JP3281238B2 - Ultrapure water supply device and sterilization method for its piping - Google Patents
Ultrapure water supply device and sterilization method for its pipingInfo
- Publication number
- JP3281238B2 JP3281238B2 JP31527895A JP31527895A JP3281238B2 JP 3281238 B2 JP3281238 B2 JP 3281238B2 JP 31527895 A JP31527895 A JP 31527895A JP 31527895 A JP31527895 A JP 31527895A JP 3281238 B2 JP3281238 B2 JP 3281238B2
- Authority
- JP
- Japan
- Prior art keywords
- pipe
- ultrapure water
- water
- pipes
- return
- 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.)
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Description
【0001】[0001]
【発明の属する技術分野】本発明は、超純水を製造する
超純水製造装置から、半導体集積回路等の製造業に係る
電子部品等の製造業、生化学工業、薬品工業などのこの
超純水を使用する装置に供給するために配管設備される
超純水供給装置、及びその配管の殺菌方法に関するもの
である。BACKGROUND OF THE INVENTION The present invention relates to an ultrapure water producing apparatus for producing ultrapure water, an ultrapure water production system for manufacturing semiconductor integrated circuits and other electronic components, a biochemical industry, a pharmaceutical industry and the like. BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an ultrapure water supply device provided with piping for supplying pure water to a device, and a method for sterilizing the piping.
【0002】[0002]
【従来技術】電子部品製造業や薬品工業等の分野で種々
の用途に使用される超純水(本明細書においては、一般
に必ずしも明確に定義分けされていない純水,超純水な
どの語で説明される高純度水を総称して「超純水」とい
う)は無菌状態で供給される必要があり、このため超純
水をその製造装置から使用装置に供給するための配管設
備は、供給水の純度低下や菌の繁殖などを防いでこの無
菌状態を維持する目的で、循環系路で超純水製造装置か
ら送水する超純水を超純水製造装置に戻す循環通水を行
いながら、その途中で複数の使用装置に適宜供給する非
滞留循環方式の構成が採用されるのが普通である(実公
昭62−34061号公報)。また、循環通水において
配管途中の管内流速を一定に保つため配管径を徐々に減
少させたり増大させたりする提案(大矢ら「純水・超純
水製造法」−要素技術と応用システム−,第179頁、
図2.5.5;昭和60年3月20日発行:幸書房、特
公平6−49187号公報)、超純水への配管からの不
純物溶出を防ぐためにPVDF等の合成樹脂材料を使用
する提案もある。2. Description of the Related Art Ultrapure water used for various applications in the fields of the electronic component manufacturing industry and the pharmaceutical industry (in this specification, terms such as pure water, High-purity water, referred to as "ultra-pure water") must be supplied under aseptic conditions, and therefore, the piping equipment for supplying ultra-pure water from its manufacturing equipment to the equipment used is In order to maintain the aseptic condition by preventing the purity of feedwater from decreasing and the propagation of bacteria, etc., circulating water is returned from the ultrapure water production equipment to the ultrapure water production equipment through the circulation system. However, it is common to adopt a non-retentive circulation type configuration that supplies a plurality of devices as needed during the process (Japanese Utility Model Publication No. Sho 62-34061). Also, in order to keep the flow velocity in the middle of the pipe constant in the circulating water flow, a proposal is made to gradually reduce or increase the pipe diameter (Oya et al., “Pure Water / Ultra Pure Water Production Method”-Element Technology and Application System-, Page 179,
Fig. 2.5.5; Published on March 20, 1985: Koshobo, JP-B-6-49187), Synthetic resin material such as PVDF is used to prevent elution of impurities from piping into ultrapure water. There are also suggestions.
【0003】このように、超純水供給のための配管設備
については、超純水製造装置で製造した高純度に精製し
た超純水をその使用目的の場所(種々の使用装置)に好
適な状態で供給するための工夫が、従来から種々提案さ
れ実施されている。[0003] As described above, with regard to the piping equipment for supplying ultrapure water, ultrapure water purified to a high purity produced by an ultrapure water production apparatus is suitable for the intended use place (various use apparatuses). Various devices for supplying in a state have been conventionally proposed and implemented.
【0004】ところで、超純水供給のための従来の配管
設備においては、長期(1ケ月〜数ケ月)にわたる連続
使用を行うと系内に菌(バクテリア)の繁殖を招くこと
は避けられない場合が多く、このため、工業的な実施設
備では定期的に超純水の供給を停止して配管系内の殺菌
洗浄を行うようにしているのが普通である。In conventional piping equipment for supplying ultrapure water, if continuous use is performed for a long period (one month to several months), it is inevitable that bacteria (bacteria) will propagate in the system. For this reason, industrial facilities generally stop the supply of ultrapure water periodically and perform sterilization and cleaning of the piping system.
【0005】しかしこの従来の配管系内の殺菌洗浄方式
においては、超純水供給の一時的な停止、したがって超
純水を使用する製造ラインの稼働を一時的に停止させる
ことが余儀なくされ、生産性の低下を招く問題となって
いた。[0005] However, in this conventional sterilization and cleaning system in the piping system, it is necessary to temporarily stop the supply of ultrapure water, and thus to temporarily stop the operation of a production line using ultrapure water. This has caused a problem of lowering the performance.
【0006】そこで、設備コストやランニングコストも
重視される工業的な設備においてこの問題を解決するた
めのいくつかの提案も従来されており、例えば、超純水
の供給停止の影響をできるだけ少なくする(すなわち製
造ラインの稼働停止期間を短かくする)目的で、超純水
中のバクテリア数を常時監視し、これが一定数に達した
ときに殺菌洗浄を行うことも考えられている。Therefore, some proposals for solving this problem have been conventionally made in industrial equipment in which equipment cost and running cost are also important. For example, the influence of stopping supply of ultrapure water is reduced as much as possible. For the purpose of shortening the downtime of the production line, the number of bacteria in ultrapure water is constantly monitored, and when the number of bacteria reaches a certain number, sterilization cleaning is considered.
【0007】[0007]
【発明が解決しようとする課題】しかし上記方法によれ
ば、バクテリアが一定程度存在することを許した用水を
使用する結果となり、例えば近年における極めて高い品
質が求められている半導体製品等の品質管理上適当でな
いし、一定品質や安全性等が高く求められる他の分野の
製品にあっても、製造ラインを停止−起動する殺菌処理
の前後において、用いる用水中のバクテリア数が変動す
ることを前提とした工業的設備の採用は問題が多い。However, according to the above-mentioned method, the use of water that permits the presence of bacteria to a certain extent results in the use of water. Even in products in other fields where constant quality and safety are highly required, it is assumed that the number of bacteria in the water used before and after the sterilization treatment that stops and starts the production line fluctuates. There are many problems with the use of industrial equipment.
【0008】本発明は以上のような従来技術の問題点を
解消することを目的としてなされたものであり、超純水
を使用する製造ライン等を停止させることなく長期にわ
たる連続稼働を可能とする超純水供給装置、及びその装
置を構成している配管内の殺菌方法を提供するところに
ある。The present invention has been made to solve the above-mentioned problems of the prior art, and enables long-term continuous operation without stopping a production line or the like using ultrapure water. It is an object of the present invention to provide an ultrapure water supply apparatus and a method for sterilizing a pipe constituting the apparatus.
【0009】また本発明の別の目的は、製造ライン等を
停止させることなく高頻度に殺菌洗浄を行うことがで
き、したがって超純水を常に無菌状態に確実に維持して
高品質の製品製造に適した用水を供給することができる
超純水供給装置、及びその装置を構成している配管内の
殺菌方法を提供するところにある。Another object of the present invention is to perform sterilization cleaning at high frequency without stopping a production line or the like. It is an object of the present invention to provide an ultrapure water supply device capable of supplying water suitable for water supply, and a method for sterilizing pipes constituting the device.
【0010】[0010]
【課題を解決するための手段】上記目的を達成する本発
明の超純水供給装置の特徴は、超純水製造装置の供給部
から延設された超純水送水用の往路配管と、該超純水製
造装置の戻り部に接続された超純水返送用の復路配管
と、これら往路配管と復路配管の間に多数並列して接続
された接続配管と、これら接続配管の途中で分岐されて
超純水の使用装置に超純水を給水する給水用配管とを備
えた超純水供給装置において、往路配管を複数本に設け
ると共に、各接続配管から使用装置への給水用配管の接
続部より上流側の位置に、これら複数の往路配管からの
送水が合流する合流部を設け、更にこれら複数の往路配
管のいずれかを選択して超純水に代えて殺菌液を供給で
きるように設けられた殺菌液供給装置と、これらの往路
配管から上記各配管への殺菌液,超純水の通水を切換え
るための通水選択手段を設けた構成をなすところにあ
る。A feature of the ultrapure water supply apparatus of the present invention that achieves the above object is that an ultrapure water supply pipe extending from a supply section of the ultrapure water production apparatus is provided. A return pipe for returning ultrapure water connected to the return section of the ultrapure water production device, a number of connection pipes connected in parallel between these outbound pipes and return pipes, and a branch in the middle of these connection pipes In the ultrapure water supply device equipped with a water supply pipe for supplying ultrapure water to the equipment using ultrapure water, a plurality of outgoing pipes are provided and connection of the water supply pipe from each connection pipe to the equipment to be used is performed. In the position on the upstream side of the section, a merging section where the water supply from the plurality of outgoing pipes is provided, and further, any one of these plurality of outgoing pipes is selected so that the sterilizing solution can be supplied instead of ultrapure water. The sterilizing solution supply device provided and the above piping Sterilizing solution, there is to forming a structure in which a water flow selecting means for switching the water flow of the ultrapure water.
