借用して海水
の逆浸透淡水化装置を運転する方法であって、その場合
は昼間ピーク時負荷電力の発電量は通常の60%となる
ので40%の電力不足分は他府県の電力会社より送電線
を使って補給を受ける必要がある。図2のフローシート
の実施例は更に本発明の構造を簡単にし、建設費を圧縮
するために図1の実施例における圧力返水管(4)を省
略し、高圧ポンプ(5)と電動機(6)及び高圧水車
(8)と発電機(9)の2組を図2の発電電動機(1
6)と高圧ポンプ水車(17)の1組で兼用したもので
あって、専用の海水逆浸透淡水化装置が非常に簡単にな
り、僅かに高圧砂濾過装置(18)とモジュールユニッ
ト(7)と上水タンク(11)のみとなる。その外に図
1の実施例と異なる点は圧力返水管(4)を省略した代
わりに使用する圧力送返水管(3)の内部と原海水との
汚れを除去するための高圧砂濾過装置(18)を山頂か
ら山麓のモジュールユニット(7)の直前に持ってきた
ため約50kg/cmの耐圧構造となる事、ポンプと
水車とを兼用した高圧ポンプ水車(17)では、海水の
揚水と発電が同時に行えないため図1実施例の24時間
淡水化運転が出来ない事であるが、図2の実施例のもう
一つの特徴は海水揚水発電所に海水の逆浸透淡水化装置
を組み込む場合に圧力送返水管(3)にバイパス管を一
本取るだけで良いために既設の海水揚水発電所を改造す
る場合でも、新設の海水揚水発電所に併設する場合でも
海水揚水発電所の機能と構造を損なうこと無く容易に建
設が出来て、海水逆浸透淡水化装置の運転も簡単になる
事である。但し、設備の運転維持管理の主体を電力会社
か水道局にするかの判断は自治体にあるが、装置の大部
分が海水揚水発電設備であり、海水の逆浸透淡水化装置
として運転するのは何年に一度しか機会が無い実情から
すれば逆浸透淡水化の専用設備部分は水道局で設備投資
して運転維持管理は電力会社に民間委託契約の形をとる
のも一案であり、今後更に上水道原水の水質悪化と浄水
処理コストの高騰が続けば、電力会社が単独で海水の逆
浸透淡水化専用の海水揚水発電所を建設して自社の深夜
余剰電力を利用した低コストで良質の水を水道局に販売
する事もできるが、電力会社と地方自治体との第三セク
ターで海水の揚水発電所兼逆浸透淡水化設備として建設
・運営する方法もある。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a block diagram showing the configuration of an embodiment of the present invention; FIG. 1 shows a flow sheet of a seawater reverse osmosis desalination apparatus that shares equipment with a seawater pumped storage power plant according to an embodiment of the present invention. In FIG. 1, the arrow → indicates the direction of the flow of seawater or fresh water, and the arrow ← → indicates that the flow reciprocates. This will be explained in the order of flow with a flow sheet. For the operation of the rectifying device, first of all, T. Seawater is pumped up to the seawater storage pond (1) installed on the summit of P + 500m class, but the amount of water is assumed to be 460,000 tons per day, which is 10% (average). In the case of supplying water to a city that can prevent nighttime water outages), if the permeation recovery rate of the seawater reverse osmosis membrane is 40% (460,000 tons x 0.1 / 0.4), approximately 1
20,000 tons of seawater is required, and if the scale of the seawater reservoir (1) is expressed numerically, length 100m x width 60m x depth 20
If the reverse osmosis desalination system is fully operated day and night, it will always be pumped and reverse osmosis desalinated, so half the size will be 60m x width 50m x depth 20m, about 60,000 tons is sufficient. Is. This seawater is filtered by a sand filter (2) at the summit in the daytime, and then pressure-fed by a pressure return pipe (4), and 40 times of seawater is fed by a module unit (7) of the reverse osmosis membrane at the foot of the mountain.
% Of the water is reverse osmosis desalinated and stored in the clean water tank (11), and the residual pressure of seawater concentrated to 60% in the module unit (7) is directly connected to the high-pressure turbine (8). Is used to generate peak daytime load power, but even in this case approximately 60% of the seawater used for reverse osmosis desalination can be generated, and then the residual pressure is recovered by the high pressure turbine (8). The concentrated seawater thus obtained is depressurized to atmospheric pressure and finally discharged and diffused from the drain pipe (12) to the near sea (14). To pump seawater into the seawater reservoir (1) at night (1)
The clear offshore seawater of 4) is collected by the water pipe (15) and removed by the dust remover (13) and supplied to the high pressure pump (5) by the water delivery pipe (10) to operate the electric motor (6) at midnight power. Water is pumped from the pressure return pipe (3) to the seawater reservoir (1). If the abnormal drought period is overcome in this way, then this equipment will use the surplus power at night as a normal seawater pumped-storage power plant to pump seawater to the seawater reservoir (1) to prepare for peak power during the daytime. All can be used for power generation. As described above, when this equipment is operated as a normal seawater pumped-storage power station except when there is an abnormal drought, it is a dedicated equipment for reverse osmosis desalination of seawater. Sand filter (2) Pressure return pipe (4) Module unit (7 ) The tap water