JPH0957259A - Sea water desalting device and method for using this device - Google Patents

Sea water desalting device and method for using this device

Info

Publication number
JPH0957259A
JPH0957259A JP7234618A JP23461895A JPH0957259A JP H0957259 A JPH0957259 A JP H0957259A JP 7234618 A JP7234618 A JP 7234618A JP 23461895 A JP23461895 A JP 23461895A JP H0957259 A JPH0957259 A JP H0957259A
Authority
JP
Japan
Prior art keywords
reverse osmosis
osmosis membrane
seawater
fresh water
water tank
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
JP7234618A
Other languages
Japanese (ja)
Inventor
Hirosuke Kawaguchi
宏祐 川口
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.)
Maruyama Manufacturing Co Ltd
Original Assignee
Maruyama 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 Maruyama Manufacturing Co Ltd filed Critical Maruyama Manufacturing Co Ltd
Priority to JP7234618A priority Critical patent/JPH0957259A/en
Publication of JPH0957259A publication Critical patent/JPH0957259A/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

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PROBLEM TO BE SOLVED: To make it possible to provide the subject device with both functions of a small-sized sea water desalting device to be used in fishing boats and culture farms for fish and shellfishes and a washing machine using sea water or fresh water. SOLUTION: This sea water desalting device is constituted by connecting, successively from a sea water side, a strainer 8, a prefilter 12, a bypass circuit C installed selectively in juxtaposition with this prefilter 12, a liquid feeder A, a reverse osmosis membrane section B, a fresh water tank 54 communicated selectively therewith and a potable water tank 25 interposed with a filter 23. While a washing section D is disposed selectively communicatably between the liquid feeder A and the reverse osmosis membrane section B, the washing section D is communicated connectably and disconnectably with and from the condensed water under the pressurization of the reverse osmosis membrane section B. The fresh water tank 54 is made connectable and disconnectable selectively with and from the suction side of the liquid feeder A. Various kinds of the use methods by selection of the respective constituting parts are thus made possible.

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】漁船や魚介類の養殖場で用い
る小型の海水淡水化装置と、海水や、清水を使つた洗浄
機の機能を兼用することを可能にした海水淡水化兼洗浄
装置とこの装置の使用方法に関する。
TECHNICAL FIELD The present invention relates to a small seawater desalination apparatus used in a fishing boat or a seafood farm, and a seawater desalination / washing apparatus capable of serving as a washing machine using seawater or fresh water. A method of using this device.

【0002】[0002]

【従来の技術】漁場や魚介類の養殖場などの施設では海
水や清水による漁船や漁網などの器具や魚介類の洗浄や
飲料水が必要となる。特に上水道の設備のない場所での
作業では、清水や飲料水はタンクなどに貯留して運搬、
供給しなければならないため、小型の海水淡水化装置が
利用されている。一方、これらの施設には、海水や、清
水による洗浄機も多く普及している。
2. Description of the Related Art In facilities such as fishing grounds and seafood farms, it is necessary to wash equipment such as fishing boats and fishing nets, seafood and drinking water with seawater or fresh water. Especially when working in places without water supply facilities, fresh water and drinking water are stored in tanks and transported,
A small seawater desalination plant is used because it must be supplied. On the other hand, in these facilities, many washing machines using sea water or fresh water are widely used.

【0003】例えば図3はモ−タ、エンジン等の原動機
駆動による従来技術による小型簡易海水淡水化装置であ
つて、これは逆浸透膜法による造水装置で、もつぱら飲
料水、生活用水の造水に用いられているものであり、図
において原動機としてのエンジン1を始動し、ケ−ブル
2を介して、スロツトルレバ−3で所定の回転数にした
後、クラツチ4の操作により、前記エンジン1の動力を
伝動部材5を介して供給ポンプ6に伝達すると、この供
給ポンプ6が駆動されることにより、海水7はストレ−
ナ8を通り給水管9から吸い込まれ、供給管10に吐出
される。
For example, FIG. 3 shows a small and simple seawater desalination apparatus according to the prior art, which is driven by a motor such as a motor and an engine. It is used for fresh water, and in the figure, an engine 1 as a prime mover is started, and after a predetermined number of rotations is made by a throttle lever 3 through a cable 2, the engine is operated by operating a clutch 4. When the power of No. 1 is transmitted to the supply pump 6 via the transmission member 5, the supply pump 6 is driven, so that the seawater 7 is strayed.
It is sucked from the water supply pipe 9 through the nozzle 8 and discharged to the supply pipe 10.

【0004】圧力計11が介設される前記供給管10の
通路には、プレフイルタ12が装置されており、海水に
混入している微細な異物が濾過され、圧送ポンプ13に
供給される状態になつたところで、前記圧送ポンプ13
には、クラツチ14の操作により、エンジン1の動力が
伝動部材15を介して伝達される。
A prefilter 12 is installed in the passage of the supply pipe 10 in which a pressure gauge 11 is interposed, and fine foreign matter mixed in seawater is filtered and supplied to a pressure pump 13. The pressure pump 13
When the clutch 14 is operated, the power of the engine 1 is transmitted to the engine 1 through the transmission member 15.