【0011】本発明において超純水製造装置というの
は、原水中の懸濁物質、無機物質、イオン等を除去する
ために種々の装置を用いた従来知られている種々の構成
の超純水製造装置を、特に限定することなく挙げること
ができ、例えば、凝集沈澱装置、砂ろ過装置等を用いて
原水を除濁処理する前処理装置、活性炭ろ過装置、逆浸
透膜,精密ろ過膜等の膜処理装置、2床3塔式等の脱塩
装置、真空脱気装置などで前処理水中の不純物を除去す
る一次純水処理装置、および紫外線酸化装置、混床式ポ
リッシャ、限外ろ過膜等の膜処理装置などで一次純水中
の微量な微粒子,コロイダル物質,有機物,金属,イオ
ン等を更に除去する二次純水処理装置を有するものを代
表的な構成のものとして挙げることができる。In the present invention, the ultrapure water producing apparatus refers to ultrapure water of various constitutions conventionally known using various apparatuses for removing suspended substances, inorganic substances, ions and the like in raw water. Examples of the production apparatus include, but are not particularly limited to, a coagulation sedimentation apparatus, a pretreatment apparatus for turbidity treatment of raw water using a sand filtration apparatus, an activated carbon filtration apparatus, a reverse osmosis membrane, a microfiltration membrane, and the like. Membrane treatment equipment, desalination equipment such as two-bed three-column type, primary deionized water treatment equipment for removing impurities in pretreatment water by vacuum deaeration equipment, etc., ultraviolet oxidation equipment, mixed-bed polisher, ultrafiltration membrane, etc. A typical example is a membrane treatment apparatus having a secondary pure water treatment apparatus for further removing trace particles, colloidal substances, organic substances, metals, ions, and the like in primary pure water.
【0012】そしてこの超純水製造装置の「供給部」と
いうのは、特に限定されないが、例えば上記二次純水処
理装置の最後段に設置された限外ろ過膜装置からの被処
理水流出部がこれに該当する。またこの供給部から延出
される超純水送水用の「往路配管」とは、超純水製造装
置から、これとは比較的離れて設置される場合が多い多
数の超純水の使用装置の近傍まで超純水を送水するため
に設けられる主送水配管をいい、本発明においては、こ
の往路配管を少なくとも2本設けることがその特徴の一
つである。この構成を採用することによって、例えば1
本の往路配管に超純水を通水することで所望の使用装置
に対する超純水の給水を確保しながら、同時に、他の往
路配管に殺菌液を流すことで所定の配管を殺菌処理する
ことを可能とできるからである。The "supply unit" of the ultrapure water production apparatus is not particularly limited. For example, the outflow of the water to be treated from the ultrafiltration membrane apparatus installed at the last stage of the secondary pure water treatment apparatus Department corresponds to this. In addition, the “outgoing pipe” for ultrapure water supply extending from this supply unit refers to a large number of ultrapure water use equipment that is often installed relatively far from the ultrapure water production equipment. It refers to a main water supply pipe provided to supply ultrapure water to the vicinity. One of the features of the present invention is to provide at least two outgoing pipes. By adopting this configuration, for example, 1
By passing ultrapure water through the outgoing pipes to ensure the supply of ultrapure water to the desired equipment, and at the same time, sterilizing predetermined pipes by flowing a sterilizing solution to the other outgoing pipes Is possible.
【0013】本発明は、上記した構成に加えて、復路配
管を複数本(例えば2本)設けると共に、上記各接続配
管に給水用配管を接続した分岐部の下流位置からこれら
複数の復路配管に送水を分ける送水分岐配管を設けた構
成とすることもできる。このようにすることで、殺菌液
として薬液を用いる場合にも、1本の復路配管にこの薬
液を流して系外に排出する方式で該復路配管の殺菌をお
こないながら、他の復路配管に超純水製造装置に戻すよ
うに超純水を流して、費用をかけて製造した超純水の有
効利用を図って無駄を防ぐことができる。なお、上記各
送水分岐配管への殺菌液,超純水の通水制御は、独立あ
るいは上記通水制御手段の一部に含ませた第2の通水選
択手段により制御することができる。According to the present invention, in addition to the above-described structure, a plurality of return pipes (for example, two pipes) are provided, and a plurality of return pipes are connected to the respective return pipes from a downstream position of a water supply pipe. It is also possible to adopt a configuration in which a water supply branch pipe for dividing water supply is provided. In this way, even when a chemical solution is used as a sterilizing solution, the chemical solution is passed through one return pipe and discharged out of the system while the return pipe is sterilized while the other return pipe is superposed. By flowing ultrapure water so as to return to the pure water production apparatus, wasteful prevention can be achieved by effectively using ultrapure water produced at high cost. The control of the flow of the sterilizing solution and the ultrapure water to each of the water supply branch pipes can be controlled independently or by the second water flow selection means included in a part of the water flow control means.
【0014】上記構成において、「復路配管」は超純水
の無駄をできるだけなくすために上記多数の超純水の使
用装置の近傍から未使用の超純水を超純水製造装置に戻
す循環径路の返送管路を形成するための配管をいう。超
純水製造装置の「戻り部」というのは、返送された超純
水を再処理するのに適当な部分をいい、一般的には上記
一次純水処理装置と二次純水処理装置の間に設けられる
一次純水貯槽(タンク)をこの戻り部として復路配管を
接続する場合が多い。In the above configuration, the "return pipe" is a circulation path for returning unused ultrapure water to the ultrapure water producing apparatus from the vicinity of the plurality of ultrapure water using apparatuses in order to minimize waste of the ultrapure water. Means a pipe for forming a return pipeline. The "return part" of the ultrapure water production device refers to a portion suitable for reprocessing the returned ultrapure water, and is generally used for the above-mentioned primary and secondary pure water treatment devices. In many cases, a return pipe is connected with a primary pure water storage tank (tank) provided therebetween as a return portion.
【0015】「接続配管」は、所定の超純水の使用装置
に超純水を供給すると共に、余剰分(未使用分)、ある
いは使用装置を停止した非使用時に超純水の循環状態
(滞留させない状態)を確保するために、上記往路配管
から復路配管に渉るように接続されるものであり、限定
されないが、一般的には一つの使用装置ごとに設けられ
て使用装置の数だけ往路配管と復路配管の間に多数並設
される場合が多い。The "connection pipe" supplies the ultrapure water to a predetermined ultrapure water use device and supplies a surplus (unused portion) or an ultrapure water circulation state when the use device is stopped and not used. In order to ensure the state of not staying), it is connected so as to cross from the above-mentioned outgoing piping to the returning piping, and is not limited, but is generally provided for each used device and the number of used devices is generally equal to the number of used devices. In many cases, a large number are arranged in parallel between the outgoing pipe and the return pipe.
【0016】本発明のように、往路配管を複数本設け
て、各接続配管の給水配管への分岐部の上流側位置でこ
れら複数の往路配管からの送水を合流させる方式を採用
することによって、例えば一方の往路配管に殺菌液、他
の往路配管に超純水を通水すれば、各接続配管に殺菌液
を流す状態と超純水を通水する状態を各配管への通水制
御で選択可能とでき、したがってある使用装置への超純
水の給水と、他の使用装置につながる接続配管内の殺菌
洗浄を同時並行して行なうことができ、製造ラインの連
続稼働が実現される。As in the present invention, by adopting a method in which a plurality of outgoing pipes are provided, and water supplied from the plurality of outgoing pipes is merged at a position upstream of a branch portion of each connecting pipe to a water supply pipe, For example, if sterilizing liquid is passed through one outgoing pipe and ultrapure water is passed through the other outgoing pipe, the state of flowing sterilizing liquid through each connecting pipe and the state of passing ultrapure water can be controlled by passing water through each pipe. It can be selected, so that the supply of ultrapure water to one use device and the sterilization and cleaning in the connection pipes connected to other use devices can be performed simultaneously in parallel, and continuous operation of the production line is realized.
