JP3480458B2 - Sterilization method - Google Patents
Sterilization methodInfo
- Publication number
- JP3480458B2 JP3480458B2 JP2001244030A JP2001244030A JP3480458B2 JP 3480458 B2 JP3480458 B2 JP 3480458B2 JP 2001244030 A JP2001244030 A JP 2001244030A JP 2001244030 A JP2001244030 A JP 2001244030A JP 3480458 B2 JP3480458 B2 JP 3480458B2
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen peroxide
- sterilization
- water
- peroxide solution
- concentration
- 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 - Lifetime
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- Apparatus For Disinfection Or Sterilisation (AREA)
- Cleaning By Liquid Or Steam (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は殺菌方法に係り、特に、
純水又は超純水を製造する水処理機器、例えば、超純水
端末フィルター(具体的には、限外濾過膜分離装置等)
の内部やこれに連絡する配管内部、或いは、洗浄装置内
配管や洗浄槽を殺菌する方法であって、低濃度の過酸化
水素溶液を用いて効率よく殺菌することができる殺菌方
法に関する。FIELD OF THE INVENTION The present invention relates to a sterilization method, and
Water treatment equipment for producing pure water or ultrapure water , for example, ultrapure water terminal filter (specifically, ultrafiltration membrane separator, etc.)
The present invention relates to a method of sterilizing the inside of a pipe, the inside of a pipe connected to the pipe, or a pipe inside a cleaning device or a cleaning tank, which can be efficiently sterilized using a low-concentration hydrogen peroxide solution.
【0002】[0002]
【従来の技術】従来、超純水端末フィルター等の水処理
機器やその配管系内の殺菌には、1重量%(以下、単に
「%」と称す。)程度の過酸化水素溶液を用い、システ
ム内を循環処理していた。例えば、特開昭62−254
805号公報には、超純水製造装置の末端逆浸透膜装置
を、0.5〜1%の過酸化水素溶液で殺菌処理した後、
45℃以上の加熱純水で洗浄することが記載されてい
る。また、特開平3−202130号公報には、中空糸
型膜モジュールに0.5〜5%の過酸化水素溶液を封入
又は通水後、温水又は熱水を通水して洗浄することが記
載されている。しかして、この特開平3−202130
号公報には、0.5%未満の過酸化水素溶液では殺菌或
いは滅菌の効果が乏しいことが記載されている。2. Description of the Related Art Conventionally, about 1% by weight (hereinafter simply referred to as "%") of hydrogen peroxide solution has been used for sterilization of water treatment equipment such as ultrapure water terminal filters and its piping system. The system was circulating. For example, JP-A-62-254
In Japanese Patent No. 805, after sterilizing a terminal reverse osmosis membrane device of an ultrapure water producing device with a 0.5 to 1% hydrogen peroxide solution,
It is described that washing with pure water heated at 45 ° C. or higher is performed. Further, in JP-A-3-202130, it is described that a hollow fiber membrane module is filled with or filled with 0.5 to 5% hydrogen peroxide solution and then hot water or hot water is passed through for washing. Has been done. Then, this Japanese Patent Laid-Open No. 3-202130
The publication describes that a hydrogen peroxide solution of less than 0.5% has a poor sterilizing or sterilizing effect.
【0003】[0003]
【発明が解決しようとする課題】上述の如く、従来の殺
菌方法においては、殺菌効果を高めるために用いる過酸
化水素溶液の濃度を高く(約1%)設定していることか
ら、
過酸化水素溶液による殺菌処理終了後、洗浄に長時
間を要する。このため、全洗浄工程に要する時間が長
い。因みに、殺菌の準備から洗浄、その後の装置立ち上
げまでの全工程は半日から1日を要する。
過酸化水素濃度が高いことから、薬剤の使用量が多
く(例えば、保有水量10m3とすると、35%過酸化
水素溶液約300リットルが必要である)、また、作業
には多大な危険が伴う。
といった問題があった。As described above, in the conventional sterilization method, since the concentration of the hydrogen peroxide solution used to enhance the sterilizing effect is set high (about 1%), It takes a long time to wash after the sterilization with the solution is completed. Therefore, the time required for the entire cleaning process is long. By the way, the whole process from preparation for sterilization to cleaning and subsequent start-up of the device requires half a day to one day. Since the concentration of hydrogen peroxide is high, the amount of chemicals used is large (for example, if the amount of water held is 10 m 3 , about 300 liters of 35% hydrogen peroxide solution is required), and the work is extremely dangerous. . There was such a problem.