【0005】前記圧送ポンプ13は、前述の供給された
海水を吸い込んで吐出し、アキユムレ−タ16により脈
動を低減され、圧送管17を通り、逆浸透膜18に導入
される。導出管19には絞り弁20Aが設けられてお
り、逆浸透膜18に導入される海水の圧力が所定の逆浸
透圧力になるように、圧力計21を見て絞り弁20Aを
調節すると、導出管22からは透過水が、導出管19か
らは濃縮水が得られる。
The pressure-feeding pump 13 sucks in and discharges the supplied seawater, the pulsation is reduced by the accumulator 16, and the seawater is introduced into the reverse osmosis membrane 18 through the pressure-feeding pipe 17. The outlet pipe 19 is provided with a throttle valve 20A. When the throttle valve 20A is adjusted by looking at the pressure gauge 21 so that the pressure of seawater introduced into the reverse osmosis membrane 18 becomes a predetermined reverse osmosis pressure, Permeate water is obtained from the pipe 22 and concentrated water is obtained from the outlet pipe 19.

【0006】前記透過水は更に活性炭濾過器のような濾
過器23により、カルキや臭みが吸着除去され、導出管
24から飲料水タンク25に飲料水26として貯留さ
れ、コツク27から適時使用に供される。
[0006] The permeated water is further adsorbed and removed of chlorine and odor by a filter 23 such as an activated carbon filter, stored as drinking water 26 in a drinking water tank 25 from a discharge pipe 24, and used from a cock 27 for timely use. To be done.

【0007】一方、濃縮水は絞り弁20Aを通り、バイ
パスホ−ス28から排出放流される。リリ−フ弁29は
前記逆透過膜18を保護するためのもので、導入される
海水の圧力が所定の圧力以上になると、前記リリ−フ弁
29が開き、バイパスホ−ス28へ圧力水を放出するよ
うになつている。
On the other hand, the concentrated water passes through the throttle valve 20A and is discharged and discharged from the bypass hose 28. The relief valve 29 is for protecting the reverse permeable membrane 18, and when the pressure of the introduced seawater becomes equal to or higher than a predetermined pressure, the relief valve 29 opens and the pressure water is supplied to the bypass hose 28. It is designed to release.

【0008】次に図4は、海水又は清水を使用した従来
の洗浄機の一例を示すもので、魚介類の養殖場の網の洗
浄や、漁船、漁場施設の各種洗浄に使用されているもの
である。この図において前記図3におけると同一又は同
等な部分には同一の符号を付するものとする。
[0008] Next, Fig. 4 shows an example of a conventional washing machine using sea water or fresh water, which is used for washing nets in a seafood farm and various washing of fishing boats and fishing ground facilities. Is. In this figure, the same or equivalent parts as in FIG. 3 are designated by the same reference numerals.

【0009】ケ−ブル2を介してスロツトルレバ−3で
所定の回動数に調節したエンジン1の動力を、伝動部材
15によつて圧送ポンプ13が駆動されると、海水7は
ストレ−ナ8を通り、吸水ホ−ス30から吸い込まれ
て、圧送管17に吐出され、延長高圧ホ−ス31から洗
浄ノズル32に導かれ、被洗浄物に向けて高圧の海水を
噴射し、網やかごなどの付着物を洗浄する。この際、噴
射圧力の調節は調圧弁33で行ない、余水は余水管34
を介して液源である海水7中に放出する。
When the pressure-feed pump 13 is driven by the transmission member 15, the power of the engine 1 adjusted to a predetermined number of revolutions by the slot lever 3 through the cable 2 is driven by the transmission member 15, and the seawater 7 becomes strainer 8. Through the water suction hose 30, discharged to the pressure feed pipe 17, guided from the extended high pressure hose 31 to the cleaning nozzle 32, jetting high-pressure seawater toward the object to be cleaned, mesh and basket. Clean the deposits. At this time, the injection pressure is adjusted by the pressure regulating valve 33, and the spillage is collected by the spillage pipe 34.
It is released into the seawater 7 which is the liquid source via the.

【0010】清水によつて洗浄作業を行なう場合は、水
道の蛇口35から延長ホ−ス36によつて、洗浄装置の
近傍に設置した清水タンク37に清水38を貯留し、こ
の清水タンク37中に、前記ストレ−ナ8、吸水ホ−ス
30、余水ホ−ス34を入れて、圧送ポンプ13で吸い
込み、延長高圧ホ−ス31から洗浄ノズル32に導き、
高圧の清水を噴射して洗浄作業を行なうのである。
When the cleaning operation is performed with fresh water, the fresh water 38 is stored in a fresh water tank 37 installed in the vicinity of the cleaning device by the extension hose 36 from the tap 35 of the water supply. , The strainer 8, the water-absorbing hose 30, and the spill-water hose 34 are put in and sucked by the pressure pump 13, and guided from the extended high-pressure hose 31 to the cleaning nozzle 32.
The cleaning work is performed by injecting high-pressure fresh water.

【0011】[0011]

【発明が解決しようとする課題】図3に示すような小型
簡易海水淡水化装置は、漁船や、上水道が設置されてい
ない離島、渇水地域に導入されており、また海水や、清
水を用いる図4に示すような洗浄機も、魚介類の養殖場
や、漁業施設に導入されており、それぞれ別々に購入さ
れ、使用されている。すなわちそれぞれの装置は共用で
きる部分が多くあるにも拘らず、専用機となつているの
で、両方の用途を必要とするユ−ザにとつては上記2つ
の装置を購入することになり、経済的負担が大きくなる
という欠点、問題点がある。
A small and simple seawater desalination apparatus as shown in FIG. 3 has been introduced into fishing boats, remote islands where water supply is not installed, drought areas, and seawater or fresh water. The washing machine as shown in 4 is also installed in a seafood farm and a fishery facility, and is purchased and used separately. That is, although each device has many parts that can be shared, since it is a dedicated machine, a user who needs both uses will purchase the above two devices, which is economical. There is a drawback and a problem that the physical burden becomes large.

