JPH0767556B2 - Sterilization method by heat generation of pump of ultrapure water and aseptic pure water production equipment - Google Patents
Sterilization method by heat generation of pump of ultrapure water and aseptic pure water production equipmentInfo
- Publication number
- JPH0767556B2 JPH0767556B2 JP60180998A JP18099885A JPH0767556B2 JP H0767556 B2 JPH0767556 B2 JP H0767556B2 JP 60180998 A JP60180998 A JP 60180998A JP 18099885 A JP18099885 A JP 18099885A JP H0767556 B2 JPH0767556 B2 JP H0767556B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- pump
- tank
- pure water
- ultrapure
- 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.)
- Expired - Fee Related
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は、超純水、無菌純水製造装置のポンプ発熱によ
る殺菌方法に関するものである。TECHNICAL FIELD The present invention relates to a sterilization method using heat generated by a pump in an apparatus for producing ultrapure water and aseptic pure water.
超純水は、例えば半導体の製造工程において洗浄水とし
て用いられ、所定の比抵抗値や、菌、微粒子、有機物等
の不純物のない理論純水に近い水質が要求されている。
また、無菌純水は、医薬品工業や医療、化粧品、醗酵、
化学あるいは食品工業等の原料水や洗浄水用として従来
の蒸溜水や滅菌精製水に代って用いられている。そして
超純水や無菌純水の製造は、通常、逆浸透膜(RO)、限
外濾過膜(UF)や超精密濾過膜(SF)等を利用した膜分
離技術によって行なわれている。Ultrapure water is used, for example, as washing water in a semiconductor manufacturing process, and is required to have a specific resistance value and a water quality close to theoretical pure water without impurities such as bacteria, fine particles, and organic substances.
In addition, sterile pure water is used in the pharmaceutical industry, medicine, cosmetics, fermentation,
It is used in place of conventional distilled water and sterilized purified water for raw water and washing water in the chemical or food industry. The production of ultrapure water or sterile pure water is usually carried out by a membrane separation technique using a reverse osmosis membrane (RO), an ultrafiltration membrane (UF), an ultraprecision filtration membrane (SF) or the like.
ところで、これらの超純水や無菌純水の製造装置におい
ては、無菌およびパイロジェンフリーを保証するため、
殺菌対策を施して無菌状態に保持する必要がある。特
に、休日や夜間等のように装置が停止し、系内に水が滞
留する場合には系内特に膜モジュール内で微生物や菌が
増殖するため殺菌装置を使用する必要がある。このため
一般的には、原水をタンクに貯え、紫外線殺菌器、除菌
フィルタを介して再びタンクへ常時循環させる方法や熱
交換器により循環水を通常85℃〜95℃に加温し、タンク
に高温で貯水させる方法が用いられている。By the way, in these ultrapure water and sterile pure water production apparatuses, in order to guarantee sterility and pyrogen-free,
It is necessary to take sterilization measures and maintain the aseptic condition. In particular, when the apparatus is stopped such as on a holiday or at night and water is retained in the system, microorganisms and bacteria grow in the system, particularly in the membrane module, so that it is necessary to use a sterilizer. Therefore, in general, the raw water is stored in a tank, and the circulating water is usually heated to 85 ° C to 95 ° C by a heat exchanger or a method of constantly circulating it again to the tank through an ultraviolet sterilizer and a sterilization filter. A method of storing water at a high temperature is used.
このような方法を実施している従来例として、休止、停
止期間中も水を止めずに紫外線殺菌器を通して低圧循環
させたり、自動で定時に間歇的に数分間低圧高流量でフ
ラッシングをして装置内特に膜モジュール内の滞留水を
系外に排出する方式がある。As a conventional example implementing such a method, low pressure circulation through the ultraviolet sterilizer without stopping the water even during the pause and stop period, or by automatically performing intermittent flushing at low pressure and high flow rate for several minutes at regular intervals There is a method of discharging accumulated water inside the apparatus, particularly inside the membrane module, to the outside of the system.