【0004】しかも、このような高濃度過酸化水素溶液
を用いても、殺菌浸漬時間として最低2時間は必要であ
り、しかも、過酸化水素濃度を濃くしても完全殺菌する
ことは困難であった。この理由は、生菌が配管や洗浄槽
の壁面に付着する場合、生菌表面に多糖類からなるポリ
マーを出して壁表面に付着する。そのため、このポリマ
ー中を殺菌剤である過酸化水素が浸透して生菌体内に到
達するためにある程度の時間を要するためと考えられ
る。Moreover, even if such a high-concentration hydrogen peroxide solution is used, a sterilization dipping time of at least 2 hours is required, and complete sterilization is difficult even if the hydrogen peroxide concentration is increased. It was The reason for this is that when viable bacteria adhere to the wall surface of a pipe or a cleaning tank, a polymer consisting of a polysaccharide is exposed on the surface of the viable bacteria and adheres to the wall surface. Therefore, it is considered that a certain amount of time is required for hydrogen peroxide, which is a bactericide, to penetrate into the polymer and reach the inside of the viable cells.
【0005】なお、超純水製造装置の端末配管や洗浄槽
内を短時間で完全に殺菌する方法としては、熱水(80
℃以上)や蒸気等を用いる方法があるが、このような方
法は、加熱のためのエネルギー費用がかかること及び端
末配管や洗浄槽の材質を耐熱性にする必要があり、設備
費(熱交換器や配管等)に莫大な費用がかかるという欠
点がある。As a method for completely sterilizing the terminal pipe and the inside of the cleaning tank of the ultrapure water production system in a short time, hot water (80
There is a method that uses heat (such as ℃ or more) or steam, but such a method requires energy cost for heating and it is necessary to make the material of the terminal piping and the cleaning tank heat resistant, so equipment cost (heat exchange) There is a disadvantage that enormous cost is required for equipment and piping).
【0006】また、配管材質の面から、このような熱水
又は蒸気による殺菌法を適用できない場合もある。例え
ば、超純水の端末配管やクリーンルーム内廃水配管は、
通常のポリ塩化ビニル製配管(非耐熱性)を使用する場
合が多く、ここで使用される通常のポリ塩化ビニル製配
管の実用的な耐熱温度は最高45℃であるため、熱水や
蒸気を流すことはできない。In some cases, such a sterilization method using hot water or steam cannot be applied from the viewpoint of piping material. For example, the terminal pipe for ultrapure water and the wastewater pipe in the clean room are
Normal polyvinyl chloride piping (non-heat resistant) is often used, and the practical heat resistant temperature of the ordinary polyvinyl chloride piping used here is 45 ° C at the maximum, so hot water or steam should not be used. It cannot be washed away.
【0007】本発明は上記従来の問題点を解決し、水処
理機器の内部及び/又はこれと連絡する配管の内部を、
過酸化水素と接触させて殺菌する方法において、低濃度
過酸化水素溶液を用いて、短時間で効率的に安価に殺菌
すると共に、殺菌処理後の洗浄処理を容易とする殺菌方
法を提供することを目的とする。The present invention solves the above-mentioned problems of the prior art, and the inside of the water treatment equipment and / or the inside of the pipe communicating with the equipment is
In a method of sterilizing by contacting with hydrogen peroxide, using a low-concentration hydrogen peroxide solution, to sterilize efficiently and inexpensively in a short time, and to provide a sterilizing method that facilitates cleaning treatment after sterilization treatment. With the goal.
