JPS60882A - Ultrapure water production equipment - Google Patents
Ultrapure water production equipmentInfo
- Publication number
- JPS60882A JPS60882A JP9491283A JP9491283A JPS60882A JP S60882 A JPS60882 A JP S60882A JP 9491283 A JP9491283 A JP 9491283A JP 9491283 A JP9491283 A JP 9491283A JP S60882 A JPS60882 A JP S60882A
- Authority
- JP
- Japan
- Prior art keywords
- water
- water supply
- valve
- membrane
- valves
- 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
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
□ この発明は超純水製造装置に関する。純度の商い水
は電子工業用洗浄水、医薬用水、原子力用水に用いられ
る。しかも、近年はこれらの工業の高度化に伴いま−j
ます純度が理論純水に近い超純水が要求されている。[Detailed Description of the Invention] □ This invention relates to an ultrapure water production device. Purity commercial water is used for cleaning water for the electronic industry, water for medicine, and water for nuclear power. Moreover, in recent years, as these industries have become more sophisticated,
Ultrapure water with purity close to theoretically pure water is increasingly required.
超純水は限外p過膜装置、逆浸透膜装置などの膜分離装
置やイオン交換樹脂装置またはこれらの組合せからなる
超純水製造装置で製造して貯蔵タンクに貯蔵し、タンク
から管路によシ使用個所へ供給する。Ultrapure water is produced by an ultrapure water production device consisting of a membrane separation device such as an ultrapolar membrane device or a reverse osmosis membrane device, an ion exchange resin device, or a combination of these devices, stored in a storage tank, and then passed through a pipe from the tank. Supply it to the place where it is used.
一般にこれらの膜分離装置の運転は、貯蔵タンク内の水
位によって制御し、貯蔵タンク内の水位が高くなって超
純水が充分に力ると膜分離装置の運転を中断し、使用箇
所で成る8度超純水が取出されてタンク内の水位が低く
なると運転を再開する。この運転停止時に(グ膜分離装
置は圧力h」放状態になるので、例えば膜分離装置が排
出する濃縮水の排出管の先端が外気に触nでいると、空
気中の細菌が排出管から速入し、膜分離装置は細附で汚
染されることがある。そうすると膜分離装置は使用箇所
が滴定する水質の超純水を製造できなくなシ、この水含
用いるプロセスクリでは製品の歩留の低下と言う不都合
が生じる。又、製造装置は一旦細菌で汚染されると高純
度の水になかなか製造できなくなる。In general, the operation of these membrane separation devices is controlled by the water level in the storage tank, and when the water level in the storage tank becomes high and the ultrapure water becomes sufficiently strong, the operation of the membrane separation device is interrupted and the operation is stopped at the point of use. When 8 degrees of ultrapure water is taken out and the water level in the tank becomes low, operation will resume. When this operation is stopped, the membrane separator releases pressure h, so for example, if the tip of the discharge pipe of the concentrated water discharged by the membrane separator comes into contact with the outside air, bacteria in the air will come out of the discharge pipe. This can cause the membrane separator to become contaminated with small particles, making it impossible for the membrane separator to produce ultrapure water of the water quality that is titrated at the point of use, and for process chemicals containing water to In addition, once the production equipment becomes contaminated with bacteria, it becomes difficult to produce highly purified water.
このため、従来は一週間に1回位の割合で膜分離装置全
薬剤で滅菌し、細菌による汚染を防止しているが、滅菌
中に超純水を製造できないので、使用箇所では超純水の
使用に制約を受ける。For this reason, conventionally, membrane separation equipment is sterilized with all chemicals once a week to prevent bacterial contamination, but since ultrapure water cannot be produced during sterilization, ultrapure water is used at the point of use. be restricted in its use.
又、そうしないためには膜分離装置を二基設置し、一方
の滅菌中は他方で超純水を製造すればよいが、そのため
にはコストが高くなる。In order to avoid this, two membrane separation devices may be installed, and while one is sterilizing, ultrapure water can be produced in the other, but this increases the cost.
