JPS60932A - Supplying device of ultrapure water - Google Patents

Supplying device of ultrapure water

Info

Publication number
JPS60932A
JPS60932A JP9491383A JP9491383A JPS60932A JP S60932 A JPS60932 A JP S60932A JP 9491383 A JP9491383 A JP 9491383A JP 9491383 A JP9491383 A JP 9491383A JP S60932 A JPS60932 A JP S60932A
Authority
JP
Japan
Prior art keywords
ultrapure water
steam
storage tank
sterile filter
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
JP9491383A
Other languages
Japanese (ja)
Other versions
JPS632232B2 (en
Inventor
Kenichiro Noda
野田 謙一郎
Toru Kawachi
河内 透
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries 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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP9491383A priority Critical patent/JPS60932A/en
Publication of JPS60932A publication Critical patent/JPS60932A/en
Publication of JPS632232B2 publication Critical patent/JPS632232B2/ja
Granted legal-status Critical Current

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  • Apparatus For Disinfection Or Sterilisation (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To supply ultrapure water to a using position without generating deterioration of water quality, by providing a steam supply device, a sterile filter, a discharge device of drain and a throttling and discharge device within a storage tank. CONSTITUTION:The titled device is provided with a manufacturing device 1 of ultrapure water and a storage tank 2 storing the ultrapure water manufactured by the device 1 within which a steam pouring pipe 15 which is a supply device of steam for sterilization, a sterile filter 6 supplying sterilized gas and a discharge device of drain are provided and orifices 8, 13 which are discharge devices for throttling and discharge of steam for sterilization are provided on the discharge device of drain and the sterile filter 6. With this construction, the storage tank 2 and the sterile filter 6 are sterilized jointly by steam and the ultrapure water is supplied to a using position 4 from the storage tank 2 through a duct 3 without deteriorating water quality.

Description

【発明の詳細な説明】 この発明は超純水供給装置に関する。純度の高い水は電
子工業用洗浄水、医薬用水、原子力用水に用いらnる。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an ultrapure water supply device. Highly purified water is used for cleaning water for the electronic industry, water for medicine, and water for nuclear power.

しかも、近年はこれらの工業の高酸化に伴い純度が理論
純水に近い超純水が要求されている。
Moreover, in recent years, with the high oxidation of these industries, there has been a demand for ultrapure water whose purity is close to theoretically pure water.

超純水は限外濾過膜装置、逆浸透膜装置などの膜分離装
置やイオン交換樹脂装置tfC,はこれらの組合せから
なる超純水製造装置で製造してタンクに貯蔵し、タンク
から管路により使用個所へ供給する。しかし、使用個所
で使用中に使用個所から細菌が進入して純度を低下する
ことがあると共に、場合によっては製造装置そのものも
細菌で汚染されることがあり、そうなると使用箇所での
用水は満足すべきものではなくなシ、この用水を用いる
プロセス側では製品の歩留の低下と言う不都合が生じる
。そして、製造装置が一旦汚染されると高純度の水はな
かなか製造できなくなる。
Ultrapure water is produced by ultrapure water production equipment consisting of a combination of membrane separation equipment such as ultrafiltration membrane equipment and reverse osmosis membrane equipment, and ion exchange resin equipment tfC, and is stored in tanks, and from the tanks to pipes. Supplied to the point of use. However, bacteria may enter the area during use and reduce purity, and in some cases, the manufacturing equipment itself may become contaminated with bacteria. However, in processes that use this water, there is an inconvenience that the yield of products decreases. Once the production equipment becomes contaminated, it becomes difficult to produce highly purified water.

このため従来は一週間に一回位の割合いで貯蔵タンク中
の水を空け、内部を蒸気で洗浄し滅菌しているが、タン
ク内部を大気に開放するためタンクに設けである無菌エ
アフィルタ(細菌をタンク内に入れないフィルタ)の滅
菌が同時に行えないので、このフィルタは外して別に蒸
気で洗浄しなければならず、非常に手数がか\る。
For this reason, conventionally the water in the storage tank is emptied about once a week and the inside is cleaned and sterilized with steam, but in order to open the inside of the tank to the atmosphere, a sterile air filter ( Since the filter (which prevents bacteria from entering the tank) cannot be sterilized at the same time, this filter must be removed and cleaned separately with steam, which is very time-consuming.

そこで本発明はこの貯蔵タンクを付属の無菌エアフィル
タ、と−緒に蒸気で滅菌できる様に改良したのであって
、以下、図示の実施例を参照して説明する。
Therefore, the present invention has improved this storage tank so that it can be sterilized with steam together with an attached sterile air filter, and will be described below with reference to the illustrated embodiment.

lは前述した超純水製造装置、コは上記製造装置が製造
した超純水を貯蔵する貯蔵タンク、3はタンク中の超純
水をポンプPで使用箇所ダに導く管路を示す。
1 is the above-mentioned ultrapure water production device, 3 is a storage tank for storing the ultrapure water produced by the above production device, and 3 is a pipe line for guiding the ultrapure water in the tank to the point of use D by a pump P.