【0012】[0012]

【課題を解決するための手段】ここにおいてこの発明
は、海水淡水化装置と洗浄機とが、送液用のポンプ、原
動機、配管などの主な構成要素、部材が共用可能である
ことに着目して、海水からの逆浸透膜を介して飲料水を
造水するように、海水側から順に、ストレ−ナ(8)と、
プレフイルタ(12)と、このプレフイルタ(12)に選択的に
並設される迂回路(C)と、送液装置(A)と、逆浸透膜部
(B)とこれに選択的に連通される清水タンク(54)と濾過
器(23)を介装された飲料水タンク(25)とを連結される海
水淡水化装置であつて、前記送液装置(A)と前記逆浸透
膜部(B)との間には洗浄部(D)が選択的に連通可能とされ
る一方、前記洗浄部(D)は前記逆浸透膜部(B)の加圧下の
濃縮水に断接可能に連通され、前記清水タンク(54)は前
記送液装置(A)の吸入側に選択的に断接可能とされてい
る海水淡水化装置を提案し、これによつて、上記各構成
部分の選択使用により、海水からの飲料水、洗浄用清水
の造水、これら飲料水や洗浄用清水の造水下における濃
縮水による洗浄作業、海水による洗浄作業、清水による
洗浄作業に使用可能とするものである。
In the present invention, attention is paid to the fact that the seawater desalination apparatus and the washing machine can share main constituent elements and members such as a pump for feeding liquid, a prime mover, and piping. Then, so as to create drinking water from the seawater through the reverse osmosis membrane, in order from the seawater side, the strainer (8),
Prefilter (12), detour (C) selectively installed in parallel with this prefilter (12), liquid transfer device (A), reverse osmosis membrane section
(B) and a fresh water tank (54) selectively connected to this and a drinking water tank (25) having a filter (23) interposed therein, which is a seawater desalination apparatus, wherein the liquid transfer A washing unit (D) can be selectively communicated between the device (A) and the reverse osmosis membrane unit (B), while the washing unit (D) is a unit of the reverse osmosis membrane unit (B). Proposed is a seawater desalination apparatus, which is connected to the concentrated water under pressure so as to be connectable and disconnectable, and the fresh water tank (54) is selectively connectable and disconnectable to the suction side of the liquid transfer device (A). Therefore, by selectively using each of the above-mentioned constituent parts, drinking water from seawater, fresh water for washing, washing work with concentrated water under the fresh water of these drinking water and fresh water for washing, washing work with seawater, fresh water It can be used for cleaning work.

【0013】[0013]

【発明の実施の形態】この発明の海水淡水化装置を図式
的に表わしたのが図1であつて、この図において、構成
要素の一部を前記図3又は図4に示したのと同等又は同
一の部分には同じ符号を付して説明すると、海水7から
ストレ−ナ8、吸入管9、プレフイルタ12を送液装置
A、逆浸透膜部B、濾過器23を経て飲料水タンク25
に至る系統と、前記ストレ−ナ8からプレフイルタ12
を通らずに送液装置Aに至る迂回路Cと、前記送液装置
Aと逆浸透膜部Bとの間から分岐して選択的に洗浄部D
に至る回路Eと、逆浸透膜部Bの加圧下の濃縮水を海水
7に戻す回路Fから前記洗浄部Dに選択的に分岐される
回路Gと、前記逆浸透膜部Bと濾過器23との間から選
択的に分岐されて構成される清水タンク54と、この清
水タンク54から前記送液装置Aの流入側に選択的に接
続される回路Hとが存在する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A seawater desalination apparatus of the present invention is schematically shown in FIG. 1, in which some of the components are equivalent to those shown in FIG. 3 or FIG. Or, the same parts will be denoted by the same reference numerals. To describe, the seawater 7 is passed through the strainer 8, the suction pipe 9, and the prefilter 12 through the liquid delivery device A, the reverse osmosis membrane part B, and the filter 23, and the drinking water tank 25.
From the strainer 8 to the prefilter 12
A bypass C leading to the liquid delivery device A without passing through the liquid delivery device A and a branch between the liquid delivery device A and the reverse osmosis membrane part B to selectively select a cleaning part D.
To the washing section D from the circuit E for returning the concentrated water under pressure of the reverse osmosis membrane section B to the seawater 7, the reverse osmosis membrane section B and the filter 23. And a circuit H selectively connected to the inflow side of the liquid delivery apparatus A from the fresh water tank 54.