そこで本発明は膜分離装置の運転を停止した場合、装置
内を陽圧、つまり加圧状態に保ち、これにより細菌が速
入するのを防止する様にしたのであって、こnによシ実
験の結果では装置を滅菌後、6ケ月以上滅菌を行わなく
ても装置な無菌状態に維持でき、頻繁に滅菌を実施する
手数、使用箇所での超純水の使用の制約を解消すると共
に、装置上二基設置する無駄を省ける。Therefore, in the present invention, when the operation of the membrane separation device is stopped, the inside of the device is maintained at a positive pressure, that is, a pressurized state, thereby preventing bacteria from entering quickly. Experimental results show that after sterilization, the device can be maintained in a sterile state for more than 6 months without sterilization, eliminating the need for frequent sterilization and restrictions on the use of ultrapure water at the point of use. Eliminates the waste of installing two units on the device.
以下、図示の一実施例を参照して説明する。Hereinafter, a description will be given with reference to one embodiment shown in the drawings.
lは限外p過膜装置、逆浸透膜装置などの膜分離装置で
、イオン交換樹脂装置などで充分に前処理した原料水に
給水タンクに貯え、この原料水を給水管と給水ポンプ3
で膜分離装置の供給側に加圧して供給し、装置に内蔵さ
れた透過膜l′を透過し、透過側に出たものを超純水と
して補給管4で貯蔵タンクSに貯え、そこから供給管6
で使用箇所7に導く。1 is a membrane separation device such as an ultrapolar filtration membrane device or a reverse osmosis membrane device, and raw water that has been sufficiently pretreated with an ion exchange resin device is stored in a water supply tank, and this raw water is passed through a water supply pipe and a water supply pump 3.
The water is pressurized and supplied to the supply side of the membrane separator, permeates through the permeation membrane l' built into the device, and the water that comes out on the permeation side is stored as ultrapure water in the storage tank S via the supply pipe 4, and from there. Supply pipe 6
will lead you to point of use 7.
貯蔵タンク3甲には内部の水位を検出1−るレベルスイ
ッチgが突入し、タンク内の超純水の水位が高くなると
給水ポンプ3を停めて装置lの運転を中断し、又、水位
が成る程度下がると給水ポンプを駆動し、装置の運転を
再開する。A level switch g that detects the internal water level enters the storage tank 3A, and when the water level of the ultrapure water in the tank rises, the water supply pump 3 is stopped and the operation of the device l is interrupted, and the water level is When the water level drops to a certain level, the water supply pump is activated and the equipment is restarted.
前述した様に、この状態では装置が運転を停止している
とき装置内の圧力は開放状態になシ、装置の供給側に骨
らTLる娘堀水のυト串管7などの先端が大気中に露出
していると錯気甲の細菌が速入し、装置全汚呆する。As mentioned above, in this state, when the device is stopped, the pressure inside the device is not in an open state, and the tip of the skewer pipe 7, etc., which is connected to the supply side of the device, If it is exposed to the atmosphere, bacteria from the parasitic system will quickly enter the system, contaminating the entire device.
そこで不発明は補給11μ、排出貨ワに大々開閉弁v1
、v2を設け、又、給水管−には給水ポンプ3と膜分離
装置lの間に開閉弁v3と圧力スイッチio’6設け、
装置lの運転を停止する際には先ず開閉弁V+、V2を
閉じ、その後、暫くして給水ポンプ3を停めると共に開
閉弁V8f閉じ、こnによシ装置/内を陽圧に保ち、タ
ンク内の水位が成る程度下って装置の運転が再開する迄
の間、装置の内圧を圧力スイッチ10で監視し、内圧が
許容限度まで下がるとこれを検知して圧力スイッチ10
は開閉弁v3を開くと同時に給水ポンプ3を駆動し、装
置の内圧が上ったら給水ポンプJf停めると共に開閉弁
v5を閉じ、これによシ装置の内圧を維持する様にした
のである。Therefore, non-invention is replenishment 11μ, large opening/closing valve v1 for discharge goods Wa
, v2 are provided, and the water supply pipe is provided with an on-off valve v3 and a pressure switch io'6 between the water supply pump 3 and the membrane separation device l,
When stopping the operation of the device 1, first close the on-off valves V+ and V2, and then, after a while, stop the water supply pump 3 and close the on-off valve V8f, thereby keeping the inside of the device at positive pressure and opening the tank. The pressure switch 10 monitors the internal pressure of the device until the water level inside the device falls to a certain level and the device resumes operation. When the internal pressure drops to the allowable limit, it is detected and the pressure switch 10
When the on-off valve v3 is opened, the water supply pump 3 is driven at the same time, and when the internal pressure of the apparatus rises, the water supply pump Jf is stopped and the on-off valve v5 is closed, thereby maintaining the internal pressure of the apparatus.