【0008】[0008]
【課題を解決するための手段】請求項1の殺菌方法は、
純水又は超純水を製造する水処理機器の内部及び/又は
これと連絡する配管の内部を、過酸化水素と接触させて
殺菌する方法において、0.01〜0.1%の過酸化水
素のみを含む溶液を30〜60℃に加温して使用するこ
とを特徴とする。A sterilizing method according to claim 1 is
In the method of sterilizing the inside of a water treatment device for producing pure water or ultrapure water and / or the inside of a pipe communicating with the same with hydrogen peroxide, 0.01 to 0.1% hydrogen peroxide is used. It is characterized in that a solution containing only is heated to 30 to 60 ° C. before use.
【0009】請求項2の殺菌方法は、請求項1の方法に
おいて、過酸化水素溶液を送水ポンプで通水循環するこ
とにより、該過酸化水素溶液を送水ポンプの発熱で加温
することを特徴とする。A sterilizing method according to a second aspect is the method according to the first aspect, characterized in that the hydrogen peroxide solution is circulated by a water pump to heat the hydrogen peroxide solution by the heat of the water pump. To do.
【0010】以下に本発明を詳細に説明する。The present invention will be described in detail below.
【0011】本発明の方法においては、純水又は超純水
を製造する水処理機器の内部及び/又はこれと連絡する
配管の内部を、30〜60℃に加温した、0.01〜
0.1%の過酸化水素のみを含む溶液と接触させて殺菌
する。In the method of the present invention, pure water or ultrapure water is used.
The inside of the water treatment equipment for producing water and / or the inside of the pipe communicating with this is heated to 30 to 60 ° C., 0.01 to
Sterilize by contact with a solution containing only 0.1% hydrogen peroxide.
【0012】用いる過酸化水素溶液の温度が30℃未満
では、このような低濃度過酸化水素溶液により十分な殺
菌を行なえない場合がある。過酸化水素溶液の温度が6
0℃を超えると、加温コストが高くつく上に、配管等に
耐熱性材料を用いる必要があるなどの不具合が生じる。If the temperature of the hydrogen peroxide solution used is less than 30 ° C., it may not be possible to perform sufficient sterilization with such a low-concentration hydrogen peroxide solution. The temperature of the hydrogen peroxide solution is 6
If the temperature exceeds 0 ° C., the heating cost becomes high and there is a problem that a heat-resistant material needs to be used for the piping and the like.
【0013】また、過酸化水素溶液の過酸化水素濃度が
0.01%未満では十分な殺菌効果が得られず、0.1
%を超えると本発明の低濃度化の目的にそぐわない。If the hydrogen peroxide concentration of the hydrogen peroxide solution is less than 0.01%, a sufficient bactericidal effect cannot be obtained, and
If it exceeds%, it does not meet the purpose of the present invention for lowering the concentration.
【0014】本発明の殺菌方法は、30〜60℃に加温
した0.01〜0.1%の過酸化水素溶液を用いること
以外は、通常の殺菌方法と同様に行なうことができる
が、好ましくは、過酸化水素溶液を送水ポンプで通水循
環し、過酸化水素溶液を送水ポンプの発熱で所定温度に
加温するのが、加温コスト、加温設備等の面で有利であ
る。The sterilization method of the present invention can be carried out in the same manner as a usual sterilization method except that a 0.01 to 0.1% hydrogen peroxide solution heated to 30 to 60 ° C. is used. Preferably, it is advantageous in terms of heating cost, heating equipment and the like that the hydrogen peroxide solution is circulated by a water feed pump and the hydrogen peroxide solution is heated to a predetermined temperature by heat generation of the water feed pump.
【0015】本発明の方法に従って殺菌処理した後は、
常法に従って、水洗浄、必要に応じて超純水による通水
洗浄を行ない、その後装置の立ち上げを行なう。この洗
浄に際しても、本発明においては低濃度過酸化水素溶液
を用いることから、洗浄時間、洗浄水量の大幅な低減が
図れる。因みに、この洗浄時間は30〜60分程度で十
分な洗浄効果が得られる。After sterilization according to the method of the present invention,
According to a conventional method, washing with water and, if necessary, washing with ultrapure water are carried out, and then the apparatus is started up. Also in this cleaning, since the low-concentration hydrogen peroxide solution is used in the present invention, the cleaning time and the amount of cleaning water can be greatly reduced. By the way, a sufficient cleaning effect can be obtained when the cleaning time is about 30 to 60 minutes.
