Nothing Special   »   [go: up one dir, main page]

JPH0768257A - Fresh water producing apparatus - Google Patents

Fresh water producing apparatus

Info

Publication number
JPH0768257A
JPH0768257A JP21859193A JP21859193A JPH0768257A JP H0768257 A JPH0768257 A JP H0768257A JP 21859193 A JP21859193 A JP 21859193A JP 21859193 A JP21859193 A JP 21859193A JP H0768257 A JPH0768257 A JP H0768257A
Authority
JP
Japan
Prior art keywords
water
raw water
reverse osmosis
osmosis membrane
valve
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP21859193A
Other languages
Japanese (ja)
Other versions
JP3270211B2 (en
Inventor
Hidenori Kayano
秀則 茅野
Yasuhide Nakakuki
康秀 中久喜
Naomi Kawahito
尚美 川人
Yuji Hayashi
佑二 林
Mari Koide
真理 小出
Hiroshi Takeuchi
宏 武内
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.)
Organo Corp
Takenaka Komuten Co Ltd
Original Assignee
Organo Corp
Takenaka Komuten Co Ltd
Japan Organo 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 Organo Corp, Takenaka Komuten Co Ltd, Japan Organo Co Ltd filed Critical Organo Corp
Priority to JP21859193A priority Critical patent/JP3270211B2/en
Publication of JPH0768257A publication Critical patent/JPH0768257A/en
Application granted granted Critical
Publication of JP3270211B2 publication Critical patent/JP3270211B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To obtain fresh water in such a state that the production amt. of water is stabilized, to enhance the coefficient of utilization of raw water and to facilitate maintenance and control by controlling the suppry pressure of water to a reverse osmosis membrane device by controlling the opening degree of a flow control valve on the basis of the detection signal of a flow rate detector. CONSTITUTION:A part of the raw water supplied to a reverse osmosis membrane device 8 transmits through a reverse osmosis membrane to be taken out as fresh water from a transmitted water pipe 24 but, at this time, the amt. of transmitted water is measured by a flow rate detector 26 to be compared with a preset amt. When the amt. of transmitted water is more than the preset amt., a control signal is sent to a flow control valve 14 to increase the opening degree of the valve 14 and the pressure of the raw water supplied to the reverse osmosis membrane device 8 is reduced to reduce the amt. of transmitted water. When the amt. of transmitted water is less than the preset amt., a control signal is sent to the flow control valve 14 to reduce the opening degree of the valve 14 and the pressure of the raw water supplied to the reverse osmosis membrane 8 is increased to increase the amt. of transmitted water. By this constitution, the amt. of transmitted water can be held to an almost preset desired value.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は飲料水等の淡水製造装置
に関し、更に詳述すれば離島等で用いて好適な逆浸透膜
装置を用いた淡水製造装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for producing fresh water such as drinking water, and more particularly to an apparatus for producing fresh water using a reverse osmosis membrane apparatus suitable for use in isolated islands.

【0002】[0002]

【従来の技術】従来、逆浸透膜を用いた飲料水の製造装
置においては、逆浸透ポンプの運転圧力は一定である。
いつも同じ塩濃度の原水(例えば海水)を利用する場合
は問題ないが、より塩濃度の低い原水を利用可能な状況
になったとき(例えば、雨水を集め、この雨水を海水と
混合して逆浸透膜装置の原水とする場合等)、原水の逆
浸透圧が低くなるため、ポンプ圧力が一定であるにもか
かわらず、生産水量が急激に増加し、これを受ける生産
水タンクの貯水量の容量をオーバーしたり、濃縮水量が
少なくなるため、逆浸透膜の目詰まりを起こす可能性が
ある。また従来の逆浸透膜装置では、逆浸透膜装置に供
給する原水は予め凝集沈澱や濾過等の前処理が必要であ
るが、このようにして前処理を行なった原水の多くを、
逆浸透膜処理の際に発生する濃縮水として捨てている。
このため、前処理設備の負荷が大きく、また原水の利用
効率が低い。
2. Description of the Related Art Conventionally, in a drinking water manufacturing apparatus using a reverse osmosis membrane, the operating pressure of a reverse osmosis pump is constant.
There is no problem if you always use raw water with the same salt concentration (for example, seawater), but when raw water with a lower salt concentration becomes available (for example, collect rainwater, mix this rainwater with seawater, and reverse When the raw water of the osmosis membrane device is used), the reverse osmotic pressure of the raw water becomes low, so the production water volume increases sharply even though the pump pressure is constant, and There is a possibility that the reverse osmosis membrane may be clogged because the capacity is exceeded or the amount of concentrated water decreases. Further, in the conventional reverse osmosis membrane device, the raw water supplied to the reverse osmosis membrane device requires pretreatment such as coagulation sedimentation or filtration in advance, but most of the raw water pretreated in this way is
It is discarded as concentrated water generated during reverse osmosis membrane treatment.
Therefore, the load of the pretreatment facility is large and the utilization efficiency of raw water is low.