貯蔵タンクのはソ頂部には通気管3が立ち、その上端に
は無菌エアフィルタ6が設けである。
A ventilation pipe 3 stands at the top of the storage tank, and a sterile air filter 6 is provided at its upper end.

無菌エアフィルタは通気管5の上端が内部に連通したフ
ィルタエレメント6αと、エレメントAaV!を有する
排気管7と、弁■2とオリフィスgを有する絞り排気管
9と、弁v3を有する圧縮空気などの気体圧入管10を
接続しである。
The sterile air filter includes a filter element 6α with the upper end of the ventilation pipe 5 communicating with the inside, and an element AaV! An exhaust pipe 7 having a valve 2 and an orifice g, a throttle exhaust pipe 9 having a valve v3, and a gas injection pipe 10 for compressed air or the like having a valve v3 are connected.

両排気管7,9は別々にケースに接続せず、図示の様に
どちらか一方をケースに接続し、その弁の手前に他方を
連結してもよい。又、例えば両排気管り、9の一方或い
は双方は気体圧入’f110の弁V8の手前に連結した
り、逆に気体圧入管/θをどちらの排気管7,9の弁の
手前に連結してもよい。
The exhaust pipes 7 and 9 may not be connected to the case separately, but one of them may be connected to the case as shown in the figure, and the other may be connected in front of the valve. Also, for example, one or both of the exhaust pipes 9 can be connected in front of the valve V8 of the gas injection pipe 'f110, or conversely, the gas injection pipe /θ can be connected in front of the valve of either exhaust pipe 7 or 9. You can.

又、貯蔵タンクの底には排水弁//と、スチームトラッ
プ/コと、オリフィス/3とを接続する。
Also, a drain valve//, a steam trap/3, and an orifice/3 are connected to the bottom of the storage tank.

この王者はスチームトラップとオリフィスには夫々弁を
設け、個々にタンクの底に接続してもよいが、図示の如
く並列にし、弁■4を介してタンクの底に接続してもよ
く、その場合、導管3の上流端部にも弁Vllを設け、
タンクの底に接続したドレン管/グに弁v4と弁V、を
分岐状に連結すると最も簡単である。
In this champion, the steam trap and orifice each have a valve and can be connected to the bottom of the tank individually, but they can also be connected in parallel as shown in the figure and connected to the bottom of the tank via valve 4. In this case, a valve Vll is also provided at the upstream end of the conduit 3,
It is easiest to connect valves V4 and V in a branched manner to a drain pipe connected to the bottom of the tank.

貯蔵タンク中に蒸気を圧入するための弁v6を有する蒸
気注入管/Sを設ける。この実施例では蒸気注入管/S
は通気管5に接続しであるが、勿論、タンクコに直接接
続してもよい。そして、製造装Rtが製造した超純水を
貯蔵タンクに補給する補給管/6にはタンク中を洗浄す
る際に閉じる弁■を設ける。
A steam injection pipe/S is provided with a valve v6 for pressurizing steam into the storage tank. In this example, the steam injection pipe/S
is connected to the ventilation pipe 5, but it may of course be connected directly to the tank. The replenishment pipe /6 for replenishing the storage tank with the ultrapure water produced by the manufacturing equipment Rt is provided with a valve (2) that is closed when cleaning the inside of the tank.

これにより常時は弁V、 、 V、 、 V、を介して
使用個所グに超純水を供給することができる。尚、v3
を介して貯蔵タンクの内部は無菌フィルタ6を通じ大気
圧よりも常時高い圧力になる様に無菌気体で加圧状態を
維持する様にする。
As a result, ultrapure water can always be supplied to the point of use via the valves V, , V, , V. Furthermore, v3
The interior of the storage tank is maintained under pressure with sterile gas through a sterile filter 6 so that the pressure is always higher than atmospheric pressure.

貯蔵タンク中を洗浄するにはタンク内の水を排水するた
めに弁Vい排水弁/lを開くと共に、必要に応じ弁V、
も開き圧縮気体(空気)で気体圧入管10.無菌フィル
タ6、通気管Sを通じタンク内上部空間に圧入し、水面
を上から加圧して排水を促進することができる。尚、そ
の他の弁は閉じて置く。タンクから排水した水は超純水
製造装置/の原水タンクに戻し、超純水製造装置の原料
水に利用する。
To clean the inside of the storage tank, open the drain valve/l to drain the water in the tank, and open the valve V, if necessary.
Also open the gas injection tube 10 with compressed gas (air). The sterile filter 6 is press-fitted into the upper space of the tank through the ventilation pipe S, and the water surface can be pressurized from above to promote drainage. In addition, keep the other valves closed. The water drained from the tank is returned to the raw water tank of the ultrapure water production equipment and used as raw water for the ultrapure water production equipment.