【0016】このような本発明の殺菌方法の適用分野と
しては例えば、次のようなものが挙げられるが、本発明
は何ら以下の分野に限定されるものではないことは言う
までもない。The fields to which the sterilizing method of the present invention is applied include, for example, the following, but it goes without saying that the present invention is not limited to the following fields.
【0017】(1) 超純水サブシステム内装置(限外濾過
膜分離装置、イオン交換塔及びイオン交換樹脂、タン
ク)及び端末配管網の殺菌
(2) 洗浄装置内配管及び洗浄槽の殺菌
(3) 超純水1次純水系逆浸透膜分離装置並びにイオン交
換塔及びイオン交換樹脂の殺菌
(4) 回収系システム内(逆浸透膜分離装置、イオン交換
装置、配管、タンク等)の殺菌
(5) 原子力発電所、火力発電所純水製造システム(タン
ク、濾過器、イオン交換装置等)及び配管系の殺菌(1) Sterilization of ultrapure water subsystem internal equipment (ultrafiltration membrane separator, ion exchange tower and ion exchange resin, tank) and terminal piping network (2) Sterilization of washing equipment internal piping and washing tank ( 3) Sterilization of ultrapure water primary pure water type reverse osmosis membrane separation device and ion exchange tower and ion exchange resin (4) Sterilization of recovery system (reverse osmosis membrane separation device, ion exchange device, piping, tank, etc.) ( 5 ) Sterilization of pure water production systems (tanks, filters, ion exchange devices, etc.) and piping systems for nuclear power plants and thermal power plants
【0018】[0018]
【作用】過酸化水素溶液を加温して、その温度を30〜
60℃に上昇させることにより、過酸化水素濃度を低く
設定することができ、過酸化水素濃度0.01〜0.1
%の低濃度で、短時間にほぼ完全な殺菌が可能となる。
例えば、過酸化水素濃度0.01%程度の過酸化水素溶
液を用いて、約30分で完全殺菌が可能となる。[Function] The hydrogen peroxide solution is heated to a temperature of 30-
By raising the temperature to 60 ° C., the hydrogen peroxide concentration can be set low, and the hydrogen peroxide concentration of 0.01 to 0.1
With a low concentration of%, almost complete sterilization is possible in a short time.
For example, complete sterilization is possible in about 30 minutes using a hydrogen peroxide solution having a hydrogen peroxide concentration of about 0.01%.
【0019】これは、加温過酸化水素溶液であれば、前
述の生菌表面に形成されたポリマー中を殺菌剤である過
酸化水素が効率的に浸透して短時間で生菌体内に到達し
て効果的に殺菌するためと考えられる。In the case of a warmed hydrogen peroxide solution, hydrogen peroxide, which is a bactericidal agent, efficiently permeates the polymer formed on the surface of the above-mentioned viable bacteria and reaches the inside of the viable cells within a short time. It is thought that this is for effective sterilization.
【0020】このように、低濃度過酸化水素溶液での殺
菌が可能になったことから、薬剤の使用量を大幅に減ら
すことができる。例えば、保有水量10m3とすると3
5%過酸化水素溶液約3リットルで殺菌が可能である。
また、使用濃度が低いことから、作業の危険性の面で大
幅な改善が図れる。Since the sterilization with the low-concentration hydrogen peroxide solution has become possible in this way, the amount of the drug used can be greatly reduced. For example, if the amount of water held is 10 m 3 , then 3
Sterilization is possible with about 3 liters of a 5% hydrogen peroxide solution.
In addition, since the concentration used is low, the work risk can be greatly improved.
【0021】また、通常のポリ塩化ビニル製配管への適
用も可能であり、部材材質を耐熱性とすることなく、効
率的な殺菌を行なえる。Further, it can be applied to ordinary polyvinyl chloride pipes, and efficient sterilization can be performed without making the material of the members heat resistant.
【0022】しかして、殺菌処理後は、容易かつ短時間
で洗浄することができる。Therefore, after the sterilization treatment, it can be washed easily and in a short time.