【0003】一方、逆浸透膜装置を用いた飲料水製造設
備は、水源の乏しい場所で使用されるが、最小のエネル
ギーで運転されることが望ましいことから、海水だけで
なく、海水より塩濃度の低い雨水混入海水やかん水まで
利用できる装置が望ましい。
On the other hand, a facility for producing drinking water using a reverse osmosis membrane device is used in a place where the water source is scarce, but it is desirable to operate with the minimum energy. Therefore, not only seawater but also salt concentration is better than seawater. It is desirable to have a device that can use seawater and brackish water mixed with low-rainwater.

【0004】[0004]

【発明が解決しようとする課題】本発明は上記問題を解
決するためになされたもので、原水中の塩濃度が変化し
ても、逆浸透膜装置の生産水量を一定にすることで、逆
浸透膜の目詰まりを防ぎ、かつ濃縮水塩濃度が低い場合
はこれを原水として再利用することで原水の有効利用率
を高め、また前処理(除濁等の前処理)の負荷を低減す
るもので、その目的とするところは、上記問題を解決し
た淡水製造装置を提供することにある。
SUMMARY OF THE INVENTION The present invention has been made to solve the above problems. Even if the salt concentration in the raw water changes, the reverse osmosis membrane device produces a constant amount of water, thereby improving the Prevents clogging of the osmosis membrane and, when the concentration of concentrated water salt is low, reuses this as raw water to increase the effective utilization rate of raw water and reduce the load of pretreatment (pretreatment such as turbidity). The object of the invention is to provide a fresh water producing apparatus that solves the above problems.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するため
に本発明においては、原水タンクと、加圧ポンプを介装
してなり前記原水タンク内の原水を逆浸透膜装置に加圧
送給する送給パイプと、加圧送給された原水を透過水と
濃縮水とに分離して取り出す逆浸透膜装置と、前記逆浸
透膜装置から取り出される濃縮水を原水タンクに返送す
る循環パイプとからなる淡水製造装置において、前記逆
浸透膜装置の透過水取出し部に透過水の流量を検出する
流量検出器を設けると共に、前記循環パイプに流量調節
弁を介装してなり、前記流量検出器の検出信号に基づい
て前記流量調節弁の開度を制御して逆浸透膜装置の供給
水圧を調節することにより逆浸透膜装置の透過水量を所
定量とするもので、送給パイプに原水の塩濃度を検出す
る濃度検出器を設け、循環パイプの流量調節弁と原水タ
ンクとの間において遮断弁を介装すると共に、循環パイ
プの前記流量調節弁と遮断弁との間において排出弁を介
装した排出管を連結するか、当該遮断弁に換えて、排出
口を有する三方弁を付設してなり、前記濃度検出器で検
出された原水の塩濃度が所定値以上になると濃度検出器
の信号に基づいて前記遮断弁を閉じると共に前記排出弁
を開くか、又は前記三方弁の排出口を開いて濃縮水を排
出管から排出することを含むものである。
In order to achieve the above object, in the present invention, a raw water tank and a pressurizing pump are interposed, and the raw water in the raw water tank is fed under pressure to a reverse osmosis membrane device. It consists of a feed pipe, a reverse osmosis membrane device that separates the pressurized and fed raw water into permeated water and concentrated water, and a circulation pipe that returns the concentrated water taken out from the reverse osmosis membrane device to a raw water tank. In the fresh water producing apparatus, a flow rate detector for detecting the flow rate of permeated water is provided in the permeated water take-out part of the reverse osmosis membrane device, and a flow rate control valve is provided in the circulation pipe to detect the flow rate detector. The permeated water amount of the reverse osmosis membrane device is adjusted to a predetermined amount by controlling the opening of the flow rate control valve based on the signal to adjust the supply water pressure of the reverse osmosis membrane device. A concentration detector to detect A cutoff valve is provided between the flow control valve of the circulation pipe and the raw water tank, and a discharge pipe provided with a discharge valve is connected between the flow control valve of the circulation pipe and the cutoff valve, or In place of the shutoff valve, a three-way valve having a discharge port is additionally provided, and when the salt concentration of the raw water detected by the concentration detector exceeds a predetermined value, the shutoff valve is closed based on the signal of the concentration detector. It includes opening the discharge valve or opening the discharge port of the three-way valve to discharge the concentrated water from the discharge pipe.

【0006】また本発明は、淡水製造装置の電源として
太陽電池モジュールを使用し、この太陽電池モジュール
に集水手段を設けると共に、前記集水手段と原水タンク
とを導水管で連結してなり、モジュール上面で受けた雨
水を前記集水手段及び導水管を介して原水タンクへ供給
する淡水製造装置である。
Further, according to the present invention, a solar cell module is used as a power source of a fresh water producing apparatus, and the solar cell module is provided with a water collecting means, and the water collecting means and the raw water tank are connected by a water pipe. It is a fresh water producing apparatus for supplying rainwater received on the upper surface of a module to a raw water tank via the water collecting means and a water conduit.