【0017】殺菌液の供給は、殺菌薬液あるいは熱水の
貯槽等として設けられた殺菌液供給装置から殺菌目的の
配管、一般的には複数の各往路配管の最上流側の位置
に、超純水に代えて殺菌液を供給できる装置を接続すれ
ばよい。The sterilizing liquid is supplied from a sterilizing liquid supply device provided as a storage tank for disinfecting chemicals or hot water to a pipe for sterilization, generally an ultrapure pipe at a most upstream position of each of a plurality of outgoing pipes. What is necessary is just to connect the apparatus which can supply a germicidal solution instead of water.
【0018】「給水用配管」は接続配管から分岐された
配管をいう。「超純水の使用装置」は供給された超純水
をそれぞれ所定の目的に従って使用する装置をいい、例
えば半導体洗浄装置では超純水は洗浄用水として使用さ
れる。"Piping for water supply" refers to a pipe branched from a connection pipe. "Ultra-pure water using apparatus" refers to an apparatus that uses supplied ultra-pure water according to a predetermined purpose, for example, in a semiconductor cleaning apparatus, ultra-pure water is used as cleaning water.
【0019】「通水選択手段」は、一般的には、各配管
における超純水の通水,遮断、超純水に代えた殺菌液の
通水,遮断を行うために適宜所定の箇所に設けられた通
水制御弁と、この通水制御弁を動作制御するコンピュー
タ等で形成された制御手段とにより構成されるが、これ
に限定されるものではない。The "flow selecting means" is generally provided at a predetermined position in order to feed or shut off ultrapure water in each pipe, or to feed or shut off a sterilizing solution instead of ultrapure water. It is constituted by the provided water flow control valve and a control means formed by a computer or the like for controlling the operation of the water flow control valve, but is not limited thereto.
【0020】以上のように設けた超純水供給装置によれ
ば、適宜必要に応じて、複数本設けた往路配管のうちの
1本に殺菌液を流すと共に、各配管の通水制御により殺
菌目的の配管に殺菌液を流しながら、他の配管について
は超純水を通水している往路配管から超純水を流して使
用装置を連続的に稼働する状態を維持することができ
る。According to the ultrapure water supply apparatus provided as described above, a sterilizing liquid is supplied to one of a plurality of outgoing pipes as required, and sterilization is performed by controlling the flow of water through each pipe. It is possible to maintain a state in which the used apparatus is continuously operated by flowing the ultrapure water from the outgoing pipe through which the ultrapure water is supplied to the other pipes while the sterilizing solution is supplied to the target pipe.
【0021】また、製造した超純水の無駄を少なくする
ために、殺菌薬液は系外に排出するが余剰(未使用)の
超純水は超純水製造装置に循環して戻すことができる。
殺菌液が熱水である場合には復路配管を通して超純水製
造装置の戻り部に戻すこともできる。Further, in order to reduce the waste of the produced ultrapure water, the germicide is discharged out of the system, but the surplus (unused) ultrapure water can be circulated back to the ultrapure water producing apparatus. .
When the sterilizing solution is hot water, it can be returned to the return portion of the ultrapure water production device through a return pipe.
【0022】更にまた本発明においては、給水用配管を
介して超純水の使用装置に接続されている接続配管とは
別に、使用装置とは関係しないバイパス管を、接続配管
と並列して往路配管と復路配管の間に設けることもでき
る。このようにすることで、複数の往路配管と復路配管
とを、各1本づつバイパス管で接続した組(通常は2
組)に構成することができ、超純水の使用装置の稼働状
況とは関係せずに超純水あるいは殺菌液を滞留させるこ
となく常時通水させる状態を維持することができるため
好ましい。Furthermore, in the present invention, apart from the connection pipe connected to the apparatus for using ultrapure water via the water supply pipe, a bypass pipe irrelevant to the apparatus used is provided in parallel with the connection pipe in the outward path. It can also be provided between the pipe and the return pipe. In this way, a set of a plurality of outgoing pipes and a return pipe connected by a bypass pipe one by one (usually 2
(Set), which is preferable because it is possible to maintain a state in which ultrapure water or a sterilizing liquid is constantly passed without stagnation regardless of the operation state of a device using ultrapure water.
【0023】本発明の好ましい構成は、熱水を殺菌液と
して用いる例としては、超純水製造装置の供給部から延
設された超純水送水用の2本の往路配管と、該超純水製
造装置の戻り部に接続された超純水返送用の1本の復路
配管と、二つの片側端部が上記2本の往路配管にそれぞ
れ接続されかつ途中で合流されてこの合流路の反対側端
部が上記1本の復路配管に接続された接続配管の複数
と、各接続配管の合流部よりも下流位置で分岐されて超
純水の使用装置に超純水を給水する給水用配管と、上記
接続配管にバイパスして2本の往路配管を1本の復路配
管に接続するバイパス配管と、2本の往路配管のいずれ
かを選択して超純水に代えて殺菌用熱水を供給する熱水
供給装置と、該往路配管から上記各配管への熱水,超純
水の通水を切換える通水選択手段とを備えたという構成
の超純水供給装置を例示することができる。In a preferred embodiment of the present invention, as an example in which hot water is used as a sterilizing solution, two outgoing pipes for water supply of ultrapure water extended from a supply section of an ultrapure water production device, One return pipe for returning ultrapure water connected to the return section of the water production apparatus, and two one-side ends are connected to the two forward pipes, respectively , and merged on the way to be opposite to the merge path. A plurality of connection pipes whose side ends are connected to the one return pipe, and a water supply pipe that is branched at a position downstream of a junction of the connection pipes and supplies ultrapure water to a device using ultrapure water. And a bypass pipe that bypasses the connection pipe and connects two outgoing pipes to one return pipe, and selects one of the two outgoing pipes and supplies hot water for sterilization instead of ultrapure water. The hot water supply device to be supplied and the flow of hot water and ultrapure water from the outgoing pipe to each of the pipes are switched. Ultrapure water feeder configurations that have a water selection means can be exemplified.
【0024】かかる装置においては、超純水供給の給水
のための配管設備の殺菌洗浄を、下記の〜の操作で
行うことができる。In such an apparatus, the sterilization and cleaning of the piping equipment for supplying the ultrapure water can be performed by the following operations.
【0025】:バイパス配管で接続された一方の往路
配管から復路配管に熱水を通水しかつ該一方の往路配管
と各接続配管の間の通水を遮断すると共に、他方の往路
配管を通して各接続配管に超純水を通水する第1工程、
:上記接続配管の少なくともいずれか一方と、超純水
が通水されている上記他方の往路配管からの通水を遮断
すると共に、熱水が通水されている上記一方の往路配管
から接続配管に熱水を通水させる第2工程、:第2工
程の接続配管に対する上記一方の往路配管からの熱水通
水を遮断しかつ上記他方の往路配管から超純水を通水す
る第3工程、:上記第2工程と第3工程の操作を必要
に応じて他の接続配管の殺菌処理のために繰返す第4工
程、:上記一方の往路配管に対する熱水供給を遮断し
て超純水を通水する第5工程。Hot water flows from one outgoing pipe connected to the bypass pipe to the return pipe, and water flow between the one outgoing pipe and each connecting pipe is cut off. The first step of passing ultrapure water through the connection pipe,
: At least one of the connection pipes and the other one of the outgoing pipes through which ultrapure water is passed, and the connection pipe from the one outgoing pipe through which hot water is passed. A second step of passing hot water through the second step: a third step of cutting off hot water flow from the one outgoing pipe to the connecting pipe in the second step and passing ultrapure water through the other outgoing pipe. , A fourth step of repeating the operations of the second step and the third step as necessary for the sterilization treatment of another connection pipe, and interrupting the supply of hot water to the one outgoing pipe to remove ultrapure water. The fifth step of passing water.
【0026】また、殺菌薬液(例えばアルコール,過酸
化水素水,ふっ酸水溶液,過酢酸水溶液,オゾン水等)
を殺菌液として用いる例としては、超純水製造装置の供
給部から延設された超純水送水用の2本の往路配管と、
該超純水製造装置の戻り部に接続された超純水返送用の
2本の復路配管と、これら2本の復路配管それぞれの下
流側位置に設けられた系外への排水配管と、中間合流路
の両側が分岐されていて片側の各分岐端部が上記2本の
往路配管に接続されかつ反対側の各分岐端部が上記2本
の復路配管にそれぞれ接続された接続配管の複数と、各
接続配管の合流路から分岐されて超純水の使用装置に超
純水を給水する給水用配管と、上記接続配管にバイパス
して往路配管と復路配管を各々1本づつの組に接続する
バイパス配管と、2本の往路配管のいずれかを選択して
超純水に代えて殺菌薬液を供給する殺菌薬液供給装置
と、該往路配管から上記各配管への殺菌薬液,超純水の
通水を切換える通水選択手段とを備えたという構成の超
純水供給装置を例示することができる。Also, a germicidal solution (for example, alcohol, aqueous hydrogen peroxide, aqueous hydrofluoric acid, aqueous peracetic acid, ozone water, etc.)