また、熱交換器を使用して加温し、タンクを通して高温
で循環させる方法の一例を添附図面の第2図に示す。第
2図においてAはタンクで、その出口側にポンプBが配
置され、このポンプBによりタンクA内の原水を限外濾
過装置Cへ通し、限外濾過装置Cの透過水出口側で透過
水を得るようにしており、また限外濾過装置Cの濃縮水
出口側は熱交換器Dを通ってタンクAに連通している。
熱交換器DにはバルブEを介して蒸気発生源(図示して
ない)から蒸気が供給される。これにより、限外濾過装
置Cの濃縮水出口側からタンクAへ流れる際に循環水は
所要の温度に加温され、こうして循環水は温水となって
系内を循環して殺菌作用を行なうようにされている。An example of a method of heating by using a heat exchanger and circulating at high temperature through a tank is shown in FIG. 2 of the accompanying drawings. In FIG. 2, A is a tank, and a pump B is arranged at the outlet side thereof, and the raw water in the tank A is passed to the ultrafiltration device C by this pump B, and the permeated water is passed through the permeated water outlet side of the ultrafiltration device C. In addition, the concentrated water outlet side of the ultrafiltration device C communicates with the tank A through the heat exchanger D.
The heat exchanger D is supplied with steam from a steam generation source (not shown) via a valve E. As a result, the circulating water is heated to the required temperature when flowing from the concentrated water outlet side of the ultrafiltration device C to the tank A, and thus the circulating water becomes hot water and circulates in the system to perform a sterilizing action. Has been
また加温手段として上記のような熱交換器の代りにヒー
タのような他の加温手段を使用することも提案されてい
る。It has also been proposed to use other heating means such as a heater as the heating means instead of the above heat exchanger.
[発明が解決しようとする問題点] ところで、紫外線殺菌器を利用したものでは、紫外線殺
菌器のランプの管理は無論のこと、ランプの外側の石英
管の回りがスケール等によって汚れ、紫外線の透過率が
低下し、殺菌効率が低下してしまう場合があり、このた
め水に接する石英管は常にクリーン状態に保つ必要があ
る。従って石英管を定期的に取外ずして洗浄する必要が
あり、管理面で手間がかかるだけでなく、逆に汚染を持
ち込む恐れもある。[Problems to be Solved by the Invention] By the way, in the case of using an ultraviolet sterilizer, it is needless to manage the lamp of the ultraviolet sterilizer. The rate of sterilization may be reduced and the sterilization efficiency may be reduced. Therefore, it is necessary to always keep the quartz tube in contact with water in a clean state. Therefore, it is necessary to regularly remove and clean the quartz tube, which is not only time-consuming in terms of management, but also may cause contamination.
また第2図に例示したような従来例では、特別の熱エネ
ルギ源を必要とし、しかもタンクを含む全系内の水を所
要の温度に加温しているため、相当量のエネルギが必要
とされ、そして通常の純水製造運転を再開する場合には
加温されている水を常温に戻す必要があるため、普通は
系内特にタンクの水を捨てて新しい水を供給して運転を
再開している。そのためランニングコストが相当高くつ
くという問題がある。しかしながら、実際には休日や夜
間等のように装置が停止し、系内に水が滞留する場合に
問題となるのは系内全体の水中に存在また増殖する微生
物や菌よりはむしろ液体分離膜装置の膜モジュール内で
微生物や菌が増殖するのをいかにして抑えるかにある。Further, in the conventional example as illustrated in FIG. 2, a special heat energy source is required, and moreover, since the water in the entire system including the tank is heated to a required temperature, a considerable amount of energy is required. Since it is necessary to return the warmed water to room temperature when restarting the normal pure water production operation, it is normal to discard the water in the system, especially the tank, and supply new water to restart the operation. is doing. Therefore, there is a problem that running cost is considerably high. However, in practice, when the equipment is stopped, such as on a holiday or at night, and water accumulates in the system, the problem is that the liquid separation membrane is rather than the microorganisms or bacteria present or growing in the entire system water. How to prevent the growth of microorganisms and fungi in the membrane module of the device.