このために開閉弁V+ 、V2 、VBは電磁式等の自
動−fff用い、給水ポンプJのモータ、レベルスイッ
チg1圧力スイッチ10と共に制御装置l/に電気的に
接続し、制御装置はレベルスイッチざがら装置の運転停
止の信号を受けると開閉弁v1、V2’ir−閉にし、
給水ボンダのモータの停止と開閉弁v8の閑は開閉弁V
+ 、 V2の閉の後、タイマーなどで所定時間経過し
てから行うが、或いは圧力スイッチioが上限の圧力を
検出したときに行う←にする。そして、内圧が圧力スイ
ッチ/θの下限(例えばθ、!;14/cM)まで下が
ると制御装置は圧力スイッチの上限に戻るまで開閉弁V
、f開き、給水ポンプのモータを駆動する。For this purpose, the on-off valves V+, V2, and VB are electrically connected to the control device l/, together with the motor of the water supply pump J, the level switch g1, the pressure switch 10, and the control device uses an automatic -fff such as an electromagnetic type. When receiving a signal to stop the operation of the device, the on-off valves v1 and V2'ir are closed,
Stopping the motor of the water supply bonder and opening the on-off valve v8 is the on-off valve V.
+ After closing V2, this is done after a predetermined time has elapsed using a timer, or when the pressure switch io detects the upper limit pressure. When the internal pressure drops to the lower limit of the pressure switch/θ (for example, θ, !; 14/cM), the control device operates the on-off valve V until it returns to the upper limit of the pressure switch.
, f opens and drives the water pump motor.
又、貯蔵タンク内の水位が下がシ、レベルスイッチgが
制#装置l/に膜分離装置の運転′f:要求する信号を
発すると制御装置は閉じている全部の開閉弁を開き、給
水ポンプのモータを駆動して膜分離装置に運転を再開さ
せる。In addition, when the water level in the storage tank drops, the level switch g sends a request signal to the control device l/ to operate the membrane separator, and the control device opens all the shut-off valves that are closed and starts water supply. Drive the pump motor to restart the membrane separation device.
以上で明らかな様に本発明は装置の運転停止時には開閉
弁v、、v2、vi で閉じらnた内部は加圧状態に維
持さnているため、この圧力によシ細菌は内部に侵入で
きず、頻繁に滅菌しないでも無菌状態を保ち、超純水製
造装置中、膜分離装置を細菌、の汚染から防謹すること
ができる。As is clear from the above, in the present invention, when the device is stopped, the interior, which is closed by the on-off valves v, , v2, and vi, is maintained in a pressurized state, and this pressure allows bacteria to enter the interior. It is possible to maintain a sterile state without frequent sterilization, and to prevent bacterial contamination of the membrane separation device in ultrapure water production equipment.
尚、本発明は新設の装置に実施する以外に、既存の装置
を改造して実施することもできる。又、圧力スイッチI
Oは給水管に設けることに限定されず、補給管ダや排水
管デの開閉弁と膜分離装置の間に設けてもよい。In addition to implementing the present invention in a newly installed device, the present invention can also be implemented by modifying an existing device. Also, pressure switch I
O is not limited to being provided in the water supply pipe, but may be provided between the on-off valve of the supply pipe or drain pipe and the membrane separation device.
図面は本発明の一実施例のフローシートで、図中、lは
膜分離装置、l′はその透過膜、コは給水管、3は給水
ポンプ、qは補給管、9は排水管、IOは圧力検出手段
で6.b圧力スイッチ、1/は制御装置、V+ 、 V
2、vsは開閉弁を示す。The drawing is a flow sheet of one embodiment of the present invention, in which l is a membrane separation device, l' is its permeable membrane, ko is a water supply pipe, 3 is a water supply pump, q is a supply pipe, 9 is a drain pipe, IO is the pressure detection means 6. b Pressure switch, 1/ is control device, V+, V
2, vs indicates an on-off valve.