【0023】特に、請求項2の方法に従って、過酸化水
素溶液の加温に送水ポンプの発熱を利用することによ
り、過酸化水素溶液の加温、循環を容易かつ低コストに
て行なうことができ、工業的に極めて有利である。例え
ば、過酸化水素溶液の通水循環のための送水ポンプの発
熱によれば、過酸化水素溶液の温度を約40℃程度にま
で上昇させることができる。In particular, according to the method of claim 2, by utilizing the heat generation of the water feed pump to heat the hydrogen peroxide solution, the hydrogen peroxide solution can be heated and circulated easily and at low cost. , Industrially very advantageous. For example, the temperature of the hydrogen peroxide solution can be raised to about 40 ° C. by the heat generation of the water pump for circulating the hydrogen peroxide solution.
【0024】[0024]
【実施例】以下に、実験例、実施例及び比較例を挙げて
本発明をより具体的に説明する。EXAMPLES The present invention will be described more specifically below with reference to experimental examples, examples and comparative examples.
【0025】実験例1
表1に示す過酸化水素濃度及び温度の過酸化水素溶液を
用い、この過酸化水素溶液中にガラスのテストピース
(10cm2)を浸漬し、テストピース1個当りのコロ
ニー数の経時変化を調べることにより、過酸化水素溶液
の温度及び過酸化水素濃度と殺菌効果との関係を確認す
る試験を行なった。結果を表1に示す。Experimental Example 1 Using a hydrogen peroxide solution having the hydrogen peroxide concentration and temperature shown in Table 1, a glass test piece (10 cm 2 ) was immersed in this hydrogen peroxide solution, and a colony was formed per test piece. A test for confirming the relationship between the temperature and the hydrogen peroxide concentration of the hydrogen peroxide solution and the bactericidal effect was conducted by examining the change with time of the number. The results are shown in Table 1.
【0026】なお、表1中、○、△、×は下記のものを
示し、またカッコ内は確認コロニー数を示す。In Table 1, ◯, Δ, and × indicate the following, and the numbers in parentheses indicate the number of confirmed colonies.
【0027】 ○:確認コロニー数 10個以下/テストピース △:確認コロニー数 10〜1000個/テストピース ×:確認コロニー数 1000個以上/テストピース[0027] ○: 10 or less confirmed colonies / test piece △: Number of confirmed colonies 10 to 1000 / test piece X: 1000 or more confirmed colonies / test piece
【0028】[0028]
【表1】 [Table 1]
【0029】表1より、30〜60℃の温度に加温され
た、過酸化水素濃度0.01〜0.1%の過酸化水素溶
液であれば、短時間で良好な殺菌効果を得ることができ
ることが明らかである。From Table 1, it is possible to obtain a good bactericidal effect in a short time with a hydrogen peroxide solution heated to a temperature of 30 to 60 ° C. and having a hydrogen peroxide concentration of 0.01 to 0.1%. It is clear that
【0030】実施例1
本発明の殺菌方法を、実際の超純水製造装置の二次純水
製造装置及び端末配管ラインに適用した。図1に適用し
た二次純水製造装置の系統図を示す。Example 1 The sterilization method of the present invention was applied to a secondary pure water production system and a terminal piping line of an actual ultrapure water production system. FIG. 1 shows a system diagram of the secondary pure water production apparatus applied.
【0031】図1中、1はタンク(容量2m3)、2は
ポンプ、3は紫外線殺菌装置、4は混床式イオン交換
塔、5は限外(UF)膜分離装置である。11は、一次
純水製造装置で得られた一次純水の導入配管、12、1
3、14はそれぞれ前工程の機器から後工程へ送水する
配管、15は洗浄時に、必要に応じて混床式イオン交換
塔をバイパスすることができるように設けられたバイパ
ス配管、16は端末配管ライン(ポリ塩化ビニル製)、
17は過酸化水素溶液の供給配管である。In FIG. 1, 1 is a tank (capacity: 2 m 3 ), 2 is a pump, 3 is an ultraviolet sterilizer, 4 is a mixed bed type ion exchange column, and 5 is an ultra UF membrane separator. Reference numeral 11 is a pipe for introducing primary pure water obtained by the primary pure water producing apparatus, and 12, 1
3 and 14 are pipes for sending water from the equipment of the previous process to the subsequent process, 15 is a bypass pipe provided so as to be able to bypass the mixed bed type ion exchange tower at the time of cleaning, and 16 is a terminal pipe Line (made of polyvinyl chloride),
Reference numeral 17 is a hydrogen peroxide solution supply pipe.