tank (11) is shut off by each attached valve, and the electric motor (6) is driven by midnight power during the night to pump seawater into the seawater reservoir (1) using the high-pressure pump (5). And store. In the daytime, this seawater flows down from the pressure transmission / return water pipe (3) in the opposite direction of the nighttime, and the high-pressure turbine (8) drives the generator (9) to generate electric power to replenish the peak daytime load power. In the above example, the seawater pumped-storage power plant owned by the existing local electric power company is attached with a reverse osmosis desalination device for seawater, and only a part of the capacity of the seawater pumped-storage power plant is observed only once during an abnormal drought. Or it is a method of operating the reverse osmosis desalination equipment of seawater by borrowing the whole waterworks of each municipality. In that case, the amount of power generated during the daytime peak load is 60% of the normal power, so 40% of the power is consumed. The shortage must be replenished by electric power companies in other prefectures using power lines. The flow sheet embodiment of FIG. 2 further simplifies the structure of the present invention and omits the pressure return pipe (4) in the embodiment of FIG. 1 to reduce the construction cost, the high pressure pump (5) and the electric motor (6). ) And a high-pressure water turbine (8) and a generator (9) as shown in FIG.
6) and a high-pressure pump turbine (17) are combined, and a dedicated seawater reverse osmosis desalination device is very simple, and a high-pressure sand filter device (18) and a module unit (7) are slightly used. And only the water tank (11). In addition, the point different from the embodiment of FIG. 1 is that a high pressure sand filter for removing dirt from the inside of the pressure water return pipe (3) used instead of omitting the pressure water return pipe (4) and raw seawater ( 18) was brought from the summit to just before the module unit (7) at the foot of the mountain, so it had a pressure-resistant structure of about 50 kg / cm 2 , and in the high-pressure pump turbine (17) that doubles as a pump and turbine, seawater is pumped and power is generated. However, the 24-hour desalination operation of the embodiment of FIG. 1 cannot be performed at the same time, but another feature of the embodiment of FIG. 2 is that when the seawater reverse osmosis desalination device is incorporated in the seawater pumped-storage power plant. The function and structure of the seawater pumped-storage power plant, whether the existing seawater-pumped-storage power plant is remodeled or attached to the new seawater-pumped power plant because only one bypass pipe is required for the pressure water return pipe (3). Construction is easy without damaging Now, the operation of the seawater reverse osmosis desalination system will be simplified. However, while it is up to the local government to decide whether the main body of operation and maintenance of equipment is the electric power company or the water department, most of the equipment is seawater pumped-storage power generation equipment, and it is not possible to operate it as a reverse osmosis desalination equipment for seawater. In view of the fact that there is only one opportunity every year, it is a good idea to invest the equipment dedicated to reverse osmosis desalination at the Waterworks Bureau, and to operate and maintain it in the form of a private contract with an electric power company. Furthermore, if the water quality of the water supply deteriorates and the cost of clean water treatment continues to rise, the power company will independently build a seawater pumped-storage power plant dedicated to reverse osmosis desalination of seawater, and will use its own late-night surplus electricity to provide good quality at low cost. Water can be sold to the water department, but there is also a method of constructing and operating as a seawater pumped-storage power station and reverse osmosis desalination facility in a third sector between the electric power company and the local government.