【0014】次に前記図1において図式的に表わしたこ
の発明の装置の構成を、より具体的に表現した図2にお
いても、図1におけると同様に、前記図3、図4に示し
た従来例と同等又は同一の部分には同一の符号を付して
説明をするものとする。図2において、原動機としての
エンジン1を始動し、ケ−ブル2を介して、スロツトル
レバ−3で所定の回転数にした後、クラツチ4の操作に
より、前記エンジン1の動力を伝動部材5を介して供給
ポンプ6に伝達すると、この供給ポンプ6が駆動される
ことにより、海水7はストレ−ナ8を通り吸入管9から
吸い込まれ、供給管10に吐出される。
Next, in FIG. 2, which more specifically expresses the configuration of the apparatus of the present invention schematically shown in FIG. 1, the conventional structure shown in FIG. 3 and FIG. 4 is the same as in FIG. The same or like parts as those in the example will be described with the same reference numerals. In FIG. 2, the engine 1 as a prime mover is started, and after the speed is set to a predetermined value by the slot lever 3 through the cable 2, the power of the engine 1 is transmitted through the transmission member 5 by operating the clutch 4. When the water is transmitted to the supply pump 6, the supply pump 6 is driven so that the seawater 7 is sucked from the suction pipe 9 through the strainer 8 and discharged to the supply pipe 10.

【0015】圧力計11が介設される前記供給管10の
通路には、プレフイルタ12が設置されており、海水に
混入している微細な異物が濾過され、送液装置Aとして
の圧送ポンプ13に供給される状態になつたところで、
前記圧送ポンプ13には、クラツチ14の操作により、
エンジン1の動力が伝動部材15を介して伝達される。
A prefilter 12 is installed in the passage of the supply pipe 10 in which a pressure gauge 11 is interposed, and fine foreign matter mixed in seawater is filtered, and a pressure pump 13 as a liquid feeding device A is provided. When it is ready to be supplied to
The pressure feed pump 13 is operated by the clutch 14 to
The power of the engine 1 is transmitted via the transmission member 15.

【0016】前記圧送ポンプ13は、前述の供給された
海水を吸い込んで吐出し、アキユムレ−タ16により脈
動を低減され、圧送管17を通り、逆浸透膜部Bの逆浸
透膜18に導入される。導出管19には前記逆浸透膜1
8と共に逆浸透膜部Bを構成する調圧弁20が設けられ
ており、逆浸透膜18に導入される海水の圧力が所定の
逆浸透圧力になるように、圧力計21を見て調圧弁20
を調節すると、導出管22からは透過水が、導出管19
からは濃縮水が得られる。
The pressure-feeding pump 13 sucks in and discharges the supplied seawater, and the pulsation is reduced by the accumulator 16 and is introduced into the reverse osmosis membrane 18 of the reverse osmosis membrane portion B through the pressure-feeding pipe 17. It The reverse osmosis membrane 1 is provided in the outlet pipe 19.
8 is provided with a pressure regulating valve 20 that constitutes the reverse osmosis membrane portion B, and the pressure regulating valve 20 is viewed by looking at the pressure gauge 21 so that the pressure of seawater introduced into the reverse osmosis membrane 18 becomes a predetermined reverse osmosis pressure.
The permeated water from the outlet pipe 22 by adjusting the
Concentrated water is obtained from.

【0017】前記透過水は更に活性炭濾過器のような濾
過器23により、カルキや臭みが吸着除去され、導出管
24から飲料水タンク25に飲料水26として貯留さ
れ、コツク27から適時使用に供される。
The permeated water is further adsorbed and removed of chlorine and odor by a filter 23 such as an activated carbon filter, stored as drinking water 26 in a drinking water tank 25 from a discharge pipe 24, and used from a cock 27 for timely use. To be done.

【0018】一方、濃縮水は調圧弁20を通り、回路F
を構成するバイパスホ−ス28から排出放流される。リ
リ−フ弁29は前記逆浸透膜18を保護するため、導入
される海水の圧力が所定の圧力以上になると、前記リリ
−フ弁29が開き、バイパスホ−ス28への圧力水を放
出するようになつている。
On the other hand, the concentrated water passes through the pressure regulating valve 20 and passes through the circuit F.
Is discharged and discharged from the bypass hose 28 which constitutes Since the relief valve 29 protects the reverse osmosis membrane 18, when the pressure of the introduced seawater becomes equal to or higher than a predetermined pressure, the relief valve 29 opens to release the pressurized water to the bypass hose 28. It is becoming like this.

【0019】前記吸入管9の途中には三方コツク39が
介設され、この三方コツク39は管路40によつて前記
供給管10に介設した三方コツク41と接続され、かつ
この供給管10にはもう一つの三方コツク42が介設さ
れていて、この三方コツク42から出た管路43が前記
圧力計11を経て圧送ポンプ13に接続され、これら三
方コツク39,41,42を経由する迂回路Cが形成さ
れる。
A three-way cock 39 is provided in the middle of the suction pipe 9, and the three-way cock 39 is connected to a three-way cock 41 provided on the supply pipe 10 by a conduit 40, and the supply pipe 10 Another three-way cock 42 is installed in the pipe, and a pipe line 43 coming out of the three-way cock 42 is connected to the pressure feed pump 13 via the pressure gauge 11 and passes through these three-way cocks 39, 41, 42. The detour C is formed.