As an example of using as a sterilizing solution, two outgoing pipes for ultrapure water water supply extended from the supply unit of the ultrapure water production device,
Two return pipes for returning ultrapure water connected to a return portion of the ultrapure water production apparatus, drainage pipes to the outside provided at downstream positions of the two return pipes, A plurality of connection pipes, both sides of the merged flow path being branched, each branch end on one side being connected to the two outgoing pipes and each branch end on the opposite side being connected to the two return pipes, respectively. , A water supply pipe that is branched from the joint flow path of each connection pipe and supplies ultrapure water to a device using ultrapure water, and a forward pipe and a return pipe are connected to a set of one pipe each by bypassing the connection pipe. And a sterilizing solution supply device for selecting one of the two outgoing lines and supplying a sterilizing solution instead of ultrapure water, and a sterilizing solution and ultrapure water from the outgoing line to each of the above pipes. An example of an ultrapure water supply device having a water selection means for switching water flow Rukoto can.
【0027】かかる装置においては、超純水供給の給水
のための配管設備の殺菌洗浄を、下記の´〜´の操
作で行うことができる。In such an apparatus, the sterilization and cleaning of the piping equipment for supplying the ultrapure water can be performed by the following operations (1) to (4).
【0028】´:バイパス配管で接続された一方の往
路配管から、復路配管、更に排水配管に殺菌薬液を通液
しながらこれらの往路配管及び復路配管と各接続配管の
間の通液は遮断すると共に、バイパス配管で接続された
他方の往路配管から、接続配管、更に復路配管に超純水
を通水して超純水製造装置に戻す第1工程、´:上記
接続配管の少なくともいずれか一つと、超純水が通水さ
れている上記他方の往路配管及び復路配管との通水を遮
断すると共に、殺菌薬液が通液されている上記一方の往
路配管及び復路配管と該接続配管とを通液させる第2工
程、´:第2工程に続き、接続配管に対する上記一方
の往路配管からの殺菌薬液の通液を遮断すると共に、上
記他方の往路配管から超純水を通水して該接続配管内を
超純水で置換する第3工程、´:第3工程で配管内が
超純水で置換された接続配管から上記一方の復路配管へ
の通水を遮断すると共に、該接続配管と上記他方の復路
配管を通水させる第4工程、´:上記第2工程〜第4
工程の操作を必要に応じて他の接続配管の殺菌処理のた
めに繰返す第5工程、´:上記一方の往路配管への殺
菌薬液の供給を遮断し、かつ超純水を通水して該一方の
往路配管から復路配管までの配管内を超純水に置換する
第6工程、´:超純水に置換された該一方の復路配管
からの排水を停止して超純水製造装置に循環水を戻す第
7工程。': While passing the sterilizing agent liquid from one outgoing pipe connected by the bypass pipe to the return pipe and further to the drain pipe, the flow between these outgoing pipes and return pipes and each connecting pipe is shut off. And a first step of passing ultrapure water from the other outbound pipe connected by the bypass pipe to the connection pipe and further to the return pipe and returning the ultrapure water to the ultrapure water producing apparatus, ': at least one of the above connection pipes And shut off the flow of water through the other outgoing pipe and the return pipe through which ultrapure water is passed, and connect the one outgoing pipe and the return pipe through which the germicide solution is passed with the connection pipe. The second step of passing the liquid, ': following the second step, while blocking the passage of the sterilizing agent solution from the one outgoing pipe to the connection pipe, and passing ultrapure water from the other outgoing pipe, Third step of replacing the connection pipe with ultrapure water ': A fourth step of interrupting the flow of water from the connection pipe whose inside of the pipe has been replaced with ultrapure water in the third step to the one return pipe, and allowing the connection pipe and the other return pipe to flow; ': The second to fourth steps
A fifth step in which the operation of the step is repeated as necessary for the sterilization treatment of another connecting pipe, ': shut off the supply of the sterilizing agent to the one of the outgoing pipes, and pass ultrapure water therethrough. Sixth step of replacing the inside of the pipe from one outgoing pipe to the return pipe with ultrapure water, ': Stopping drainage from the one return pipe replaced with ultrapure water and circulating it to the ultrapure water production device Seventh step of returning water.
【0029】[0029]
【発明の実施の形態】以下本発明を図面に示す実施形態
に基づいて更に説明するが、複数とされる往路配管は一
般的には2本で十分本発明の目的を達成し、また必要に
応じて複数とされる復路配管も一般的には2本で十分本
発明の目的を達成するので、以下に示す実施形態におい
てはこれらの配管が2本の場合として説明する。ただし
本発明はこの構成に限定されるものではない。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be further described below with reference to an embodiment shown in the drawings. In general, two outgoing pipes are used in a plurality, and the object of the present invention is sufficiently achieved. In general, two return pipes corresponding to the plurality of return pipes generally sufficiently satisfies the object of the present invention. Therefore, in the embodiment described below, the case where the number of these pipes is two will be described. However, the present invention is not limited to this configuration.
【0030】実施形態1 図1に示される本例において、1は、超純水製造装置
(不図示)の供給部としてその超純水製造装置の最後段
に設置された限外ろ過膜(以下「UF」と略記する)で
あり、これに接続された初段供給配管2は、分岐弁3
1 ,32 を有する分岐管41 ,42 により分岐されて、
2本の往路配管51 ,52 に接続されている。Embodiment 1 In the present embodiment shown in FIG. 1, reference numeral 1 denotes an ultrafiltration membrane (hereinafter, referred to as a supply section of an ultrapure water production apparatus (not shown)) installed at the last stage of the ultrapure water production apparatus. The first-stage supply pipe 2 connected thereto is connected to a branch valve 3.
Branched by branch pipes 4 1 and 4 2 having 1 and 3 2 ,
Two outbound pipeline 5 1, 5 2 are connected.
【0031】また、この超純水製造装置に並列する形で
設置されている殺菌液供給装置(本例は熱水供給装置)
6は、分岐弁71 ,72 を有する分岐管81 ,82 によ
り分岐されて、上記2本の往路配管51 ,52 に接続さ
れている。なお本例のこの熱水供給装置6は、超純水製
造装置で製造された超純水を熱交換して熱水とする装置
として構成されている。Also, a sterilizing solution supply device (in this example, a hot water supply device) installed in parallel with the ultrapure water production device.
6 is branched by the branch pipes 8 1, 8 2 having a branching valve 7 1, 7 2 are connected to the forward pipe 5 1, 5 2 two above. The hot water supply device 6 of the present embodiment is configured as a device that exchanges heat with ultrapure water produced by the ultrapure water production device to produce hot water.
【0032】9は復路配管であり、本例ではその下流端
は上記超純水製造装置の一次純水貯槽(タンク)10に
接続されている。Reference numeral 9 denotes a return line. In this embodiment, the downstream end thereof is connected to a primary pure water storage tank (tank) 10 of the above ultrapure water producing apparatus.
【0033】11,12,13は、2本の往路配管5
1 ,52 から1本の復路配管9の間に多数並列して接続
された接続配管であり、各接続配管は、2本の往路配管
51 ,52 に接続する二つの片側端部に連なる上流側分
岐配管111 ,112 (121,122 、131 ,132
)と、1本の復路配管9に連なる下流側合流管11
3(123 、133 )とを有していて、上流側分岐配管
111 ,112 (121 ,122 、131 ,132 )に
は、開閉切換え制御弁141 ,142 (151 ,15
2 、161 ,162 )が介設されている。Reference numerals 11, 12, and 13 denote two outgoing pipes 5
1, 5 and 2 from one return pipe 9 parallel to the connected connecting pipe number between each connection pipe, the two one end portion connected to two outgoing pipe 5 1, 5 2 Continuous upstream branch pipes 11 1 , 11 2 (12 1 , 12 2 , 13 1 , 13 2
) And the downstream merging pipe 11 connected to one return pipe 9
3 (12 3 , 13 3 ), and the upstream side branch pipes 11 1 , 11 2 (12 1 , 12 2 , 13 1 , 13 2 ) are provided with open / close switching control valves 14 1 , 14 2 ( 15 1 , 15
2 , 16 1 , 16 2 ).
【0034】17,18,19は超純水の使用装置であ
り、上記した下流側合流管113 ,123 、133 から
分岐されると共に途中に開閉切換え制御弁20,21、
22が介設された給水用配管114 ,124 、134 に
より超純水が給水されるように接続されている。Reference numerals 17, 18, and 19 denote devices for using ultrapure water, which are branched off from the above-mentioned downstream merging pipes 11 3 , 12 3 , and 13 3 .
The water supply pipes 11 4 , 12 4 , and 13 4 in which 22 is provided are connected so that ultrapure water is supplied.
【0035】なお、上記の各分岐弁31 ,32 と71 ,
72 、及び開閉切換え制御弁141,142 ,151 ,
152 、161 ,162 と20,21、22は、図示し
ない通水制御装置により開閉されて所定の系路の通水状
態が制御されるようになっている。The above branch valves 3 1 , 3 2 and 7 1 ,
7 2, and the on-off switching control valve 14 1, 14 2, 15 1,
15 2 , 16 1 , 16 2 , 20, 21 and 22 are opened and closed by a water flow control device (not shown) to control the water flow state of a predetermined system path.