【0007】[0007]

【実施例】以下、実施例により本発明を詳細に説明す
る。
The present invention will be described in detail below with reference to examples.

【0008】(実施例1)図1は本発明の一実施例を示
すフロー図で、図中2は淡水化する海水等を貯留する原
水タンクである。原水タンク内の原水は送給パイプ4に
介装された加圧ポンプ6によって逆浸透膜装置8に送給
され、ここでその一部が脱塩された透過水となり、該装
置8の取出し部10から取出されると共に、残部は濃縮
水として循環パイプ12を通り原水タンク2に返送され
る。前記循環パイプ12には、逆浸透膜装置8側から順
次流量調節弁14、及び遮断弁16が介装されており、
これらの弁14及び16は電気信号により作動するもの
である。
(Embodiment 1) FIG. 1 is a flow chart showing an embodiment of the present invention, in which 2 is a raw water tank for storing desalinated seawater and the like. The raw water in the raw water tank is fed to the reverse osmosis membrane device 8 by the pressurizing pump 6 interposed in the feed pipe 4, where a part of the raw water becomes desalted permeate, and the take-out part of the device 8 While being taken out from the tank 10, the rest is returned as concentrated water to the raw water tank 2 through the circulation pipe 12. The circulation pipe 12 is provided with a flow rate control valve 14 and a shutoff valve 16 sequentially from the reverse osmosis membrane device 8 side,
These valves 14 and 16 are operated by electric signals.

【0009】また、これらの弁14及び16の間におい
て循環パイプ12には排出管18の一端が連結されてい
る。なお、20は排出管18に介装された排出弁で、電
気信号によって作動するようになっている。
Further, one end of a discharge pipe 18 is connected to the circulation pipe 12 between the valves 14 and 16. A discharge valve 20 is provided in the discharge pipe 18 and is operated by an electric signal.

【0010】22は原水タンク2と加圧ポンプ6との間
において送給パイプ4に介装された濃度検出器(本例に
おいては電気伝導率計)で、パイプ4内を送られる原水
中の塩濃度を検出し、塩濃度に対応する電気信号を前記
遮断弁16及び排出弁20に送出し、これにより両弁1
6,20が開閉する。
Reference numeral 22 denotes a concentration detector (in this example, an electric conductivity meter) interposed in the feed pipe 4 between the raw water tank 2 and the pressurizing pump 6, and the concentration detector in the raw water fed in the pipe 4 The salt concentration is detected, and an electric signal corresponding to the salt concentration is sent to the shutoff valve 16 and the discharge valve 20, whereby both valves 1
6, 20 open and close.

【0011】24は透過水の取出し部10に連結された
透過水パイプで、流量検出器26が介装されている。こ
の検出器26は、透過水パイプ24内を流れる透過水の
流量を検出して、その流量に対応する電気信号を前記流
量調節弁14に送り、これにより流量調節弁14の開度
を調節して循環パイプ12内を原水タンク2に返送され
る濃縮水の流量を制御するものである。
Reference numeral 24 is a permeated water pipe connected to the permeated water take-out portion 10, and a flow rate detector 26 is interposed therein. The detector 26 detects the flow rate of the permeated water flowing through the permeated water pipe 24 and sends an electric signal corresponding to the flow rate to the flow rate control valve 14, thereby adjusting the opening degree of the flow rate control valve 14. The flow rate of the concentrated water returned to the raw water tank 2 through the circulation pipe 12 is controlled.

【0012】次に上記構成の淡水製造装置を用いて、一
例として海水に雨水が混合された原水を淡水化する場合
につき説明すると、まず原水は公知の前処理装置によっ
て除濁等の前処理がなされた後、原水タンク2に貯留さ
れる。この場合、タンク2内の原水の塩濃度は雨水が混
合しているので海水よりも低いものである。原水タンク
2内の原水は、次いで加圧ポンプ6によって逆浸透膜装
置8に加圧送給されるが、この際逆浸透膜装置8に送給
される原水中の塩濃度が濃度検出器22により測定さ
れ、予め設定された塩濃度(本例にあっては海水の塩濃
度)と比較され、設定濃度よりも低い場合には遮断弁1
6が“開”、排出弁20が“閉”になる制御信号が検出
器22から両弁16,20にそれぞれ送られる。
Next, using the fresh water producing apparatus having the above-mentioned structure, as an example, the case of desalinating raw water in which rainwater is mixed with seawater will be explained. After being done, it is stored in the raw water tank 2. In this case, the salt concentration of the raw water in the tank 2 is lower than that of seawater because rainwater is mixed. The raw water in the raw water tank 2 is then pressure-fed by the pressure pump 6 to the reverse osmosis membrane device 8. At this time, the salt concentration in the raw water fed to the reverse osmosis membrane device 8 is detected by the concentration detector 22. It is measured and compared with a preset salt concentration (in this example, salt concentration of seawater), and when it is lower than the set concentration, the shutoff valve 1
A control signal is sent from the detector 22 to both valves 16 and 20 such that 6 is "open" and discharge valve 20 is "closed".