【0020】前記圧送管17の途中に介設した三方コツ
ク44から出た分岐管45は調圧弁33に接続され、前
記三方コツク44、分岐管45と共に回路Eを構成する
この調圧弁33から導出される管路46は、カプラ47
によつて延長高圧ホ−ス31に結合され、この延長高圧
ホ−ス31の末端には、開閉レバ−48を具える洗浄ノ
ズル32が形成され、これら延長高圧ホ−ス31、開閉
レバ−48及び洗浄ノズル32で洗浄部Dを構成する。
A branch pipe 45 extending from a three-way cock 44 provided in the middle of the pressure feed pipe 17 is connected to a pressure regulating valve 33, and is derived from this pressure regulating valve 33 which constitutes a circuit E together with the three-way cock 44 and the branch pipe 45. The pipe line 46 is a coupler 47.
Is connected to the extended high pressure hose 31 and a washing nozzle 32 having an open / close lever 48 is formed at the end of the extended high pressure hose 31. The extended high pressure hose 31 and the open / close lever are provided. The cleaning unit D is composed of the cleaning nozzle 48 and the cleaning nozzle 32.

【0021】前記管路46から分岐して回路Gを構成す
る分岐管49は三方コツク50に接続され、この三方コ
ツク50は前記導出管19の調圧弁20より下流側に介
設されており、前記調圧弁20から導出される余水管5
1は、前記バイパスホ−ス28に接続される。
A branch pipe 49, which branches from the pipe line 46 and constitutes the circuit G, is connected to a three-way cock 50, and the three-way cock 50 is provided downstream of the pressure regulating valve 20 of the outlet pipe 19, Spill pipe 5 derived from the pressure regulating valve 20
1 is connected to the bypass hose 28.

【0022】前記導出管22の途中に介設される三方コ
ツク52からの導出管53は清水タンク54に導入さ
れ、この清水タンク54に貯留される洗浄用清水55
は、必要に応じてコツク56から取り出せる。また前記
清水タンク54から導出されて回路Hを構成する吸入管
57は前記三方コツク41に接続される。
The lead-out pipe 53 from the three-way cock 52 provided in the middle of the lead-out pipe 22 is introduced into the fresh water tank 54, and the clean water 55 for cleaning stored in the fresh water tank 54.
Can be taken out of the cock 56 as needed. A suction pipe 57, which is drawn from the fresh water tank 54 and constitutes the circuit H, is connected to the three-way cock 41.

【0023】次に上記構成からなるこの発明の海水淡水
化装置の各種使用方法について順次説明すると、先ず飲
料水の造水においては、供給ポンプ6で海水7をストレ
−ナ8を通して吸入管9で汲みあげ、プレフイルタ12
で濾過した海水7を圧送ポンプ13に供給し、吐出す
る。次いでこの海水7は調圧弁20により所定の圧力に
調節され、逆浸透膜18に導入され、透過水と濃縮水に
分離され、透過水は三方コツク52を通り濾過器23で
カルキ成分などを吸着除去して飲料水26を造水して飲
料水タンク25に貯留する。
Next, various methods of using the seawater desalination apparatus of the present invention having the above-mentioned structure will be sequentially described. First, in the production of drinking water, the seawater 7 is passed through the strainer 8 and the seawater 7 through the strainer 8 and the suction pipe 9. Pumping up, prefilter 12
The seawater 7 filtered in step 3 is supplied to the pressure pump 13 and discharged. Next, this seawater 7 is adjusted to a predetermined pressure by the pressure regulating valve 20, introduced into the reverse osmosis membrane 18, separated into permeated water and concentrated water, and the permeated water passes through the three-way cock 52 and adsorbs the scaly component etc. in the filter 23. The drinking water 26 is removed to make fresh water and stored in the drinking water tank 25.

【0024】次に洗浄用清水の造水に当つては、前記飲
料水の造水において、三方コツク52を導出管53方向
に切り変え、洗浄用清水55を造水し、清水タンク54
に貯留する。
Next, in producing fresh water for cleaning, in the production of drinking water, the three-way cock 52 is switched to the direction of the outlet pipe 53 to create fresh water for cleaning 55, and the fresh water tank 54.
Store in.

【0025】海水による洗浄作業に当つては、エンジン
1の動力をクラツチ4で遮断し供給ポンプ6を停止した
状態で、圧送ポンプ13が海水7をストレ−ナ8から三
方コツク39,41,42を介して吸入し、圧送管43
に吐出される。三方コツク44は分岐管45方向にあ
り、調圧弁33で所定の圧力に調節されて、カプラ47
に導びかれ、それに接続する延長高圧ホ−ス31を通し
て洗浄ノズル32により洗浄作業を行なう。噴射停止時
は調圧弁33から全流量が余水管34から排出されバイ
パスホ−ス28により放出される。
In the washing operation with seawater, the pressure feed pump 13 pumps the seawater 7 from the strainer 8 to the three-way cocks 39, 41, 42 while the power of the engine 1 is shut off by the clutch 4 and the supply pump 6 is stopped. Inhaled through the pressure feed pipe 43
Is discharged. The three-way cock 44 is in the direction of the branch pipe 45, and is adjusted to a predetermined pressure by the pressure regulating valve 33, so that the coupler 47
The cleaning operation is carried out by the cleaning nozzle 32 through the extended high pressure hose 31 connected to it. When the injection is stopped, the entire flow rate is discharged from the pressure regulating valve 33 from the spill pipe 34 and discharged by the bypass hose 28.