【0036】このような構成の超純水供給装置は、次の
ように操作することで所定の配管内の殺菌洗浄を行うこ
とができる。The operation of the ultrapure water supply apparatus having the above-described structure can sterilize and clean a predetermined pipe.
【0037】(イ).通常時(超純水の通水時) 分岐弁71 ,72 を閉じると共に、UF1からの分岐弁
31 ,32 、及び開閉切換え制御弁141 ,142 ,1
51 ,152 、161 ,162 を全て開き、更に稼働さ
せる必要のあるいずれかの使用装置17,18,19へ
の給水のために関連する開閉切換え制御弁20,21、
22を開く。(A). Normal time (when ultrapure water flows) The branch valves 7 1 and 7 2 are closed, and the branch valves 3 1 and 3 2 from the UF 1 and the open / close switching control valves 14 1 , 14 2 , 1
5 1 , 15 2 , 16 1 , 16 2 are all opened and associated open / close switching control valves 20, 21, 21, for supplying water to any use device 17, 18, 19 which needs to be operated further
Open 22.
【0038】これにより2本の往路配管51 ,52 それ
ぞれに超純水が流れ、復路配管9を通して一次純水貯槽
10に超純水が循環する状態が確保されながら、必要な
使用装置への給水が行われる。As a result, the ultrapure water flows through each of the two outgoing pipes 5 1 , 5 2, and the state where the ultrapure water circulates through the return pipe 9 to the primary pure water storage tank 10 is ensured. Water is supplied.
【0039】(ロ).殺菌洗浄時 往路配管の一方51 について、各接続配管11〜13の
上流側分岐配管111,121 ,131 に介設した開閉
切換え制御弁141 ,151 ,161 を閉じる。(B). For one 5 1 sterilization during washing outbound pipeline, upstream branch pipe 11 1 of the connection pipe 11 to 13, 12 1, 13 1 opening is interposed switching control valve 14 1, 15 1, 16 1 Close.
【0040】次に、分岐弁31 を閉じると共に、分岐弁
71 を開いて、上記往路配管51 に熱水供給装置6から
殺菌用の熱水を流し、更に、稼働していない使用装置
(したがって給水用配管途中の開閉切換え制御弁20〜
22のいずれかは閉じている)にかかわる接続配管への
開閉切換え制御弁(141 ,151 ,161 のいずれ
か)を開いて熱水を流し、配管内の殺菌洗浄を行う。Next, it closes the branch valve 3 1, by opening the branch valve 71, flowing hot water for sterilizing the hot water supply device 6 to the outgoing pipe 5 1, further not running using apparatus (Therefore, the open / close switching control valves 20 to
Any opening and closing the switching valve to the connection pipe according to it are) closed 22 (14 1, 15 1, 16 1 either) the flow of hot water to open, perform sterilizing and washing in the pipe.
【0041】この際、稼働している使用装置に対して
は、他方の往路配管52 から超純水が通水されるため、
稼働を停止させる必要がない。なお、熱水を流している
接続配管への他方の往路配管52 からの超純水の通水を
遮断することがよい。[0041] In this case, with respect to the equipment used for running, the ultrapure water is passed through from the other outbound pipeline 5 2,
There is no need to stop operation. Incidentally, it is possible to shut off the water flow of the ultrapure water from the other outbound pipeline 5 2 to the connection pipe is flowing hot water.
【0042】(ハ).通常状態への復帰 往路配管51 への熱水供給を停止し、分岐弁31 を開く
と共に、分岐弁71 を閉じる。また開閉切換え制御弁1
41 ,151 ,161 を全て開く。(C). The hot water supply to the return outbound pipeline 5 1 to the normal state is stopped, it opens the branch valve 3 1, closing the branch valve 71. Open / close switching control valve 1
Opening 4 1, 15 1, 16 1 all.
【0043】本例の構成によれば、殺菌液として超純水
の熱水により適宜の配管内を殺菌処理することができ
る。また熱水を用いているため、殺菌処理後の液を系外
に排出することなく一次純水貯槽10に戻しても差し支
えなく、また必要があれば熱交換装置を用いて熱水を冷
却してもよい。According to the structure of this embodiment, the inside of an appropriate pipe can be sterilized with hot water of ultrapure water as a sterilizing liquid. In addition, since hot water is used, the sterilized liquid can be returned to the primary pure water storage tank 10 without being discharged out of the system, and if necessary, the hot water can be cooled using a heat exchange device. You may.
【0044】実施形態2 図2に示した本例は、図1の構成の装置において、接続
配管11〜13の下流側合流管113 ,123 、133
に、開閉切換え制御弁23,24,25を介設すると共
に、使用装置への給水用配管114 ,124 、134 の
分岐部と該開閉切換え制御弁23,24,25の間に、
途中に開閉切換え制御弁26,27、28を介設した系
外への排水配管115 ,125 、135 を分岐接続した
ことを特徴とするものであり、他の構成は図1と同じで
あるので、同じ符号を付して説明は省略する。Embodiment 2 The present embodiment shown in FIG. 2 is a device having the configuration shown in FIG. 1 and includes downstream merging pipes 11 3 , 12 3 and 13 3 of connecting pipes 11 to 13.
In addition, an opening / closing switching control valve 23, 24, 25 is interposed, and between the branch of the water supply pipes 11 4 , 12 4 , 13 4 and the opening / closing switching control valve 23, 24, 25.
And characterized in that it has middle drain pipe 11 5, 12 5, 13 5 to branch connection of the opening and closing switching control valve 26, 27, 28 to the outside of the system interposed, other configurations are the same as FIG. 1 Therefore, the same reference numerals are given and the description is omitted.
【0045】本例においては、上記実施形態1の洗浄操
作における(ロ)の洗浄時において、洗浄を行う例えば
接続配管11の途中に介設されている開閉切換え制御弁
23を閉じて、殺菌液を排水配管115 から系外に排水
するように操作される。In the present embodiment, at the time of the washing operation (b) in the washing operation of the first embodiment, for example, the open / close switching control valve 23 provided in the middle of the connection pipe 11 for washing is closed, and the sterilizing solution is washed. It is operated to drained out of the system from the discharge pipe 11 5.
【0046】このように殺菌液を一次純水貯槽10に戻
さずに系外に排出するので、殺菌液として、熱水に限ら
ず、薬液を用いることも可能となる。なお殺菌薬液を用
いる場合には、殺菌を行った接続配管内に残っている薬
液を超純水で排水配管115から系外に排水した後、該
接続配管系の復路配管との接続を開くようにすることが
必要である。As described above, since the sterilizing solution is discharged out of the system without returning to the primary pure water storage tank 10, it is possible to use a chemical solution as well as hot water as the sterilizing solution. Note that when using a sterilizing chemical liquid, after draining the liquid medicine remaining in was sterilized connection in the pipe to the outside of the system from the discharge pipe 11 5 with ultrapure water, opening a connection to the return pipe of the connection piping system It is necessary to do so.
【0047】すなわち、熱水を殺菌液として用いる場合
には次のように殺菌洗浄の操作をすることができる。That is, when hot water is used as a germicidal solution, the germicidal washing operation can be performed as follows.
【0048】(ロ).殺菌洗浄時 2本の往路配管51 ,52 に超純水を通水している通常
時の状態から、バイパス配管で接続された一方の往路配
管(例えば51 )に熱水を通水しかつこの往路配管51
と各接続配管11〜13の間の通水を、開閉切換え制御
弁141 ,151 ,161 を閉じることで遮断すると共
に、他方の往路配管52 を通して各接続配管11〜13
に超純水を通水する(第1工程)。(B). From normal state that passed through the ultrapure water sterilization during washing two outbound pipeline 5 1, 5 2, passed through the hot water in one of the outgoing pipe connected in the bypass pipe (e.g., 5 1) Shikatsu's outbound piping 5 1
And the water flow between the respective connecting pipes 11 to 13 with blocking in the off switching control valve 14 1, 15 1 and 16 1 closed, the connection pipe through the other outbound pipeline 5 2 11-13
Through which ultrapure water is passed (first step).
【0049】次に、接続配管の少なくともいずれか一つ
(例えば11)と、超純水が通水されている往路配管5
2 からの通水を遮断すると共に、熱水が通水されている
往路配管51 から熱水を通水させて殺菌洗浄する(第2
工程)。殺菌に使用した熱水は、排水配管11 5 を通し
て系外に排水する。Next, at least one of the connecting pipes (for example, 11) and the outgoing pipe 5 through which the ultrapure water is passed.
While blocking the water passing from 2, hot water sterilized washed by passing water hot water from outgoing pipe 5 1, which is passed through (second
Process). The hot water used for sterilization is drain pipe 11 5 Through the system.