【0013】前記逆浸透膜装置8に送給された原水は、
その一部が逆浸透膜を透過して淡水化された透過水とな
り、透過水パイプ24から取り出されるが、この際、流
量検出器26によって透過水量が測定され、予め設定さ
れた透過水量と比較が行なわれる。そして、透過水量が
設定された透過水量よりも多い場合には、検出器26か
ら流量調節弁14に制御信号が送られ、弁14の開度を
大きくする。これにより、逆浸透膜装置8に送給される
原水圧(供給水圧)が減少し、透過水量は減少する方向
に向う。また、透過水量が設定された透過水量よりも少
ない場合には、検出器26から流量調節弁14に制御信
号が送られ、弁14の開度を小さくする。これにより逆
浸透膜装置8に送給される原水圧が増加し、透過水量は
増大する方向に向う。このようにして、透過水量はほぼ
予め設定された所望の値を保つものである。
The raw water sent to the reverse osmosis membrane device 8 is
A part of the permeated water passes through the reverse osmosis membrane and becomes desalinated water, which is taken out from the permeated water pipe 24. At this time, the permeated water amount is measured by the flow rate detector 26 and compared with the preset permeated water amount. Is performed. Then, when the amount of permeated water is larger than the set amount of permeated water, a control signal is sent from the detector 26 to the flow rate control valve 14 to increase the opening degree of the valve 14. As a result, the raw water pressure (supply water pressure) sent to the reverse osmosis membrane device 8 decreases, and the amount of permeated water decreases. Further, when the amount of permeated water is smaller than the set amount of permeated water, a control signal is sent from the detector 26 to the flow rate control valve 14 to reduce the opening degree of the valve 14. As a result, the raw water pressure fed to the reverse osmosis membrane device 8 increases, and the amount of permeated water increases. In this way, the amount of permeated water is maintained at a preset desired value.

【0014】一方、逆浸透膜装置8から返送される濃縮
水は塩濃度が高められた状態で原水タンク2に流入し、
これによって徐々に原水タンク2内の原水の塩濃度が高
まる。そして、濃度検出器22で測定される塩濃度の値
が予め設定した値(本例にあっては海水の塩濃度)を越
えると濃度検出器22から信号が送出され、これにより
遮断弁16が閉じると共に、排出弁20が開き、逆浸透
膜装置8からの濃縮水(海水よりも高い塩濃度)は排出
管18から系外に排出される。なお、この状態におい
て、原水タンク2には前処理をした原水が常に供給され
ており、かつ、濃縮水は原水タンク2に循環せずに排出
管18から排出されているので、原水は一過式で処理し
ていることになる。
On the other hand, the concentrated water returned from the reverse osmosis membrane device 8 flows into the raw water tank 2 with the salt concentration increased,
This gradually increases the salt concentration of the raw water in the raw water tank 2. Then, when the value of the salt concentration measured by the concentration detector 22 exceeds a preset value (in this example, the salt concentration of seawater), a signal is sent from the concentration detector 22, which causes the shutoff valve 16 to operate. Upon closing, the discharge valve 20 is opened, and the concentrated water (higher salt concentration than seawater) from the reverse osmosis membrane device 8 is discharged out of the system through the discharge pipe 18. In this state, the raw water tank 2 is always supplied with the pretreated raw water, and the concentrated water is discharged from the discharge pipe 18 without being circulated to the raw water tank 2. It is processed by an expression.

【0015】また、この状態で原水タンク2に上記原水
が継続して供給され、濃度検出器22で測定される塩濃
度が設定した値よりも低くなると、上記と同様の手順で
弁16が開くと共に、弁20が閉じて最初の状態に復帰
するが、この場合においても透過水量は流量検出器26
及び流量調節弁14の作動によって一定に保たれている
ものである。
Further, when the raw water is continuously supplied to the raw water tank 2 in this state and the salt concentration measured by the concentration detector 22 becomes lower than the set value, the valve 16 is opened by the same procedure as described above. At the same time, the valve 20 closes and returns to the initial state. Even in this case, the amount of permeated water is determined by the flow rate detector 26.
And is kept constant by the operation of the flow rate control valve 14.