Claims (1)
装置において、 膜分離装置の供給側に接続した給水管に原料水を加圧し
て膜分離装置に供給する給水ポンプと、給水ポンプと膜
分離装置の間に開閉弁に設け、 膜分離装置の供給側から排出される濃縮水の排水管と、
膜分離装置の透過側に得られる超純水を導く補給管に夫
々開閉弁を設け、これら三つの給水管、排水管、補給管
のうち少くとも一つの管には開閉弁と膜分離装置の間に
圧力検出手段を設け、 且つ三つの開閉弁と、給水ポンプのモータと、圧力検出
手段は、給水ポンプを停める信号を受信すると補給管と
排水管の開閉弁を閉じたのち、給水管の開閉弁を閉じる
と共に給水ポンプのモータを停め、三つの開閉弁が閉じ
ているときに膜分離装置の回シの圧力の低下を圧力検出
手段が検出すると給水管の開閉弁を開くと共に給水ポン
プのモータを駆動する制御装置に接続したことを特徴と
する超純水製造装置。 (2、特許請求の範囲(1)の装置において、補給管と
排水管の開閉弁を閉じたのち給水管の開閉弁を閑じ且つ
給水ポンプのモータを停めるのは膜分離装置の回りの圧
力の高ま#)を圧力検出手段が検出して制御装置に行わ
せる超純水製造装置。(1) In an ultrapure water production device that has a membrane separation device with a built-in permeation membrane, there is a water supply pump that pressurizes raw water to the water supply pipe connected to the supply side of the membrane separation device and supplies it to the membrane separation device, and a water supply pump. and a drain pipe for concentrated water discharged from the supply side of the membrane separator;
An on-off valve is installed in each of the supply pipes that lead the ultrapure water obtained to the permeate side of the membrane separator, and at least one of these three water supply pipes, drain pipes, and supply pipes is equipped with an on-off valve and an on-off valve for the membrane separator. A pressure detection means is provided in between, and when the three on-off valves, the water supply pump motor, and the pressure detection means receive a signal to stop the water supply pump, they close the on-off valves of the supply pipe and the drain pipe, and then close the water supply pipe. When the on-off valves are closed and the water supply pump motor is stopped, and when the three on-off valves are closed and the pressure detection means detects a drop in the pressure of the membrane separator, the water supply pipe on-off valve is opened and the water supply pump motor is stopped. An ultrapure water production device characterized by being connected to a control device that drives a motor. (2. In the device according to claim (1), after closing the on-off valves of the supply pipe and drain pipe, the on-off valve of the water supply pipe is turned off and the motor of the water supply pump is stopped due to the pressure around the membrane separator. An ultrapure water production device in which a pressure detection means detects the height of #) and causes a control device to perform the operation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9491283A JPS60882A (en) | 1983-05-31 | 1983-05-31 | Ultrapure water production equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9491283A JPS60882A (en) | 1983-05-31 | 1983-05-31 | Ultrapure water production equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS60882A true JPS60882A (en) | 1985-01-05 |
Family
ID=14123217
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9491283A Pending JPS60882A (en) | 1983-05-31 | 1983-05-31 | Ultrapure water production equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60882A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60235616A (en) * | 1984-05-10 | 1985-11-22 | Asahi Chem Ind Co Ltd | Automatic stopping device of up-lift pressure in filtration apparatus |
| US4832965A (en) * | 1985-05-17 | 1989-05-23 | Helin Stig Aake | Method of making a bottle and packaging a water ration therein |
| JP2008068243A (en) * | 2006-09-15 | 2008-03-27 | Kankyo Kogaku:Kk | Water purifier |
| JP2019025391A (en) * | 2017-07-26 | 2019-02-21 | 栗田工業株式会社 | Operation method of ultrapure water production apparatus and ultrapure water production apparatus |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57144003A (en) * | 1981-03-03 | 1982-09-06 | Toyota Motor Corp | Operating method for membrane separator |
-
1983
- 1983-05-31 JP JP9491283A patent/JPS60882A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57144003A (en) * | 1981-03-03 | 1982-09-06 | Toyota Motor Corp | Operating method for membrane separator |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60235616A (en) * | 1984-05-10 | 1985-11-22 | Asahi Chem Ind Co Ltd | Automatic stopping device of up-lift pressure in filtration apparatus |
| US4832965A (en) * | 1985-05-17 | 1989-05-23 | Helin Stig Aake | Method of making a bottle and packaging a water ration therein |
| JP2008068243A (en) * | 2006-09-15 | 2008-03-27 | Kankyo Kogaku:Kk | Water purifier |
| JP2019025391A (en) * | 2017-07-26 | 2019-02-21 | 栗田工業株式会社 | Operation method of ultrapure water production apparatus and ultrapure water production apparatus |
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