【0026】清水による洗浄作業に当つては、エンジン
1の動力をクラツチ4で遮断し、供給ポンプ6を停止し
た状態で、圧送ポンプ13が清水タンク54に貯留して
ある洗浄用清水55を、吸入管57、三方コツク41,
42を通して吸入し圧送管17に吐出させる。この際三
方コツク44は分岐管45方向にあり、調圧弁33で所
定の圧力に調節されて、カプラ47に導びかれ、それに
接続する延長高圧ホ−ス31を通して、洗浄ノズル32
により洗浄作業を行なう。清水による洗浄作業の際は節
水のため、バイパスホ−ス28の排出口は清水タンク5
4に投入されており、開閉レバ−48で噴射を停止した
とき、調圧弁33から全流量が余水管34から排出さ
れ、バイパスホ−ス28により放出される。
In the cleaning operation with fresh water, the power of the engine 1 is shut off by the clutch 4 and the supply pump 6 is stopped, and the pumping pump 13 cleans the clean water 55 stored in the fresh water tank 54. Suction pipe 57, three-way cock 41,
It is sucked through 42 and discharged to the pressure feed pipe 17. At this time, the three-way cock 44 is in the direction of the branch pipe 45, is adjusted to a predetermined pressure by the pressure regulating valve 33, is guided to the coupler 47, and is passed through the extended high pressure hose 31 connected thereto, and the washing nozzle 32 is connected.
Perform the cleaning work by. Since the water is saved when cleaning with clean water, the outlet of the bypass hose 28 is the clean water tank 5
When the injection is stopped by the open / close lever 48, the entire flow rate is discharged from the pressure regulating valve 33 from the spill pipe 34 and discharged by the bypass hose 28.

【0027】濃縮水を用いて洗浄作業を行ないながら洗
浄用清水を造水するには、前記濃縮水を用いて洗浄作業
を行ないつつ飲料水を造水する場合において、三方コツ
ク52を導出管53方向に切り変え、洗浄用清水55を
生成し、清水タンク54に貯留する。この間一方では濃
縮水による洗浄作業が行なわれる。洗浄ノズル32から
の噴射及び停止は開閉レバ−48で行なわれ、噴射停止
時は調圧弁20から全流量が余水管51から排出され
る。
In order to produce fresh water for cleaning while performing the washing operation using the concentrated water, in the case where the drinking water is produced while performing the washing operation using the concentrated water, the three-way cock 52 is connected to the outlet pipe 53. Switching to the direction, clean water 55 for cleaning is generated and stored in the fresh water tank 54. On the other hand, on the other hand, a washing operation with concentrated water is performed. The injection from the cleaning nozzle 32 and the stop are performed by the open / close lever 48, and when the injection is stopped, the entire flow rate is discharged from the spill pipe 51 from the pressure regulating valve 20.

【0028】濃縮水を用いて、洗浄作業を行ないながら
飲料水を生成するには前記飲料水の造水において、三方
コツク50を分岐管49方向に切り変え、加圧されてい
る濃縮水を分岐管49からカプラ47に導びき、それに
接続される延長高圧ホ−ス31を通して、洗浄ノズル3
2により洗浄作業を行なう。この間一方では飲料水が造
水される。
In order to produce drinking water while performing a washing operation using concentrated water, the three-way cock 50 is switched in the direction of the branch pipe 49 in the above-mentioned drinking water making process to divert the concentrated water under pressure. The washing nozzle 3 is led from the pipe 49 to the coupler 47 and is passed through the extended high pressure hose 31 connected thereto.
Perform the cleaning work according to 2. Meanwhile, drinking water is produced.

【0029】原動機としてエンジンを使用した場合に
は、前記逆浸透膜18に導入される海水の流量はエンジ
ン1の回転数を調節するスロツトルレバ−3で行なうこ
とができ、また洗浄作業のみを行なうときは、エンジン
1の回転数をスロツトルレバ−3で高速で使用すること
もでき、これによつて噴射流量を増やすことが可能とな
る。なお逆浸透膜18に導入される海水の圧力は約40
〜60Kgf/cm2でありこれは、通常の洗浄機で使
用される圧力の範囲内である。
When an engine is used as a prime mover, the flow rate of seawater introduced into the reverse osmosis membrane 18 can be controlled by a slot lever 3 which adjusts the rotation speed of the engine 1, and when only the cleaning work is performed. Can also use the engine 1 at a high speed with the throttle lever-3, which makes it possible to increase the injection flow rate. The pressure of seawater introduced into the reverse osmosis membrane 18 is about 40.
A ~60Kgf / cm 2 and this is within the range of pressures used in conventional cleaning machines.

【0030】この発明においては、前述したように従来
の海水淡水化装置及び洗浄機の構成要素部材の中で、圧
送ポンプ13、原動機としてのエンジン1、調圧弁3
3、アキユムレ−タ16、圧力計21及び吸入管9、供
給管10、圧送管17、導出管22、導出管19、バイ
パスホ−ス28等の配管を共用し、三方コツク42,4
4,52,39,41,50を設けて、上述の6種類の
作業を行なえる機能を持たせ、前記三方コツクの操作の
組み合わせにより、これらを選択できるようにしたもの
であつて、これら三方コツクは電動式とすることもで
き、この場合はスイツチによる選択が可能である。
In the present invention, as described above, among the components of the conventional seawater desalination apparatus and the washing machine, the pressure pump 13, the engine 1 as the prime mover, and the pressure regulating valve 3 are included.
3, the accumulator 16, the pressure gauge 21 and the suction pipe 9, the supply pipe 10, the pressure feeding pipe 17, the outlet pipe 22, the outlet pipe 19, the bypass hose 28 and the like are commonly used, and the three-way cocks 42, 4 are used.
4, 52, 39, 41, 50 are provided so as to have a function of performing the above-mentioned 6 types of work, and these can be selected by a combination of the operations of the three-way cocks. The cock can also be of the electric type and, in this case, can be selected by a switch.