【0016】なお、上記実施例においては原水として、
海水に雨水が混合された、したがって海水よりも塩濃度
の低い水を処理する場合について説明したが、上記淡水
製造装置を用いて常時海水を処理する場合には、前記遮
断弁16を閉じ、前記排出弁20を“開”として逆浸透
膜装置8の濃縮水を排出管18から常時系外に排出しな
がら淡水の製造を行うこともできる。また、濃度検出器
としては、抵抗率計等も使用できる。更に濃度検出器2
2において予め設定された値は海水の塩濃度に限られず
任意の値に設定できるものである。
In the above embodiment, as raw water,
The case of treating water in which rainwater is mixed with seawater and therefore having a lower salt concentration than seawater has been described. However, in the case of always treating seawater using the fresh water producing apparatus, the shutoff valve 16 is closed, and It is also possible to manufacture the fresh water while constantly discharging the concentrated water of the reverse osmosis membrane device 8 to the outside of the system by opening the discharge valve 20. A resistivity meter or the like can also be used as the concentration detector. Further concentration detector 2
The value preset in 2 is not limited to the salt concentration of seawater and can be set to any value.

【0017】更に、上記実施例では排出管18に排出弁
20を、また循環パイプ12に遮断弁16をそれぞれ介
装したが、遮断弁16に換えて排出口を有する三方弁を
付設し、前記濃度検出器の信号によって三方弁の流路を
切換えるようにしても上記実施例と同じ制御を行うこと
ができ、このようにすれば排出弁20を省略することが
できる。
Further, in the above-described embodiment, the discharge valve 20 is provided in the discharge pipe 18 and the shutoff valve 16 is provided in the circulation pipe 12, respectively. Instead of the shutoff valve 16, a three-way valve having a discharge port is additionally provided. Even if the flow path of the three-way valve is switched by the signal of the concentration detector, the same control as in the above embodiment can be performed, and in this case, the discharge valve 20 can be omitted.

【0018】(実施例2)図2は本発明の他の実施例を
示すもので、この例にあっては、本発明の淡水製造装置
に太陽電池を組込んだものである。
(Embodiment 2) FIG. 2 shows another embodiment of the present invention, in which a solar cell is incorporated in the fresh water producing apparatus of the present invention.

【0019】図2において、30は直方体状の原水タン
クで、その上面に逆浸透膜装置32が載置されている。
34は送給パイプで、加圧ポンプ36を作動させること
により、原水タンク30内の原水を前記逆浸透膜装置3
2に送り、淡水製造を行なうもので、弁、検出器等は記
載を省略してあるが、これらにより、前記実施例1の淡
水製造装置が構成されている。
In FIG. 2, reference numeral 30 denotes a rectangular parallelepiped raw water tank on which a reverse osmosis membrane device 32 is mounted.
Reference numeral 34 denotes a feed pipe, which operates the pressurizing pump 36 to feed the raw water in the raw water tank 30 to the reverse osmosis membrane device 3
2, the fresh water production is performed, and the valves, detectors, and the like are omitted, but these constitute the fresh water production apparatus of the first embodiment.

【0020】前記原水タンク30の上面には架台38が
設けられており、前記架台38に上記淡水製造装置の電
源である太陽電池モジュール40が水平面に対して所定
の傾きをもって取付けられている。また、太陽電池モジ
ュール40の両端部、及び下端部には集水溝42が形成
されており、太陽電池モジュール40の傾斜表面で受け
た雨水は、集水溝42に集められた後、導水管44,4
6を通って原水タンク30に流下する。なお、48は除
濁処理をした海水を原水タンクへ供給する供給管であ
る。
A gantry 38 is provided on the upper surface of the raw water tank 30, and a solar cell module 40, which is a power source of the fresh water producing apparatus, is attached to the gantry 38 with a predetermined inclination with respect to a horizontal plane. Further, water collecting grooves 42 are formed at both ends and the lower end of the solar cell module 40, and the rainwater received by the inclined surface of the solar cell module 40 is collected in the water collecting grooves 42, and then the water conduit pipe. 44,4
It flows through 6 to the raw water tank 30. Reference numeral 48 is a supply pipe for supplying the turbidity-treated seawater to the raw water tank.

【0021】なお、上記実施例においては原水として海
水、及び雨水を用いたがこれに限らず河川水、カン水等
各種のものが使用できる。
Although seawater and rainwater are used as raw water in the above embodiment, various kinds of water such as river water and can water can be used.

【0022】本例のように構成すると、雨水集取が簡単
になり、かつ本装置の設置に必要な面積も少ないので、
特に離島における飲料水製造用として好ましいものであ
る。
The configuration of this example simplifies the collection of rainwater and reduces the area required to install this device.
Particularly, it is preferable for producing drinking water in remote islands.

【0023】[0023]

【発明の効果】本発明装置は原水の塩濃度変化に対応す
る制御機能を有することで、生産水量が安定した状態で
淡水が得られる。また原水の利用率が高く、また維持管
理が容易である。
The device of the present invention has a control function corresponding to changes in salt concentration of raw water, so that fresh water can be obtained in a state where the amount of produced water is stable. In addition, the utilization rate of raw water is high and maintenance is easy.