そこで、本発明の目的は、休日や夜間等のように装置が
停止し、系内に水が滞留する場合に、系全体に水を循環
させずに膜モジュールを含む管路部分にのみ水を循環さ
せ、しかも水を加温するのに特別の熱エネルギ源を用い
ずに循環ポンプの排熱を利用してランニングコストを大
幅に低減できる超純水、無菌純水製造装置のポンプ発熱
による殺菌方法を提供することにある。Therefore, an object of the present invention is to provide water only to the pipe line portion including the membrane module without circulating the water throughout the system when the apparatus stops and the water stays in the system such as on a holiday or at night. Ultrapure water that can circulate and can significantly reduce running costs by using the exhaust heat of the circulation pump without using a special heat energy source to heat water, and sterilization by heat generation from the pump of an aseptic pure water production system To provide a method.
[問題点を解決するための手段] 上記の目的を達成するために、本発明によれば、前処理
した原水を貯蔵するタンクと、上記タンクの出口側に連
結されたポンプと、上記ポンプにより上記タンクから供
給された原水を濾過して超純水、無菌純水として送出す
る超純水、無菌給水出口及び濃縮水を送出する濃縮水出
口を備えた液体物理膜装置と、上記ポンプ及び上記液体
分離膜装置を通る濃縮水側の閉じた配管路とを有する超
純水、無菌純水製造装置において、濾過運転停止時に、
上記濃縮水側の閉じた配管路内でその中に存在する水を
上記ポンプにより循環させると同時に上記ポンプ発熱で
昇温させ温水殺菌を行なうようにしたことを特徴として
いる。[Means for Solving the Problems] In order to achieve the above object, according to the present invention, a tank for storing pretreated raw water, a pump connected to the outlet side of the tank, and the pump are used. A liquid physical membrane device having ultrapure water for filtering raw water supplied from the tank and delivering it as sterile pure water, aseptic water supply outlet, and concentrated water outlet for delivering concentrated water, the pump and the above In the ultrapure water and sterile pure water production apparatus having a closed pipeline on the concentrated water side that passes through the liquid separation membrane device, when the filtration operation is stopped,
It is characterized in that the water existing therein is circulated by the pump in the closed pipeline on the concentrated water side, and at the same time the temperature is raised by the heat generated by the pump to sterilize the hot water.
なお、液体分離膜装置の分離膜としては、限外濾過膜モ
ジュールや逆浸透モジュールが使用され得る。An ultrafiltration membrane module or a reverse osmosis module can be used as the separation membrane of the liquid separation membrane device.
[作用] このように構成した本発明による超純水、無菌純水製造
装置のポンプ発熱による殺菌方法においては、ポンプと
液体分離膜装置とを通る閉じた配管路を設けてタンクを
通さずに水を循環させるようにしているので、循環する
水の総量は比較的少なく、そのためポンプの発熱量で循
環する水を微生物や菌の増殖を抑えるのに必要な温度ま
で十分加熱することができる。これにより液体分離膜装
置の膜モジュール内における微生物や菌の増殖は有効に
抑制され得る。[Operation] In the sterilization method by the pump heat generation of the ultrapure water and aseptic pure water production apparatus according to the present invention configured as described above, a closed pipe line passing through the pump and the liquid separation membrane device is provided so that the tank is not passed through. Since the water is circulated, the total amount of water circulated is relatively small, so that the heat of the pump can sufficiently heat the circulated water to a temperature necessary for suppressing the growth of microorganisms and bacteria. Thereby, the growth of microorganisms and fungi in the membrane module of the liquid separation membrane device can be effectively suppressed.
また、運転を再開する際には高温で循環している比較的
少量の水を常温に戻すか捨てるだけでよく、この場合に
はタンク内の水は捨ても捨てなくてもよい。Further, when restarting the operation, a relatively small amount of water circulating at a high temperature may be returned to room temperature or discarded, and in this case, the water in the tank may or may not be discarded.
[実施例] 以下、添附図面の第1図を参照して本発明の実施例につ
いて説明する。[Embodiment] An embodiment of the present invention will be described below with reference to FIG. 1 of the accompanying drawings.