【0050】第2工程の接続配管11に対する往路配管
51 からの熱水通水を遮断し、往路配管52 から超純水
を通水する(第3工程)。The blocking hot water through the water from the outbound pipeline 5 1 to the connection pipe 11 of the second step, passed through the ultrapure water from the outbound pipeline 5 2 (third step).
【0051】第2工程と第3工程の操作を必要に応じて
他の接続配管の殺菌処理のために繰返す(第4工程)。The operations of the second step and the third step are repeated as necessary for sterilizing another connecting pipe (fourth step).
【0052】(ハ).通常状態への復帰 往路配管51 に対する熱水供給を遮断して超純水を通水
する(第5工程)。(C). By blocking the hot water supply to return the forward pipe 5 1 a to the normal state passed through the ultra-pure water (step 5).
【0053】実施形態3 図3に示した本例は、図2の構成における復路配管9を
2本(91 ,92 )に設けると共に、接続配管11〜1
3の下流側合流管113 ,123 、133 を分岐させ、
途中の開閉切換え制御弁231 ,232 、241 ,24
2 、251 ,252 を介して分岐先端部を上記2本の復
路配管91 ,92 に接続し、更に、2本の復路配管の循
環戻り側の先端部に、戻り水を一次純水貯槽10に戻す
か、系外に排出するかを切り換えるための切換え弁30
1 ,302 、311 ,312 を設けたことを特徴とする
ものであり、他の構成は図2と同じであるので、同じ符
号を付して説明は省略する。Embodiment 3 In the present embodiment shown in FIG. 3, two return pipes 9 (9 1 and 9 2 ) in the configuration of FIG.
The 3 downstream branch pipes 11 3 , 12 3 , and 13 3 are branched,
Opening / closing switching control valves 23 1 , 23 2 , 24 1 , 24
2 , 25 1 , and 25 2 , the branch tip is connected to the two return pipes 9 1 , 9 2 , and further, the return water is firstly purified to the tip of the two return pipes on the circulation return side. A switching valve 30 for switching between returning to the water storage tank 10 and discharging to the outside of the system
1, 30 2, 31 1, 31 is characterized in 2 that was provided, since the other configuration is the same as FIG. 2, is described with the same reference numerals will be omitted.
【0054】本例においては、接続配管11〜13の殺
菌洗浄のみならず、復路配管を2本とし、その循環下流
側で系外に排出するようにしたことで、復路配管91 ,
92内の殺菌洗浄も行える利点がある。In the present embodiment, not only the sterilization and cleaning of the connection pipes 11 to 13 but also two return pipes, which are discharged to the outside of the system on the downstream side of the circulation, so that the return pipes 9 1 ,
There is an advantage that allows even sterilizing and washing in 9 2.
【0055】実施形態4 図4に示した本例は、図3の構成において、接続配管1
1〜13の下流側合流管113 ,123 、133 に、開
閉切換え制御弁23,24,25を介設すると共に、使
用装置への給水用配管114 ,124 、134 の分岐部
と該開閉切換え制御弁231 ,232 ,241 ,24
2 ,251 2 ,252 の間に、途中に開閉切換え制御弁
26,27、28を介設した系外への排水配管115 ,
125 、135 を分岐接続したことを特徴とするもので
あり、他の構成は図3と同じであるので、同じ符号を付
して説明は省略する。Embodiment 4 The present embodiment shown in FIG. 4 is different from the configuration shown in FIG.
Downstream merging pipe 11 3, 12 3, 13 3 1-13, as well as interposed closing switching control valves 23, 24, 25, the water supply pipe 11 4 to use device, 12 4, 13 4 branches Section and the open / close switching control valve 23 1 , 23 2 , 24 1 , 24
2, 25 1 2, 25 between the two, the drainage pipe 11 5 to the outside of the system which is interposed closing switching control valves 26, 27, 28 in the middle,
It is characterized by the fact that 12 5 and 13 5 are branched and connected, and the other configuration is the same as that of FIG. 3.
【0056】実施形態5 図5に示した本例は、図4の構成において、使用装置に
給水するための給水用配管が分岐接続されていないバイ
パス配管331 ,332 を、往路配管51 と復路配管9
1 の間、及び往路配管52 と復路配管92 の間にそれぞ
れ接続し、この途中に通常閉の開閉切換え制御弁34
1 ,342 を介設したことを特徴とするものである。[0056] The examples shown in the embodiment 5 5, in the configuration of FIG. 4, a bypass pipe 33 1, 33 2 water supply pipe for supplying water to the apparatus used is not branched and connected, outgoing pipe 5 1 And return line 9
Between 1 and respectively connected between the outbound pipeline 5 2 and return pipe 9 2, normally-closed-off switching control valve in this way 34
1, 34 is characterized in that 2 is interposed.
【0057】このような構成によれば、超純水及び殺菌
液をいずれも滞留させることなく通水状態としながら、
所定配管の殺菌洗浄処理と、必要な使用装置への超純水
の給水を行うことができる。According to such a configuration, while keeping the ultrapure water and the sterilizing solution in a water-passing state without stagnation,
It is possible to perform a sterilization and cleaning treatment of a predetermined pipe and supply of ultrapure water to a necessary use device.
【0058】すなわち、具体的な洗浄処理として以下の
操作を行うことができる。That is, the following operation can be performed as a specific cleaning process.
【0059】(ロ).殺菌洗浄時 バイパス配管331 で接続された往路配管51 から、復
路配管91 を通して系外に至るように殺菌薬液(または
熱水)を通液しながら、これらの往路配管51及び復路
配管91 と各接続配管11〜13との間の通液は遮断
し、バイパス配管332 で接続された他方の往路配管5
2 から、接続配管11〜13、更に復路配管92 に超純
水を通水して一次純水貯槽10に戻す(第1工程)。(B). From outgoing pipe 5 1 connected by sterilizing and washing during bypass pipe 33 1, while passed through sterilizing chemical liquid (or hot water) to reach the outside of the system through the return pipe 9 1, these outbound pipeline 5 1 and return pipe 9 1 and the other outbound pipeline liquid passage is blocked, which is connected with bypass piping 33 2 between the connecting pipes 11 to 13 5
2, the connection pipe 11 to 13, back to the primary pure water storage tank 10 and passed through the ultrapure water further to return pipe 9 2 (first step).
【0060】接続配管11〜13の少なくともいずれか
一つ(例えば11)と、超純水が通水されている上記往
路配管52 及び復路配管92 との通水を遮断すると共
に、殺菌薬液が通液されている上記往路配管51 及び復
路配管91 とこの接続配管11とを通液させる(第2工
程)。[0060] and at least one of the connection pipe 11 to 13 (e.g. 11), with ultra-pure water to block the water flow between the outbound pipeline 5 2 and return pipe 9 2 being passed through, sterilizing chemical There is passed through the connection pipe 11 of the outbound pipeline 5 1 and return pipe 9 1 Toko being passed through (second step).
【0061】第2工程に続き、接続配管11に対する上
記往路配管51 からの殺菌薬液の通液を遮断すると共
に、上記往路配管52 から超純水を通水してこの接続配
管内を超純水で置換する(第3工程)。[0061] Following the second step, together with blocking the liquid passage of the sterilizing liquid medicine from the forward pipe 5 1 to the connection pipe 11, the connection in the pipe and passed through an ultra-pure water from the outbound pipeline 5 2 Ultra Replace with pure water (third step).
【0062】第3工程で配管内が超純水で置換された接
続配管11から復路配管91 への通水を遮断すると共
に、この接続配管11と復路配管92 を通水させる(第
4工程)。[0062] with the pipe in the third step is to cut off the water flow to the return pipe 9 1 from the connecting pipe 11 which is substituted with ultrapure water, thereby passed through the return pipe 9 2 this connection pipe 11 (4th Process).
【0063】第2工程〜第4工程の操作を必要に応じて
他の接続配管12,13の殺菌処理のために繰返す(第
5工程)。The operations of the second to fourth steps are repeated as necessary for the sterilization of the other connecting pipes 12 and 13 (fifth step).
【0064】(ハ).通常状態への復帰 往路配管51 への殺菌薬液の供給を遮断し、かつ超純水
を通水してこの往路配管51 から復路配管91 までの配
管内を超純水に置換する(第6工程)。(C). Cut off the supply of sterilizing chemical liquid to return outbound pipeline 5 1 to the normal state, and ultrapure water was passed through to replace the pipe from the outward pipe 5 1 to return pipe 9 1 ultrapure water ( Sixth step).
【0065】超純水に置換された復路配管91 からの排
水を停止して超純水製造装置に循環水を戻す(第7工
程)。[0065] returning the circulating water to the ultrapure water production system to stop the waste water from return pipe 9 1 substituted in ultrapure water (seventh step).