【0024】この様な機能を有する装置を、例えば雨量
の多い南方の離島などで、雨水と海水の両方を利用しな
がら使うことによって、淡水を長期間、安定した供給量
で供給可能になる。また、逆浸透膜は他の濾過膜と異な
り、細菌も確実に除去できるので、特に飲料水を製造す
る場合、衛生上の信頼性が高くなり、従って衛生上の維
持管理も容易になる。
By using an apparatus having such a function, for example, on a remote island in the south where there is a large amount of rainfall while utilizing both rainwater and seawater, it becomes possible to supply fresh water at a stable supply amount for a long period of time. Further, unlike other filtration membranes, reverse osmosis membranes can surely remove bacteria, so that hygienic reliability becomes high, and hygiene maintenance and management becomes easy, especially when producing drinking water.

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

【図1】本発明の一実施例を示すフロー図である。FIG. 1 is a flow chart showing an embodiment of the present invention.

【図2】本発明の他の実施例を示す概略斜視図である。FIG. 2 is a schematic perspective view showing another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

2 原水タンク 4 送給パイプ 6 加圧ポンプ 8 逆浸透膜装置 10 取出し部 12 循環パイプ 14 流量調節弁 16 遮断弁 18 排出管 20 排出弁 22 濃度検出器 24 透過水パイプ 26 流量検出器 30 原水タンク 32 逆浸透膜装置 40 太陽電池モジュール 2 Raw water tank 4 Supply pipe 6 Pressurizing pump 8 Reverse osmosis membrane device 10 Extraction part 12 Circulation pipe 14 Flow rate control valve 16 Shutoff valve 18 Discharge pipe 20 Discharge valve 22 Concentration detector 24 Permeate pipe 26 Flow rate detector 30 Raw water tank 32 reverse osmosis membrane device 40 solar cell module

───────────────────────────────────────────────────── フロントページの続き (72)発明者 川人 尚美 東京都江東区南砂2丁目5番14号 株式会 社竹中工務店技術研究所内 (72)発明者 林 佑二 埼玉県戸田市川岸1丁目4番9号 オルガ ノ株式会社総合研究所内 (72)発明者 小出 真理 埼玉県戸田市川岸1丁目4番9号 オルガ ノ株式会社総合研究所内 (72)発明者 武内 宏 東京都文京区本郷5丁目5番16号 オルガ ノ株式会社内 ─────────────────────────────────────────────────── --- Continuation of the front page (72) Inventor Naomi Kawato 2-5-14 Minamisuna, Koto-ku, Tokyo Inside the Takenaka Corporation Technical Research Institute (72) Inventor Yuji Hayashi 1-4 Kawagishi, Toda City, Saitama Prefecture No. 9 Organo Research Institute (72) Inventor Mari Koide 1-4-9 Kawagishi, Toda City, Saitama Organo Research Institute (72) Inventor Hiroshi Takeuchi 5 Hongo, Bunkyo-ku, Tokyo No. 5-16 Organo Corporation

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 原水タンクと、加圧ポンプを介装してな
り前記原水タンク内の原水を逆浸透膜装置に加圧送給す
る送給パイプと、加圧送給された原水を透過水と濃縮水
とに分離して取り出す逆浸透膜装置と、前記逆浸透膜装
置から取り出される濃縮水を原水タンクに返送する循環
パイプとからなる淡水製造装置において、前記逆浸透膜
装置の透過水取出し部に透過水の流量を検出する流量検
出器を設けると共に、前記循環パイプに流量調節弁を介
装してなり、前記流量検出器の検出信号に基づいて前記
流量調節弁の開度を制御して逆浸透膜装置の供給水圧を
調節することにより逆浸透膜装置の透過水量を所定量と
することを特徴とする淡水製造装置。
1. A raw water tank, a feed pipe for interposing a pressure pump to feed the raw water in the raw water tank to a reverse osmosis membrane device under pressure, and the raw water fed under pressure is concentrated with permeate. A reverse osmosis membrane device that separates and extracts water, and a circulating water pipe that returns concentrated water extracted from the reverse osmosis membrane device to a raw water tank, in a permeated water extraction part of the reverse osmosis membrane device. A flow rate detector for detecting the flow rate of permeated water is provided, and a flow rate control valve is provided in the circulation pipe, and the opening of the flow rate control valve is controlled based on the detection signal of the flow rate detector to reverse the flow rate. A fresh water producing apparatus characterized in that the permeated water amount of a reverse osmosis membrane device is adjusted to a predetermined amount by adjusting the supply water pressure of the osmotic membrane device.
【請求項2】 送給パイプに原水の塩濃度を検出する濃
度検出器を設け、循環パイプの流量調節弁と原水タンク
との間において遮断弁を介装すると共に、循環パイプの
前記流量調節弁と遮断弁との間において排出弁を介装し
た排出管を連結するか、当該遮断弁に換えて、排出口を
有する三方弁を付設してなり、前記濃度検出器で検出さ
れた原水の塩濃度が所定値以上になると濃度検出器の信
号に基づいて前記遮断弁を閉じると共に排出弁を開く
か、又は前記三方弁の排出口を開いて濃縮水を排出管か
ら排出する請求項1に記載の淡水製造装置。
2. A concentration detector for detecting the salt concentration of raw water is provided in the feed pipe, a shutoff valve is provided between the flow control valve of the circulation pipe and the raw water tank, and the flow control valve of the circulation pipe is provided. And a shut-off valve are connected to a drain pipe with a drain valve interposed therebetween, or a three-way valve having a drain port is attached instead of the shut-off valve, and salt of raw water detected by the concentration detector is attached. The concentrated water is discharged from the discharge pipe by closing the shutoff valve and opening the discharge valve or opening the discharge port of the three-way valve based on a signal from the concentration detector when the concentration becomes a predetermined value or more. Fresh water production equipment.
【請求項3】 請求項1又は2に記載の淡水製造装置の
電源として太陽電池モジュールを使用し、この太陽電池
モジュールに集水手段を設けると共に、前記集水手段と
原水タンクとを導水管で連結してなり、モジュール上面
で受けた雨水を前記集水手段及び導水管を介して原水タ
ンクへ供給することを特徴とする淡水製造装置。
3. A solar cell module is used as a power source of the fresh water producing apparatus according to claim 1 or 2, and the solar cell module is provided with water collecting means, and the water collecting means and the raw water tank are connected by a water conduit. A fresh water producing apparatus characterized in that the rain water received by the upper surface of the module is connected to the raw water tank via the water collecting means and the water conduit.
JP21859193A 1993-09-02 1993-09-02 Freshwater production equipment Expired - Fee Related JP3270211B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21859193A JP3270211B2 (en) 1993-09-02 1993-09-02 Freshwater production equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21859193A JP3270211B2 (en) 1993-09-02 1993-09-02 Freshwater production equipment