【0031】次に表1によつて、この発明の装置による
6つの機能と、各三方コツクの通路方向を示す。連通の
向きは図2に示した各三方コツクの設置態様にもとづ
く。
Next, Table 1 shows the six functions of the device of the present invention and the direction of passage of each three-way cock. The direction of communication is based on the installation mode of each three-way cock shown in FIG.

【0032】[0032]

【表1】 [Table 1]

【0033】[0033]

【発明の効果】【The invention's effect】

1)この発明による装置を使用すれば、海水淡水化によ
る造水機能と、洗浄機機能とを備えており、従来のよう
に、それぞれ機械装置を単独で設置しなくても済み、6
種類の作業が可能であり、原動機及びポンプは1台の運
転であるから省エネで、設備投資費用が低減できる経済
効果がある。 2)それぞれの作業は、三方コツクの方向を切り変える
ことにより選択できるので、取扱使用に便利である。 3)洗浄しながら造水できるので、同時機能による付加
価値が高く、省力効果がある。 4)海水で洗浄した後、清水で洗浄できるので、洗浄効
果が高い。
1) By using the device according to the present invention, it has a function of producing water by desalination of seawater and a function of a washing machine, so that it is not necessary to separately install each mechanical device as in the conventional case.
It is possible to perform various kinds of work, and since the prime mover and the pump are operated by one unit, there is an economic effect that energy savings can be achieved and facility investment costs can be reduced. 2) Each work can be selected by changing the direction of the three-way cock, which is convenient for handling and use. 3) Since water can be created while washing, it has a high added value due to the simultaneous function and has a labor-saving effect. 4) Since it can be washed with fresh water after washing with seawater, the washing effect is high.

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

【図1】この発明の装置を図式的に示した構成図であ
る。
FIG. 1 is a schematic diagram showing an apparatus of the present invention.

【図2】この発明の装置をより具体的に表現した構成図
である。
FIG. 2 is a configuration diagram more specifically expressing the device of the present invention.

【図3】従来技術による小型簡易海水淡水化装置の構成
図である。
FIG. 3 is a configuration diagram of a small and simple seawater desalination apparatus according to a conventional technique.

【図4】海水又は清水を使用した従来の洗浄機の一例を
示す構成図である。
FIG. 4 is a configuration diagram showing an example of a conventional washing machine using seawater or fresh water.

【符号の説明】[Explanation of symbols]

A 送液装置 B 逆浸透膜部 C 迂回路 D 洗浄部 8 ストレ−ナ 12 プレフイルタ 23 濾過器 25 飲料水タンク 54 清水タンク A Liquid sending device B Reverse osmosis membrane part C Detour D Cleaning part 8 Strainer 12 Prefilter 23 Filter 25 Drinking water tank 54 Fresh water tank