第1図には本発明を実施している超純水、無菌純水製造
装置の要部の構成を示し、1はタンクてこのタンク1に
は図示してない前処理系で前処理した水が供給される。
タンク1の出口側はポンプ2を介して液体分離膜装置を
構成する限外濾過装置3の入口側に連結され、この限外
濾過装置3の透過水出口側は純水供給通路4に連通し、
濃縮水出口側は管路5を通ってポンプ2の上流に連結さ
れ、ポンプ2の限外濾過装置3とを通る循環路が形成さ
れる。FIG. 1 shows the structure of the essential parts of an apparatus for producing ultrapure water and aseptic pure water according to the present invention. Reference numeral 1 denotes a tank lever 1 which is water pretreated by a pretreatment system not shown in the tank 1. Is supplied.
The outlet side of the tank 1 is connected via a pump 2 to the inlet side of an ultrafiltration device 3 constituting a liquid separation membrane device, and the permeated water outlet side of this ultrafiltration device 3 communicates with a pure water supply passage 4. ,
A concentrated water outlet side is connected to an upstream side of the pump 2 through a pipe line 5 to form a circulation path passing through the ultrafiltration device 3 of the pump 2.
このように構成した図示実施例の装置において、通常の
運転時にはタンク1からの水はポンプ2により限外濾過
装置3に送られ、この限外濾過装置3の膜モジュールを
通って濾過されて純水供給通路4に供給される。この場
合濃縮水は管路5を通ってポンプ2の上流に戻され得
る。一方、休日や夜間等のように装置を停止させる場合
には、タンク1からポンプ2へ通じる管路は図示してな
いバルブ等により遮断され、それにより、ポンプ2と限
外濾過装置3とを通る循環路内でその中に存在する水が
ポンプ2によって循環させられ、循環する水はポンプ2
の発熱により所定の温度に加熱される。こうして特に限
外濾過装置3の膜モジュール内における微生物や菌の増
殖は効果的に抑制され得る。この場合、使用するポンプ
の発熱量に応じて循環させる水量を制御しても、あるい
は予じめ循環させる水量を決めておき、ポンプの出力を
制御して循環している水を所要の温度範囲で加熱できる
ようにしてもよい。なお、当然使用するポンプ2は、通
常の運転時すなわち純水の製造時には自己の発熱で水を
予定の温度以上に加温しないように設定され得る。In the apparatus of the illustrated embodiment configured in this way, during normal operation, the water from the tank 1 is sent to the ultrafiltration device 3 by the pump 2, filtered through the membrane module of the ultrafiltration device 3 and purified. It is supplied to the water supply passage 4. In this case, the concentrated water can be returned to the upstream of the pump 2 through the line 5. On the other hand, when the apparatus is stopped such as on a holiday or at night, the pipe line leading from the tank 1 to the pump 2 is blocked by a valve or the like (not shown), whereby the pump 2 and the ultrafiltration apparatus 3 are separated. The water existing therein is circulated by the pump 2 in the circulating circuit, and the circulating water is circulated by the pump 2.
It is heated to a predetermined temperature by the heat generation of. In this way, in particular, the growth of microorganisms and fungi in the membrane module of the ultrafiltration device 3 can be effectively suppressed. In this case, even if the amount of water to be circulated is controlled according to the calorific value of the pump used, or the amount of water to be circulated is determined in advance and the output of the pump is controlled to circulate the water in the required temperature range. You may make it possible to heat. It should be noted that the pump 2 to be used can naturally be set so as not to heat the water above a predetermined temperature by its own heat generation during normal operation, that is, during the production of pure water.