Publications (2)

Publication Number Publication Date
JPH0768257A true JPH0768257A (en) 1995-03-14
JP3270211B2 JP3270211B2 (en) 2002-04-02

Family

ID=16722362

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21859193A Expired - Fee Related JP3270211B2 (en) 1993-09-02 1993-09-02 Freshwater production equipment

Country Status (1)

Country Link
JP (1) JP3270211B2 (en)

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996041675A1 (en) * 1995-06-08 1996-12-27 Schael Wilfried Process and device for controlling a reverse osmosis system for water treatment
WO1998052874A3 (en) * 1997-05-20 1999-03-25 United States Filter Corp Water treatment system having dosing control
US5919357A (en) * 1997-05-20 1999-07-06 United States Filter Corporation Filter cartridge assembly
WO2003033120A1 (en) * 2001-10-15 2003-04-24 Scilog, Inc. Method and apparatus for enhancing filtration yields in tangential flow filtration
US7410587B2 (en) 2004-08-03 2008-08-12 Scilog, Inc. Liquid handling for filtration and preparative chromatography
KR101334651B1 (en) * 2012-08-14 2013-11-29 한국수자원공사 Apparatus for water purification without water storage tank and method for water purification using the same
JP5606615B1 (en) * 2013-12-05 2014-10-15 三菱重工業株式会社 Membrane separator, circulating water utilization system
WO2015083773A1 (en) * 2013-12-05 2015-06-11 三菱重工業株式会社 Membrane separation device, circulated water utilization system
US9611161B2 (en) 2013-12-05 2017-04-04 Mitsubishi Hitachi Power Systems, Ltd. Circulating water utilization system
US9783963B2 (en) 2013-12-05 2017-10-10 Mitsubishi Hitachi Power Systems, Ltd. Safety device for circulating water utilization system and circulating-water utilization system
JP2018034129A (en) * 2016-09-01 2018-03-08 株式会社トップウォーターシステムズ Water purifier
US10315930B2 (en) 2013-12-05 2019-06-11 Mitsubishi Hitachi Power Systems, Ltd. Method and system for remotely monitoring a group of circulating-water utilization systems
CN110770176A (en) * 2017-06-15 2020-02-07 甘布罗伦迪亚股份公司 Water purification apparatus and method for controlling at least one fluid property in a water purification apparatus
US10997673B2 (en) 2013-12-05 2021-05-04 Wota Group Llc Charging device of circulating water utilization system and circulating-water utilization system
JP2022010263A (en) * 2017-07-21 2022-01-14 オルガノ株式会社 Membrane filtration device

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103748040B (en) 2011-08-24 2016-05-11 东丽株式会社 Fresh water generation method