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 海水から逆浸透膜を介して飲料水を造水
するように、海水側から順に、ストレ−ナ(8)と、プレ
フイルタ(12)と、このプレフイルタ(12)に選択的に並設
される迂回路(C)と、送液装置(A)と、逆浸透膜部(B)と
これに選択的に連通される清水タンク(54)と、濾過器(2
3)を介装された飲料水タンク(25)とを連結される海水淡
水化装置であつて、前記送液装置(A)と前記逆浸透膜部
(B)との間には洗浄部(D)が選択的に連通可能とされる一
方、前記洗浄部(D)は前記逆浸透膜部(B)の加圧下の濃縮
水に断接可能に連通され、前記清水タンク(54)は前記送
液装置(A)の吸入側に選択的に断接可能とされている海
水淡水化装置。
1. A strainer (8), a prefilter (12), and this prefilter (12) are selectively disposed in order from the seawater side so that drinking water is produced from seawater through a reverse osmosis membrane. A bypass line (C) installed in parallel, a liquid delivery device (A), a reverse osmosis membrane part (B), a fresh water tank (54) selectively communicating with this, and a filter (2
3) A seawater desalination apparatus that is connected to a drinking water tank (25) having an intermediate interposed therebetween, wherein the liquid delivery apparatus (A) and the reverse osmosis membrane section
A washing part (D) can be selectively communicated with (B), while the washing part (D) can be connected to and disconnected from the concentrated water under pressure of the reverse osmosis membrane part (B). A seawater desalination apparatus in which the fresh water tank (54) is connected and can be selectively connected to and disconnected from the suction side of the liquid transfer apparatus (A).
【請求項2】 前記ストレ−ナ(8)と、プレフイルタ(1
2)と、送液装置(A)と、逆浸透膜部(B)と、濾過器(23)を
経て飲料水タンク(25)に至る系統を選択してなる、請求
項1記載の海水淡水化装置の飲料水造水のための使用方
法。
2. The strainer (8) and the prefilter (1)
2. The seawater freshwater according to claim 1, wherein a system from 2), a liquid sending device (A), a reverse osmosis membrane part (B), and a drinking water tank (25) through a filter (23) is selected. Method of use of water purification equipment for drinking water production.
【請求項3】 前記ストレ−ナ(8)と、プレフイルタ(1
2)と、送液装置(A)と、逆浸透膜部(B)とを経て清水タン
ク(54)に至る系統を選択してなる、請求項1記載の海水
淡水化装置の洗浄用清水造水のための使用方法。
3. A strainer (8) and a prefilter (1)
The fresh water production for cleaning of a seawater desalination apparatus according to claim 1, wherein a system leading to the fresh water tank (54) through 2), the liquid sending device (A) and the reverse osmosis membrane part (B) is selected. Usage for water.
【請求項4】 海水を前記ストレ−ナ(8)から前記迂回
路(C)により直接送液装置(A)を介して洗浄部(D)に圧送
する系統を選択してなる請求項1記載の海水淡水化装置
の海水による洗浄作業のための使用方法。
4. A system in which seawater is pressure-fed from the strainer (8) to the cleaning section (D) by the bypass (C) directly via the liquid delivery device (A) is selected. Of using the seawater desalination equipment in Japan for washing with seawater.
【請求項5】 前記清水タンク(54)からの清水を、送液
装置(A)を介して洗浄部(D)へ圧送する系統を選択してな
る請求項1記載の海水淡水化装置の清水による洗浄作業
のための使用方法。
5. The fresh water of the seawater desalination apparatus according to claim 1, wherein a system is selected in which the fresh water from the fresh water tank (54) is pressure-fed to the cleaning section (D) via the liquid feeding apparatus (A). How to use for cleaning work.
【請求項6】 前記ストレ−ナ(8)と、プレフイルタ(1
2)と、送液装置(A)と、逆浸透膜部(B)とを経て清水タン
ク(54)に至る系統からなる洗浄用清水造水を行ないつ
つ、前記逆浸透膜部(B)の加圧下の濃縮水を前記洗浄部
(D)に送液して洗浄作業を行なうようにした請求項1記
載の海水淡水化装置の使用方法。
6. The strainer (8) and a prefilter (1)
2), the liquid-sending device (A), while performing the clean fresh water for cleaning consisting of a system that goes through the reverse osmosis membrane part (B) to the fresh water tank (54), the reverse osmosis membrane part (B) Concentrated water under pressure is added to the cleaning unit.
The method of using the seawater desalination apparatus according to claim 1, wherein the washing operation is performed by sending the liquid to (D).
【請求項7】 前記ストレ−ナ(8)と、プレフイルタ(1
2)と送液装置(A)と、逆浸透膜部(B)と、濾過器(23)を経
て飲料水タンク(25)に至る系統からなる飲料水造水を行
ないつつ、前記逆浸透膜部(B)の加圧下の濃縮水を前記
洗浄部(D)に送液して洗浄作業を行なうようにした請求
項1記載の海水淡水化装置の使用方法。
7. The strainer (8) and a prefilter (1)
2) and the liquid feeding device (A), the reverse osmosis membrane portion (B), while performing drinking water fresh water consisting of a system that goes through the filter (23) to the drinking water tank (25), the reverse osmosis membrane The method of using the seawater desalination apparatus according to claim 1, wherein concentrated water under pressure in the section (B) is sent to the cleaning section (D) to perform the cleaning operation.
JP7234618A 1995-08-22 1995-08-22 Sea water desalting device and method for using this device Pending JPH0957259A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7234618A JPH0957259A (en) 1995-08-22 1995-08-22 Sea water desalting device and method for using this device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7234618A JPH0957259A (en) 1995-08-22 1995-08-22 Sea water desalting device and method for using this device

Publications (1)

Publication Number Publication Date
JPH0957259A true JPH0957259A (en) 1997-03-04

Family

ID=16973873

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7234618A Pending JPH0957259A (en) 1995-08-22 1995-08-22 Sea water desalting device and method for using this device

Country Status (1)

Country Link
JP (1) JPH0957259A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004210036A (en) * 2002-12-27 2004-07-29 Shinko:Kk Hydrophore tank unit and inboard water supply system
JP2012071233A (en) * 2010-09-28 2012-04-12 Kyb Co Ltd Seawater desalination apparatus
WO2013039224A1 (en) * 2011-09-15 2013-03-21 東レ株式会社 Freshwater production apparatus and method for producing freshwater
CN115228297A (en) * 2022-07-15 2022-10-25 华北电力科学研究院有限责任公司 Reverse osmosis automatic cleaning method and system

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004210036A (en) * 2002-12-27 2004-07-29 Shinko:Kk Hydrophore tank unit and inboard water supply system
JP2012071233A (en) * 2010-09-28 2012-04-12 Kyb Co Ltd Seawater desalination apparatus
WO2013039224A1 (en) * 2011-09-15 2013-03-21 東レ株式会社 Freshwater production apparatus and method for producing freshwater
JPWO2013039224A1 (en) * 2011-09-15 2015-03-26 東レ株式会社 Fresh water production apparatus and fresh water production method
AU2012309380B2 (en) * 2011-09-15 2016-10-20 Toray Industries, Inc. Freshwater production apparatus and method for producing freshwater
CN115228297A (en) * 2022-07-15 2022-10-25 华北电力科学研究院有限责任公司 Reverse osmosis automatic cleaning method and system

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