【0007】[0007]

【発明の効果】本発明は上記したように山上の海水貯留
池よりの高落差水圧を利用した海水の逆浸透淡水化設備
と海水揚水発電所の設備を共用する事によって建設費の
大半を海水揚水発電所と分担共有して節減する効果があ
る。何年に一回かの異常渇水時にのみ海水揚水発電所の
発電の為に揚水した山上の海水貯留池の海水の全部又は
一部を逆浸透淡水化装置で淡水化する様にすれば、常時
は本来の設備を海水揚水発電所として運転出来るので設
備の大部分を有効に活用して遊休期間を少なくする効果
もある。異常渇水時に逆浸透淡水化設備で海水の一部ま
たは全部を淡水化する時その期間の発電能力の40%の
不足は他府県の電力会社から送電線を通じた援助が可能
であって、水道管等による隣接他府県水道局からの直接
の送水援助が受けられない場合でも結果的には遠隔地よ
り送電線で送水を受けるのと同じ効果がある。図1の実
施例の様に長期の異常渇水時に海水貯留池の海水の全量
を逆浸透淡水化する時には夜間電力で昼間に淡水化に必
要な充分な量の海水を揚水しておけば夜間電力を24時
間利用したと同じ事になり全電力を深夜電力単価で運転
出来る効果があり、昼間ピーク時の午後1時〜午後4時
の3時間に限れば後の21時間で造水することにより発
電と造水を両立させる事も可能である。図2の実施例で
は高圧ポンプと高圧水車が1台で兼用出来るのと、現地
工事費の嵩む山頂から落差500mの水圧管路も圧力返
水管を省略して圧力送返水管1本に出来るので建設費と
建設期間を大幅に圧縮出来る効果がある。近年の上水道
原水の水質悪化の対策として上水道浄水時に使用する脱
臭用粉末活性炭の投入等浄水処理費用の高騰に対しても
本発明により海水の逆浸透淡水化の電力原単価が大幅に
引き下げられれば、海水の逆浸透水の水質はそのままで
も充分水道法水質基準に近いため僅かな後処理のみで、
粉末活性炭による脱臭処理が不要でしかも塩素の注入も
微量で良い為に将来は塩素の過剰注入によって発生する
上水道水の発ガン性物質トリハロメタン混入防止対策と
しても海水の逆浸透水が上水道水に代替出来る効果の可
能性もある。異常渇水時に常にもう一つの対策として検
討されている径年貯留ダム構想も巨額の建設費を要する
と共に環境破壊や水没地域住民対策等に問題が多くて建
設に長期間を要し更に異常渇水の無い時は完全な遊休設
備となる為に本発明の方が全ての面で投資効率の良くな
る効果がある。実際の建設と運営に当たっては第3セク
ター方式で電力会社と自治体が共同出資で海水の逆浸透
装置を共用した海水揚水発電所を建設して運営すれば、
常時はピーク時負荷電力を電力会社に販売し、異常渇水
時にのみ淡水を生産して自治体の上水道に販売出来る効
果もある。
As described above, according to the present invention, most of the construction cost can be reduced by using the reverse osmosis desalination facility for seawater utilizing the high head water pressure from the seawater reservoir on the mountain and the facility of the seawater pumped storage power plant. It has the effect of sharing the share with the pumped storage power plant to save energy. If the reverse osmosis desalination device desalinates all or part of the seawater in the mountaintop seawater storage pond that was pumped up for power generation at the seawater pumped-storage power plant, only when there is an abnormal drought once every several years. Since the original equipment can be operated as a seawater pumped-storage power plant, most of the equipment can be effectively used to reduce idle periods. When a part or all of seawater is desalinated by reverse osmosis desalination equipment during abnormal drought, the lack of 40% of the power generation capacity during that period can be assisted by electric power companies in other prefectures through transmission lines, such as water pipes. Even if the direct water supply assistance from other neighboring prefecture waterworks is not received, the result is the same as receiving water from a remote place through a transmission line. When reverse osmosis desalination of the entire amount of seawater in a seawater storage pond is carried out during a long-term abnormal drought as in the embodiment of Fig. 1, nighttime electricity can be obtained by pumping a sufficient amount of seawater necessary for desalination in the daytime. It is the same as using 24 hours a day, and there is an effect that all electricity can be operated at the unit price of midnight power, and if it is limited to 3 hours from 1:00 pm to 4:00 pm at the peak of daytime, by creating water in the next 21 hours It is also possible to combine power generation and desalination. In the embodiment shown in FIG. 2, the high pressure pump and the high pressure water turbine can be used as one unit, and the pressure return pipe can be omitted from the summit where the construction cost is high and the head is 500 m. It has the effect of significantly reducing the construction cost and construction period. As a measure against the deterioration of the quality of raw water in recent years, if the present invention can significantly reduce the unit price of electricity for reverse osmosis desalination of seawater, even if the cost of water purification treatment such as the input of deodorizing powdered activated carbon used during water purification is high. , The quality of seawater reverse osmosis water is sufficiently close to the water quality standard of the Waterworks Law, so only a small amount of post-treatment is required.
Reverse osmosis water of seawater is replaced with tap water as a measure to prevent contamination of the tap water carcinogen trihalomethane, which is generated in the future with excessive chlorine injection, because deodorization treatment with powdered activated carbon is not required and chlorine injection is small. There is also the possibility of an effect that can be achieved. The concept of a long-term storage dam, which is always considered as another measure during abnormal drought, also requires huge construction costs, and there are many problems such as environmental destruction and measures to protect residents in submerged areas. When it is not present, the present invention has the effect of improving the investment efficiency in all aspects because it becomes a completely idle facility. In the actual construction and operation, if the electric power company and the local government jointly invest in the construction and operation of the seawater pumped storage power plant that shares the seawater reverse osmosis equipment,
There is also an effect that the peak load power can be sold to the electric power company at all times, and fresh water can be produced only when there is an abnormal drought and sold to the municipal water supply.