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1996041675A1 (en) * 1995-06-08 1996-12-27 Schael Wilfried Process and device for controlling a reverse osmosis system for water treatment
WO1998052874A3 (en) * 1997-05-20 1999-03-25 United States Filter Corp Water treatment system having dosing control
US5919357A (en) * 1997-05-20 1999-07-06 United States Filter Corporation Filter cartridge assembly
US5925240A (en) * 1997-05-20 1999-07-20 United States Filter Corporation Water treatment system having dosing control
US6607669B2 (en) 2000-06-23 2003-08-19 Scilog, Inc. Method and apparatus for enhancing filtration yields in tangential flow filtration
WO2003033120A1 (en) * 2001-10-15 2003-04-24 Scilog, Inc. Method and apparatus for enhancing filtration yields in tangential flow filtration
US7410587B2 (en) 2004-08-03 2008-08-12 Scilog, Inc. Liquid handling for filtration and preparative chromatography
KR101334651B1 (en) * 2012-08-14 2013-11-29 한국수자원공사 Apparatus for water purification without water storage tank and method for water purification using the same
JP5606615B1 (en) * 2013-12-05 2014-10-15 三菱重工業株式会社 Membrane separator, circulating water utilization system
WO2015083783A1 (en) * 2013-12-05 2015-06-11 三菱重工業株式会社 Membrane separation device, circulated water utilization system
WO2015083773A1 (en) * 2013-12-05 2015-06-11 三菱重工業株式会社 Membrane separation device, circulated water utilization system
US9611161B2 (en) 2013-12-05 2017-04-04 Mitsubishi Hitachi Power Systems, Ltd. Circulating water utilization system
US9783963B2 (en) 2013-12-05 2017-10-10 Mitsubishi Hitachi Power Systems, Ltd. Safety device for circulating water utilization system and circulating-water utilization system
US10315930B2 (en) 2013-12-05 2019-06-11 Mitsubishi Hitachi Power Systems, Ltd. Method and system for remotely monitoring a group of circulating-water utilization systems
US10997673B2 (en) 2013-12-05 2021-05-04 Wota Group Llc Charging device of circulating water utilization system and circulating-water utilization system
JP2018034129A (en) * 2016-09-01 2018-03-08 株式会社トップウォーターシステムズ Water purifier
CN110770176A (en) * 2017-06-15 2020-02-07 甘布罗伦迪亚股份公司 Water purification apparatus and method for controlling at least one fluid property in a water purification apparatus
CN110770176B (en) * 2017-06-15 2022-12-30 巴克斯特国际公司 Water purification apparatus and method for controlling at least one fluid property in a water purification apparatus
JP2022010263A (en) * 2017-07-21 2022-01-14 オルガノ株式会社 Membrane filtration device

Also Published As

Publication number Publication date
JP3270211B2 (en) 2002-04-02

Similar Documents

Publication Publication Date Title
JPH0768257A (en) Fresh water producing apparatus
US20040168978A1 (en) Method and apparatus for recirculating tangential separation system
CN201164379Y (en) Water-saving type RO drinking fountain
WO2022121678A1 (en) Water purification system, water purifier, and water purifier control method
CN100379687C (en) Water purification system
CN101597111B (en) Quality-separation water clarifier with water purification function
EP1289632B1 (en) Method and device for purifying water
KR101682756B1 (en) Rainwater recycle apparatus having initial rainwater processing means
CN210595635U (en) Drinking water treatment device
US20050087492A1 (en) Reverse osmosis water filtering system
CN109336305B (en) Time-delay stop type household water purifying device and household water purifier
CN218089142U (en) Two-stage water purifying device
CN208603872U (en) A kind of micro- waste water water purification system
CN106830463A (en) A kind of rainwater advanced purification treatment system
CN207957955U (en) A kind of water treatment facilities peculiar to vessel
US20160288021A1 (en) System for processing food process waste water including purification and optional recycling of purified waste water
CN207108696U (en) A kind of rainwater advanced purification treatment system
RU2199377C1 (en) Membrane plant for separation of solutions
CN205367938U (en) Intelligence sea water, rain water purifying equipment
CN212334821U (en) Internal pressure type ultrafiltration water purification equipment
CN207957962U (en) Reverse osmosis purified water processing system
CN209178157U (en) A kind of household water purifier and domestic water purifying machine that water quality is controllable
CN207581494U (en) A kind of automatic emptier for reverse osmosis drinking machine
CN107142993B (en) Intelligent negative-pressure-free multi-path quality-divided water supply equipment and water supply method thereof
CN209397040U (en) A kind of water purification machine waste strength regulating device

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

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

Free format text: PAYMENT UNTIL: 20080118

Year of fee payment: 6

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

Year of fee payment: 7

Free format text: PAYMENT UNTIL: 20090118

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

Free format text: PAYMENT UNTIL: 20090118

Year of fee payment: 7

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

Free format text: PAYMENT UNTIL: 20100118

Year of fee payment: 8

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

Free format text: PAYMENT UNTIL: 20100118

Year of fee payment: 8

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

Year of fee payment: 9

Free format text: PAYMENT UNTIL: 20110118

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

Free format text: PAYMENT UNTIL: 20110118

Year of fee payment: 9

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

Year of fee payment: 10

Free format text: PAYMENT UNTIL: 20120118

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

Free format text: PAYMENT UNTIL: 20130118

Year of fee payment: 11

LAPS Cancellation because of no payment of annual fees