[発明の効果] 以上説明してきたように、本発明によれば、超純水、無
菌純水製造装置において、ポンプと液体分離膜装置とを
通る濃縮水側の閉じた配管路を設けてタンクを通さずに
水を循環させるようにしているので、循環する水の総量
を比較的少なくでき、そのためポンプの発熱量で循環す
る水を微生物や菌の増殖を抑えるのに必要な温度まで十
分加熱することができる。これにより膜モジュール内に
おける微生物や菌の増殖を有効に抑制できると共に、従
来装置のように特別の加熱手段や殺菌手段を用いずに、
殺菌を行なうことができ、その結果、管理の手間が省け
るだけでなく、エネルギコストの低減と共に装置の簡略
化を計ることができ、超純粋、無菌純水を低コストで精
製することができる。[Effects of the Invention] As described above, according to the present invention, in the apparatus for producing ultrapure water and aseptic pure water, a tank is provided by providing a closed pipeline on the concentrated water side that passes through the pump and the liquid separation membrane device. Since the water is circulated without passing through it, the total amount of water circulated can be relatively small, and therefore the heat of the pump heats the circulated water sufficiently to the temperature necessary to suppress the growth of microorganisms and bacteria. can do. With this, it is possible to effectively suppress the growth of microorganisms and bacteria in the membrane module, without using a special heating means or sterilizing means as in the conventional device,
Sterilization can be performed, and as a result, not only the labor for management can be saved, but also the energy cost can be reduced and the apparatus can be simplified, and ultrapure, sterile pure water can be purified at low cost.
第1図は本発明の一実施例を示す概略線図、第2図は従
来装置の一例を示す概略線図である。 図中、1:タンク、2:ポンプ、3:限外濾過装置、5:管路。FIG. 1 is a schematic diagram showing an embodiment of the present invention, and FIG. 2 is a schematic diagram showing an example of a conventional device. In the figure, 1: tank, 2: pump, 3: ultrafiltration device, 5: pipeline.
Claims (1)
タンクの出口側に連結されたポンプと、上記ポンプによ
り上記タンクから供給された原水を濾過して超純水、無
菌純水として送出する超純水、無菌純水出口及び濃縮水
を送出する濃縮水出口を備えた液体分離膜装置と、上記
ポンプ及び上記液体分離膜装置を通る濃縮水側の閉じた
配管路とを有し、濾過運転停止時に、上記濃縮水側の閉
じた配管路内でその中に存在する水を上記ポンプにより
循環させると同時に上記ポンプの発熱で昇温させ温水殺
菌を行なうようにしたことを特徴とする超純水、無菌純
水製造装置のポンプ発熱による殺菌方法。1. A tank for storing pretreated raw water, a pump connected to the outlet side of the tank, the raw water supplied from the tank by the pump is filtered and delivered as ultrapure water or sterile pure water. Ultrapure water, a sterile pure water outlet and a liquid separation membrane device having a concentrated water outlet for delivering the concentrated water, and a closed pipe path on the concentrated water side that passes through the pump and the liquid separation membrane device, When the filtration operation is stopped, the water existing in the closed pipeline on the concentrated water side is circulated by the pump and at the same time the temperature of the water is raised by the heat generated by the pump to perform hot water sterilization. Sterilization method by pump heat generation of ultrapure water and aseptic pure water production equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60180998A JPH0767556B2 (en) | 1985-08-20 | 1985-08-20 | Sterilization method by heat generation of pump of ultrapure water and aseptic pure water production equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60180998A JPH0767556B2 (en) | 1985-08-20 | 1985-08-20 | Sterilization method by heat generation of pump of ultrapure water and aseptic pure water production equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6242789A JPS6242789A (en) | 1987-02-24 |
JPH0767556B2 true JPH0767556B2 (en) | 1995-07-26 |
Family
ID=16092943
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60180998A Expired - Fee Related JPH0767556B2 (en) | 1985-08-20 | 1985-08-20 | Sterilization method by heat generation of pump of ultrapure water and aseptic pure water production equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0767556B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4949658B2 (en) * | 2005-06-22 | 2012-06-13 | ダイセン・メンブレン・システムズ株式会社 | Dialysis water production apparatus and sterilization method thereof |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60216808A (en) * | 1984-04-10 | 1985-10-30 | Daicel Chem Ind Ltd | Process for preventing reverse contamination |
JPS6161689A (en) * | 1984-08-31 | 1986-03-29 | Hitachi Ltd | Apparatus for producing pure water |
-
1985
- 1985-08-20 JP JP60180998A patent/JPH0767556B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPS6242789A (en) | 1987-02-24 |
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