【0066】本発明は、以上説明した実施形態1〜5の
構成に限定されるものではなく、種々の変更した態様で
実施できることは当然であり、例えば実施形態5で説明
したバイパス配管は、その途中に介設した開閉切換え制
御弁341 ,342 を省略することもできるし、またこ
のバイパス配管を、実施形態1〜4において設けること
もできる。The present invention is not limited to the configurations of Embodiments 1 to 5 described above, and it is obvious that the present invention can be carried out in various modified forms. it is also possible to omit the closing switching control valve 34 1 34 2 which is interposed in the middle, also the bypass pipe, it is also possible to provide in the first to fourth embodiments.
【0067】[0067]
【発明の効果】本発明の超純水供給装置によれば、全使
用装置の稼働停止、すなわち製造ライン等の停止を行う
ことなしに、製造された超純水を供給元から使用場所に
供給する配管設備の所望箇所を、適宜必要に応じて殺菌
洗浄することができ、したがって長期にわたって製造ラ
インの連続稼働が可能になり、生産性の向上に多大な効
果をもたらす。According to the ultrapure water supply apparatus of the present invention, the produced ultrapure water is supplied from the supply source to the place of use without stopping the operation of all the used apparatuses, that is, without stopping the production line or the like. A desired part of the piping equipment to be sterilized and cleaned can be appropriately cleaned as needed, and therefore, the production line can be continuously operated for a long period of time, which has a great effect on improving the productivity.
【0068】また、製造ライン等を停止させることなく
高頻度に殺菌洗浄を行うことができるので、超純水を常
に無菌状態に維持した用水として供給でき、高品質の製
品製造に極めて有効であるという効果を奏する。Further, since sterilization cleaning can be performed frequently without stopping the production line, etc., ultrapure water can be supplied as service water which is always kept in an aseptic state, which is extremely effective for producing high quality products. This has the effect.
【図1】本発明の実施形態1の超純水供給装置の構成概
要を示したフロー図。FIG. 1 is a flowchart showing a configuration outline of an ultrapure water supply device according to a first embodiment of the present invention.
【図2】本発明の実施形態2の超純水供給装置の構成概
要を示したフロー図。FIG. 2 is a flowchart showing a schematic configuration of an ultrapure water supply device according to a second embodiment of the present invention.
【図3】本発明の実施形態3の超純水供給装置の構成概
要を示したフロー図。FIG. 3 is a flowchart showing a configuration outline of an ultrapure water supply device according to a third embodiment of the present invention.
【図4】本発明の実施形態4の超純水供給装置の構成概
要を示したフロー図。FIG. 4 is a flowchart showing a schematic configuration of an ultrapure water supply device according to a fourth embodiment of the present invention.
【図5】本発明の実施形態5の超純水供給装置の構成概
要を示したフロー図。FIG. 5 is a flowchart showing a schematic configuration of an ultrapure water supply device according to a fifth embodiment of the present invention.
1・・・超純水製造装置の供給部(UF)、2・・・初
段供給配管、3・・・分岐弁、4・・・分岐管、5・・
・往路配管、6・・・殺菌液供給装置(熱水供給装
置)、7・・・分岐弁、8・・・分岐管、9・・・復路
配管、10・・・一次純水貯槽、11〜13・・・接続
配管、111 ,112 ,121 ,122 、131 ,13
2 ・・・上流側分岐配管、113 ・・・下流側合流管1
14 ・・・給水用配管、115 ・・・排水配管、14〜
16・・・開閉切換え制御弁、17〜19・・・(超純
水の)使用装置、23〜28・・・開閉切換え制御弁、
30,31・・・切換え弁、33・・・バイパス配管、
34・・・開閉切換え制御弁。1 ... supply unit (UF) of ultrapure water production equipment, 2 ... first stage supply pipe, 3 ... branch valve, 4 ... branch pipe, 5 ...
Outgoing piping, 6: sterilizing liquid supply device (hot water supply device), 7: branch valve, 8: branch pipe, 9: return piping, 10: primary pure water storage tank, 11 ... 13 Connection piping, 11 1 , 11 2 , 12 1 , 12 2 , 13 1 , 13
2・ ・ ・ Upstream branch pipe, 11 3・ ・ ・ Downstream merge pipe 1
1 4 ... water supply piping, 11 5 ... drainage pipe, 14
16 ··· Open / close switching control valve, 17-19 ··· Use device (ultra pure water), 23-28 ··· Open / close switching control valve,
30, 31 ... switching valve, 33 ... bypass piping,
34 ... Open / close switching control valve.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI A61L 2/18 A61L 2/18 (58)調査した分野(Int.Cl.7,DB名) C02F 1/50 A61L 2/00 C23G 3/00 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 identification code FI A61L 2/18 A61L 2/18 (58) Investigated field (Int.Cl. 7 , DB name) C02F 1/50 A61L 2/00 C23G 3/00
Claims (9)
た超純水送水用の往路配管と、該超純水製造装置の戻り
部に接続された超純水返送用の復路配管と、これら往路
配管と復路配管の間に多数並列して接続された接続配管
と、これら接続配管の途中で分岐されて超純水の使用装
置に超純水を給水する給水用配管とを備えた超純水供給
装置において、 上記往路配管を複数本に設けると共に、上記各接続配管
が複数の往路配管と同数の片側端部を有し、当該片側端
部は複数の往路配管にそれぞれ接続されかつ給水用配管
の接続部より上流側の位置に、これら複数の往路配管か
らの送水が合流する合流部を設け、更にこれら複数の往
路配管のいずれかを選択して超純水に代えて殺菌液を供
給する殺菌液供給装置と、これらの往路配管から上記各
配管への殺菌液,超純水の通水を切換える通水選択手段
を設けたことを特徴とする超純水供給装置。1. An ultrapure water supply line extending from a supply section of an ultrapure water production apparatus, and an ultrapure water return path pipe connected to a return section of the ultrapure water production apparatus. A plurality of connection pipes connected in parallel between the forward pipe and the return pipe, and a water supply pipe that is branched in the middle of the connection pipe and supplies ultrapure water to a device using ultrapure water. In the ultrapure water supply device, a plurality of the outgoing pipes are provided and
Has the same number of one-side ends as the plurality of outgoing pipes, and the one-side end
The part is connected to each of the plurality of outgoing pipes and provided at a position upstream of the connecting portion of the water supply pipe, a junction where water from the plurality of outgoing pipes merges, and further, any one of these plurality of outgoing pipes is provided. A sterilizing solution supply device for selectively supplying a sterilizing solution in place of ultrapure water, and a water flow selecting means for switching the flow of the sterilizing solution and ultrapure water from these outgoing pipes to the respective pipes. Ultrapure water supply device.
設けると共に、各接続配管に対する上記給水用配管の接
続部より下流側の位置に該接続配管からこれら複数の復
路配管への送水を分岐する返送用分岐配管を設け、更に
これら返送用分岐配管への通水を切換える第2の通水選
択手段を設けたことを特徴とする超純水供給装置。2. The method according to claim 1, wherein a plurality of return pipes are provided, and water supply from the connection pipe to the plurality of return pipes is branched to a position downstream of a connection portion of the water supply pipe to each connection pipe. An ultrapure water supply device, comprising: a return branch pipe for supplying water; and a second water flow selection means for switching water flow to the return branch pipe.
復路配管がそれぞれ2本であることを特徴とする超純水
供給装置。3. The ultrapure water supply apparatus according to claim 1, wherein the number of outgoing pipes and the number of return pipes are two.
ら使用装置への給水用配管接続部より下流側の位置又は
復路配管に、殺菌液を系外に排水する排水手段を設けた
ことを特徴とする超純水供給装置。4. The drainage means according to claim 2 or 3, wherein a drainage means for draining the sterilizing liquid out of the system is provided at a position downstream of the connection part for supplying water from each connection pipe to the device to be used or at the return pipe. Ultrapure water supply device.
前記往路配管と復路配管の間に、超純水使用装置への給
水用配管が接続されていないバイパス管を前記接続配管
と並列して設けたことを特徴とする超純水供給装置。5. The method according to claim 1, wherein
An ultrapure water supply apparatus, wherein a bypass pipe, to which a water supply pipe to an ultrapure water using apparatus is not connected, is provided in parallel with the connection pipe between the outward pipe and the return pipe.