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

【図1】海水逆浸透装置の高圧ポンプと高圧水車を別々
にした実施例のフローチャート
FIG. 1 is a flowchart of an embodiment in which a high-pressure pump and a high-pressure turbine of a seawater reverse osmosis device are separately provided.

【図2】海水逆浸透装置に高圧ポンプ水車を使用した実
施例のフローチャート
FIG. 2 is a flowchart of an example in which a high-pressure pump turbine is used in a seawater reverse osmosis device.

【符号の説明】[Explanation of symbols]

(1)海水貯留池 (2)砂濾過装置 (3)圧力送返水管 (4)圧力返水管 (5)高圧ポンプ (6)電動機 (7)モジュールユニット (8)高圧水車 (9)発電機 (10)送水管 (11)上水タンク (12)排水管 (13)除塵機 (14)近海 (15)取水管 (16)発電電動機 (17)高圧ポンプ水車 (18)高圧砂濾過装置 (1) Seawater reservoir (2) Sand filter (3) Pressure water return pipe (4) Pressure water return pipe (5) High pressure pump (6) Electric motor (7) Module unit (8) High pressure water turbine (9) Generator ( 10) Water pipe (11) Water tank (12) Drain pipe (13) Dust remover (14) Near sea (15) Water intake pipe (16) Generator motor (17) High-pressure pump turbine (18) High-pressure sand filter