貯蔵タンク中の水の排水が完了したら、次には弁■6を
開き、タンク内に蒸気注入管ノ(から蒸気を注入して滅
菌を行う。この場合、タンク、無菌フィルタ、これらに
接続した管内に空気が残存し、空気溜が生じていると、
蒸気は空気に障害されて空気溜と接触する面を滅菌する
ことができないので、滅菌に先立って空気を完全に駆出
することか好ましい。
Once the water in the storage tank has been drained, open valve 6 and inject steam into the tank through the steam injection pipe to sterilize the tank. If air remains in the pipe and an air pocket is created,
It is preferable to completely evacuate the air prior to sterilization, since steam cannot sterilize surfaces in contact with the air reservoir due to air interference.

それには蒸気注入管/!rの弁v6だけを開いて蒸気を
入れ、貯蔵タンク、無菌フィルタ、これらに接続する管
内に夫々弁の前までを蒸気で充満し、蒸気加圧を行い、
それから弁v4と排水弁//だけを開き、内部の蒸気を
排気し、内部圧力を開放する。この工程を1回ないし数
回行うことによシ内部に残存していた空気は蒸気と一緒
に排水弁//から完全に排出される。
Steam injection pipe for that! Open only valve v6 of r to let in steam, fill the storage tank, sterile filter, and pipes connected to these with steam up to the front of each valve, and pressurize the steam.
Then, only valve v4 and drain valve // are opened to exhaust the internal steam and release the internal pressure. By repeating this step once or several times, the air remaining inside is completely discharged from the drain valve along with the steam.

蒸気滅菌を行うには蒸気注入管15の弁■6を開くと共
に、弁■、と弁v4を開く。これにより注入された蒸気
は弁■、とオリフィスざ、弁V4とオリフイス/3、ス
チームトラップ/2を通じて排出され、貯蔵タンク、通
気管S、無菌フィルタ6を同時に滅菌する。
To perform steam sterilization, open valve (6) of the steam injection pipe 15, and open valve (2) and valve (v4). As a result, the injected steam is discharged through the valve (1), the orifice (V4), the orifice (3), and the steam trap (2), thereby sterilizing the storage tank, the ventilation pipe (S), and the sterile filter (6) at the same time.

蒸気滅菌が終了したら、気体圧入管10の弁v3を開い
て圧縮空気を無菌フィルタ6、通気管Sを経て貯蔵タン
ク3に入れ、弁v4、排気弁//を開いて排出し、これ
により無菌フィルタとタンクを冷却する。そして、冷却
したら補給管/6の弁■、を開いてタンク中に超純水を
補給し、弁■。
When steam sterilization is completed, open valve v3 of gas injection pipe 10 to introduce compressed air into storage tank 3 through sterile filter 6 and ventilation pipe S, and open valve v4 and exhaust valve // to discharge the air, thereby sterilizing the air. Cool the filter and tank. Then, once it has cooled, open the supply pipe/valve 6 and replenish the tank with ultrapure water, then turn on the valve ■.

■、を開いてその超純水を管路3に流し、使用個所ダで
取出せる様にする。
②Open it and let the ultrapure water flow into the pipe 3 so that it can be taken out at the point of use.

弁V、からV♂と、排水弁//は例えば電磁式の開閉弁
で構成し、上述の動作を全自動とすることができる。) 以上の実施例の説明で明らかな如く本発明によれば無菌
フィルタ乙にはオリフィスざが接続してあり、又、タン
ク3の底にもオリフィス/3を接続しである。このため
蒸気滅菌工程の際に注入した蒸気がこjらのオリフィス
ざ、 /J ヲ通じ外に出られる様にすることにより貯
蔵タンクと無菌フィルタを同時に滅菌でき、無菌フィル
タを外して別に滅菌する手数が解消する。
The valves V to V♂ and the drain valve // are constituted by electromagnetic on-off valves, for example, and the above-mentioned operation can be made fully automatic. ) As is clear from the above description of the embodiments, according to the present invention, an orifice is connected to the sterile filter B, and an orifice /3 is also connected to the bottom of the tank 3. Therefore, by allowing the steam injected during the steam sterilization process to exit through these orifices, the storage tank and sterile filter can be sterilized at the same time, and the sterile filter can be removed and sterilized separately. The hassle is eliminated.