超純水送水用の2本の往路配管と、該超純水製造装置の
戻り部に接続された超純水返送用の1本の復路配管と、
二つの片側端部が上記2本の往路配管にそれぞれ接続さ
れかつ途中で合流されてこの合流路の反対側端部が上記
1本の復路配管に接続された接続配管の複数と、各接続
配管の合流部よりも下流位置で分岐されて超純水の使用
装置に超純水を給水する給水用配管と、上記接続配管に
バイパスして2本の往路配管を1本の復路配管に接続す
るバイパス配管と、2本の往路配管のいずれかを選択し
て超純水に代えて殺菌用熱水を供給する熱水供給装置
と、該往路配管から上記各配管への熱水,超純水の通水
を切換える通水選択手段とを備えたことを特徴とする超
純水供給装置。6. An ultrapure water supply apparatus, comprising two outgoing pipes extending from a supply section of the ultrapure water production apparatus for supplying ultrapure water, and an ultrapure water return pipe connected to a return section of the ultrapure water production apparatus. One return pipe,
A plurality of connection pipes each having two one-side ends connected to the two outgoing pipes and merging along the way, and having the opposite end of the merged flow path connected to the one return pipe; And a water supply pipe that is branched at a position downstream of the junction of the ultrapure water and supplies ultrapure water to a device using ultrapure water, and two outgoing pipes are connected to one return pipe bypassing the connection pipe. A bypass pipe, a hot water supply device for selecting one of two outgoing pipes and supplying hot water for sterilization instead of ultrapure water, and hot water and ultrapure water from the outgoing pipe to each of the above pipes An ultrapure water supply device, comprising: a water flow selecting means for switching water flow.
超純水送水用の2本の往路配管と、該超純水製造装置の
戻り部に接続された超純水返送用の2本の復路配管と、
これら2本の復路配管それぞれの下流側位置に設けられ
た系外への排水配管と、中間合流路の両側が分岐されて
いて片側の各分岐端部が上記2本の往路配管に接続され
かつ反対側の各分岐端部が上記2本の復路配管にそれぞ
れ接続された接続配管の複数と、各接続配管の合流路か
ら分岐されて超純水の使用装置に超純水を給水する給水
用配管と、上記接続配管にバイパスして往路配管と復路
配管を各々1本づつの組に接続するバイパス配管と、2
本の往路配管のいずれかを選択して超純水に代えて殺菌
薬液を供給する殺菌薬液供給装置と、該往路配管から上
記各配管への殺菌薬液,超純水の通水を切換える通水選
択手段とを備えたことを特徴とする超純水供給装置。7. Two outgoing pipes for supplying ultrapure water extending from a supply section of the ultrapure water production apparatus and an ultrapure water return pipe connected to a return section of the ultrapure water production apparatus. Two return pipes,
A drainage pipe to the outside of the system provided at the downstream position of each of these two return pipes, and both sides of the intermediate junction flow path are branched, and each branch end on one side is connected to the two forward pipes, and A plurality of connection pipes whose opposite branch ends are respectively connected to the two return pipes, and a water supply for supplying ultrapure water to a device using ultrapure water which is branched from a junction of the connection pipes. A pipe, a bypass pipe connecting the outgoing pipe and the return pipe to each one set by bypassing the connecting pipe,
A disinfectant solution supply device for selecting one of the outgoing pipes and supplying a disinfectant solution instead of ultrapure water, and a water flow for switching the disinfectant solution and ultrapure water from the outgoing pipe to each of the pipes An ultrapure water supply device comprising: a selection unit.
の〜の操作で殺菌洗浄を行うことを特徴とする配管
の殺菌方法 :バイパス配管で接続された一方の往路配管から復路
配管に熱水を通水しかつ該一方の往路配管と各接続配管
の間の通水を遮断すると共に、他方の往路配管を通して
各接続配管に超純水を通水する第1工程、 :上記接続配管の少なくともいずれか一方と、超純水
が通水されている上記他方の往路配管からの通水を遮断
すると共に、熱水が通水されている上記一方の往路配管
から接続配管に熱水を通水させる第2工程、 :第2工程の接続配管に対する上記一方の往路配管か
らの熱水通水を遮断しかつ上記他方の往路配管から超純
水を通水する第3工程、 :上記第2工程と第3工程の操作を必要に応じて他の
接続配管の殺菌処理のために繰返す第4工程、 :上記一方の往路配管に対する熱水供給を遮断して超
純水を通水する第5工程。8. A method of sterilizing a pipe in the ultrapure water supply apparatus according to claim 6, wherein sterilization and cleaning are performed by the following operations: heat is supplied from one outgoing pipe connected by a bypass pipe to a return pipe. A first step of passing water and interrupting water flow between the one outgoing pipe and each connecting pipe, and passing ultrapure water to each connecting pipe through the other outgoing pipe; Block the flow of water from at least one of the outgoing pipes, through which ultrapure water is passed, and the hot water from the one outgoing pipe, through which hot water is passed, to the connection pipe. A second step of blocking the hot water flow from the one outgoing pipe to the connecting pipe in the second step and a flow of ultrapure water from the other outgoing pipe to the connecting pipe in the second step; Perform the operations of the third step and the third step as necessary. The fourth step of repeating for the: fifth step of passing water ultrapure water was shut off hot water supply to one of the outbound pipeline above.
の´〜´の操作で殺菌洗浄を行うことを特徴とする
配管の殺菌方法 ´:バイパス配管で接続された一方の往路配管から、
復路配管、更に排水配管に殺菌薬液を通液しながらこれ
らの往路配管及び復路配管と各接続配管の間の通液は遮
断すると共に、バイパス配管で接続された他方の往路配
管から、接続配管、更に復路配管に超純水を通水して超
純水製造装置に戻す第1工程、 ´:上記接続配管の少なくともいずれか一つと、超純
水が通水されている上記他方の往路配管及び復路配管と
の通水を遮断すると共に、殺菌薬液が通液されている上
記一方の往路配管及び復路配管と該接続配管とを通液さ
せる第2工程、 ´:第2工程に続き、接続配管に対する上記一方の往
路配管からの殺菌薬液の通液を遮断すると共に、上記他
方の往路配管から超純水を通水して該接続配管内を超純
水で置換する第3工程、 ´:第3工程で配管内が超純水で置換された接続配管
から上記一方の復路配管への通水を遮断すると共に、該
接続配管と上記他方の復路配管を通水させる第4工程、 ´:上記第2工程〜第4工程の操作を必要に応じて他
の接続配管の殺菌処理のために繰返す第5工程、 ´上記一方の往路配管への殺菌薬液の供給を遮断し、
かつ超純水を通水して該一方の往路配管から復路配管ま
での配管内を超純水に置換する第6工程、 ´:超純水に置換された該一方の復路配管からの排水
を停止して超純水製造装置に循環水を戻す第7工程。9. A method of sterilizing a pipe in the ultrapure water supply apparatus according to claim 7, wherein sterilization and washing are performed by the following operations (1) to (4):
While passing the sterilizing solution through the return pipe and the drain pipe, the liquid between the forward pipe and the return pipe and each connection pipe is shut off, and the connection pipe, Further, a first step of returning ultrapure water to the ultrapure water producing apparatus by passing ultrapure water through the return pipe, ′: at least one of the connection pipes, the other outward pipe through which ultrapure water is passed, and A second step of interrupting the water flow to the return pipe and passing the one of the outward pipe and the return pipe through which the germicide solution is passed and the connection pipe, ′: connection pipe following the second step A third step of interrupting the flow of the sterilizing agent solution from the one outgoing pipe to the above, and passing ultrapure water from the other outgoing pipe to replace the inside of the connecting pipe with ultrapure water. From the connection pipe whose inside was replaced with ultrapure water in 3 steps, A fourth step of interrupting the flow of water to the one return pipe and allowing the connection pipe and the other return pipe to flow, ′: performing the operations of the second to fourth steps as necessary. The fifth step which is repeated for the sterilization treatment of the pipes, 'the supply of the sterilizing agent liquid to the one outgoing pipe is cut off,
And a sixth step of passing the ultrapure water and replacing the inside of the pipe from the one outgoing pipe to the return pipe with ultrapure water, ′: draining water from the one return pipe replaced with the ultrapure water. The seventh step of stopping and returning the circulating water to the ultrapure water production apparatus.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP31527895A JP3281238B2 (en) | 1995-12-04 | 1995-12-04 | Ultrapure water supply device and sterilization method for its piping |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP31527895A JP3281238B2 (en) | 1995-12-04 | 1995-12-04 | Ultrapure water supply device and sterilization method for its piping |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH09155361A JPH09155361A (en) | 1997-06-17 |
| JP3281238B2 true JP3281238B2 (en) | 2002-05-13 |
Family
ID=18063489
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP31527895A Expired - Fee Related JP3281238B2 (en) | 1995-12-04 | 1995-12-04 | Ultrapure water supply device and sterilization method for its piping |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3281238B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2013066822A (en) * | 2011-09-21 | 2013-04-18 | Panasonic Corp | Water treatment device |
| JP6802059B2 (en) * | 2016-12-27 | 2020-12-16 | 三菱ケミカルアクア・ソリューションズ株式会社 | Purified water supply system and its operation method |
| JP6956223B2 (en) * | 2016-12-27 | 2021-11-02 | 三菱ケミカルアクア・ソリューションズ株式会社 | Purified water supply system and its operation method |
| JP6687509B2 (en) * | 2016-12-27 | 2020-04-22 | 三菱ケミカル・クリンスイ株式会社 | Purified water supply system and its operating method |
-
1995
- 1995-12-04 JP JP31527895A patent/JP3281238B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH09155361A (en) | 1997-06-17 |
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