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 深夜余剰電力を利用して高圧ポンプで海
水を逆浸透淡水化すると共に濃縮海水の残圧を高圧水車
と発電機で電力として回収しつつ同時に山上の海水貯留
池にも揚水し、昼間にはその海水貯留池の海水を高落差
水圧で逆浸透淡水化すると共に濃縮海水の残圧を高圧水
車と発電機で電力として回収することによって深夜余剰
電力を24時間利用する方法。
1. A midnight surplus power is used to reverse osmosis desalinate seawater with a high-pressure pump, and the residual pressure of concentrated seawater is recovered as electric power with a high-pressure turbine and a generator, and at the same time pumped to a seawater reservoir on a mountain. In the daytime, the seawater in the seawater storage pond is reverse osmosis desalinated at a high head water pressure, and the residual pressure of concentrated seawater is recovered as electric power by a high-pressure turbine and a generator to use the late night surplus power for 24 hours.
【請求項2】 山上の海水貯留池に発電電動機直結の高
圧ポンプ水車で海水を揚水し、その高落差水圧で海水を
逆浸透淡水化すると共に濃縮海水の残圧を同じ高圧ポン
プ水車で発電電動機を駆動して電力を回収する方法。
2. A high-pressure pump turbine to which seawater is pumped to a seawater reservoir on a mountain by a high-pressure pump turbine directly connected to the generator-motor, the seawater is reverse osmosis desalinated by the high head water pressure, and the residual pressure of concentrated seawater is generated by the same high-pressure pump turbine. Method to drive electricity to recover electric power.
【請求項3】 異常渇水時には設備を海水の逆浸透淡水
化装置として運転し、他の時期には通常の海水揚水発電
所として運転出来る様に海水揚水発電所と設備を共用し
た海水の逆浸透淡水化方法。
3. The reverse osmosis of seawater shared with the seawater pumped-storage power plant so that the equipment can be operated as a reverse osmosis desalination device during abnormal drought, and can be operated as a normal seawater pumped-storage power plant at other times. Desalination method.
JP7271684A 1995-09-12 1995-09-12 Reverse osmosis desalting method for sea water making common use of sea water pumping up power plant and equipment Pending JPH0975935A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7271684A JPH0975935A (en) 1995-09-12 1995-09-12 Reverse osmosis desalting method for sea water making common use of sea water pumping up power plant and equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7271684A JPH0975935A (en) 1995-09-12 1995-09-12 Reverse osmosis desalting method for sea water making common use of sea water pumping up power plant and equipment

Publications (1)

Publication Number Publication Date
JPH0975935A true JPH0975935A (en) 1997-03-25

Family

ID=17503425

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7271684A Pending JPH0975935A (en) 1995-09-12 1995-09-12 Reverse osmosis desalting method for sea water making common use of sea water pumping up power plant and equipment

Country Status (1)

Country Link
JP (1) JPH0975935A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003145149A (en) * 2001-11-14 2003-05-20 Nkk Corp Water cleaning facility
EP1755772A1 (en) * 2004-04-30 2007-02-28 Brian Douglas Parkinson Static head reverse osmosis
JP2007144354A (en) * 2005-11-30 2007-06-14 Takashi Matsuda Apparatus for operating reverse osmosis membrane without using power
JP2014069092A (en) * 2012-09-27 2014-04-21 Sharp Corp Desalination plant
KR101505620B1 (en) * 2011-11-30 2015-03-30 지에스건설 주식회사 Reverse osmosis desalination system coupled with real time electric power price and method for operating the same
JP2020195950A (en) * 2019-05-31 2020-12-10 オルガノ株式会社 Membrane filtration system, operation method of membrane filtration system, and electricity supply device and electricity supply method for membrane filtration system

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003145149A (en) * 2001-11-14 2003-05-20 Nkk Corp Water cleaning facility
EP1755772A1 (en) * 2004-04-30 2007-02-28 Brian Douglas Parkinson Static head reverse osmosis
EP1755772A4 (en) * 2004-04-30 2007-07-18 Brian Douglas Parkinson Static head reverse osmosis
JP2007144354A (en) * 2005-11-30 2007-06-14 Takashi Matsuda Apparatus for operating reverse osmosis membrane without using power
KR101505620B1 (en) * 2011-11-30 2015-03-30 지에스건설 주식회사 Reverse osmosis desalination system coupled with real time electric power price and method for operating the same
JP2014069092A (en) * 2012-09-27 2014-04-21 Sharp Corp Desalination plant
JP2020195950A (en) * 2019-05-31 2020-12-10 オルガノ株式会社 Membrane filtration system, operation method of membrane filtration system, and electricity supply device and electricity supply method for membrane filtration system

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