又、本発明はこれに限らず、例えば弁vIと排水弁//
を開閉弁にしないで開度を調整できる調整弁とし、蒸気
滅菌工程の際に開度をオリフィスと同様に小さく調整す
れば、この調整弁を通じ絞って蒸気を逃出させ同様に貯
蔵タンクと無菌フィルタを同時に滅菌することができる
Further, the present invention is not limited to this, and for example, the valve vI and the drain valve//
If you use a regulating valve that can adjust the opening degree without using an on-off valve, and adjust the opening degree to a small value like an orifice during the steam sterilization process, the steam will be squeezed through this regulating valve and sterilized. Filters can be sterilized at the same time.

こうして本発明によれば超純水の貯蔵タンクと付属の無
菌フィルタを容易且つ完全に滅菌処理することにより、
これから使用箇所に供給される超純水の水質低下を起こ
さない様にすることができろう そして、本発明は装置全体を新設する場合以外に、既存
の装置を改造して簡単に実施することもできる。
Thus, according to the present invention, by easily and completely sterilizing the ultrapure water storage tank and the attached sterile filter,
It will be possible to prevent the quality of ultrapure water that will be supplied to the point of use from now on to deteriorate.In addition to installing the entire device, the present invention can also be easily implemented by modifying an existing device. can.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は本発明の一実施例を示すフローシートで、図中、
lは超純水製造装置、コは貯蔵タンク、3は管路、lI
は使用箇所、乙は無菌フィルタ、/lIはドレン管、g
と/3は絞り排出手段として例示したオリフィス、lS
は蒸気注入管を示す。
The drawing is a flow sheet showing an embodiment of the present invention, and in the drawing,
l is ultrapure water production equipment, ko is storage tank, 3 is pipe, lI
is the location where it is used, O is the sterile filter, /I is the drain pipe, g
and /3 is an orifice exemplified as a throttle ejection means, lS
indicates a steam injection pipe.

Claims (1)

【特許請求の範囲】 (1)超純水製造装置と、超純水製造装置が製造した超
純水の貯蔵タンクと、貯蔵タンクから使用箇所に超純水
を導く管路とからなる超純水供給装置において、 上記貯蔵タンクには滅菌用の蒸気供給手段と、無菌気体
を供給する無菌フィルタと、ドレン排出手段を設け、ド
レン排出手段と、無菌フィルタには滅菌用蒸気を絞って
排出するための絞り排出手段を夫々備えさせたことを特
徴とする超純水供給装置。 (2、特許請求の範囲(1)の装置において、ドレン排
出手段と無菌フィルタの絞シ排出手段はオリフィスであ
る超純水供給装置。 (3)%許請求の範囲(1)の装置においてドレン排出
手段と無菌フィルタの絞り排出手段は開度の調整可能な
弁である超純水供給装置。
[Scope of Claims] (1) Ultrapure water comprising an ultrapure water production device, a storage tank for the ultrapure water produced by the ultrapure water production device, and a pipe line leading the ultrapure water from the storage tank to the point of use. In the water supply device, the storage tank is provided with a sterilizing steam supply means, a sterile filter for supplying sterile gas, and a drain discharge means, and the sterilization steam is squeezed and discharged into the drain discharge means and the sterile filter. An ultrapure water supply device characterized in that it is equipped with a throttle discharge means for each purpose. (2. In the device according to claim (1), the drain discharge means and the sterile filter constriction discharge means are orifices. The discharge means and sterile filter throttle discharge means is an ultrapure water supply device whose opening degree can be adjusted.
JP9491383A 1983-05-31 1983-05-31 Supplying device of ultrapure water Granted JPS60932A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9491383A JPS60932A (en) 1983-05-31 1983-05-31 Supplying device of ultrapure water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9491383A JPS60932A (en) 1983-05-31 1983-05-31 Supplying device of ultrapure water

Publications (2)

Publication Number Publication Date
JPS60932A true JPS60932A (en) 1985-01-07
JPS632232B2 JPS632232B2 (en) 1988-01-18

Family

ID=14123241

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9491383A Granted JPS60932A (en) 1983-05-31 1983-05-31 Supplying device of ultrapure water

Country Status (1)

Country Link
JP (1) JPS60932A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05167984A (en) * 1991-12-13 1993-07-02 Sanyo Electric Co Ltd Generating circuit for video head switching signal

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
JOURNAL OF PARENTERAL SCIENCE AND TECHNOLOGY=1981 *
JOURNAL OF PARENTERAL SCIENCE AND TECHNOLOGY=1982 *
PHARMACEUTICAL TECHNOLOGY=1978 *

Also Published As

Publication number Publication date
JPS632232B2 (en) 1988-01-18

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