【0032】この系内における所定位置の生菌数は表2
に示す通りであったので、本発明の殺菌方法に従って殺
菌処理を行なった。まず、系内のタンク2の水位を通常
の25%(約500リットル)とすると共に、1次純水
の導入を停止して、ポンプ3により系内の水を循環通水
したところ、系内の水温は40℃に加温された。その
後、配管17より35%過酸化水素溶液をタンク2に投
入し、系内の過酸化水素濃度を0.01%に調節した。Table 2 shows the viable cell count at a predetermined position in this system.
Therefore, the sterilization treatment was performed according to the sterilization method of the present invention. First, the water level in the tank 2 in the system was set to 25% (about 500 liters) of the normal level, the introduction of primary pure water was stopped, and the water in the system was circulated through the pump 3. The water temperature was heated to 40 ° C. Then, a 35% hydrogen peroxide solution was introduced into the tank 2 through the pipe 17 to adjust the hydrogen peroxide concentration in the system to 0.01%.
【0033】このような殺菌処理を1時間行なった後、
超純水による通水洗浄を60分行ない、殺菌及び洗浄後
の生菌数を調べ、結果を表2に示した。After performing such sterilization treatment for 1 hour,
Washing with ultrapure water was carried out for 60 minutes, the number of viable bacteria after sterilization and washing was examined, and the results are shown in Table 2.
【0034】比較例1
実施例1において、ポンプによる予備通水による加温を
行なわず、温度20〜23℃の過酸化水素溶液を用い
て、1時間殺菌処理を行なったこと以外は同様にして殺
菌洗浄処理を行ない、殺菌及び洗浄後の生菌数を調べ結
果を表2に示した。Comparative Example 1 The same procedure as in Example 1 was carried out except that the heating was not performed by preliminarily passing water through a pump, and a sterilization treatment was performed for 1 hour using a hydrogen peroxide solution at a temperature of 20 to 23 ° C. After sterilization and washing treatment, the number of viable bacteria after sterilization and washing was examined, and the results are shown in Table 2.
【0035】[0035]
【表2】 [Table 2]
【0036】表2より、本発明の殺菌方法によれば、低
濃度過酸化水素溶液を用いて、系内を十分に殺菌できる
ことが明らかである。From Table 2, it is clear that according to the sterilization method of the present invention, the inside of the system can be sufficiently sterilized by using the low concentration hydrogen peroxide solution.
【0037】[0037]
【発明の効果】以上詳述した通り、本発明の殺菌方法に
よれば、低濃度過酸化水素溶液を用いて、短時間でほぼ
完全に純水又は超純水を製造する水処理機器やその配管
系の内部を殺菌することができる。As described above in detail, according to the sterilization method of the present invention, a water treatment apparatus for producing pure water or ultrapure water in a short time using a low-concentration hydrogen peroxide solution and a method thereof. The inside of the piping system can be sterilized.
【0038】従って、本発明の方法によれば、
(i) 殺菌処理時間の短縮と共に、過酸化水素濃度の低
濃度化によるその後の洗浄処理時間の短縮が図れ、結果
として、殺菌、洗浄及び装置立ち上げに要する時間を大
幅に短縮できる。
(ii) 過酸化水素濃度の低濃度化により、薬剤コストの
大幅な低減が図れる。
(iii) 過酸化水素濃度の低濃度化により、作業の危険性
が大幅に改善される。
(iv) 配管材料等に耐熱性材料を必要とせず、塩化ビニ
ル製配管等の従来の部材に有効に適用できる。等の効果
が奏され、工業的に極めて有利である。Therefore, according to the method of the present invention, (i) the sterilization processing time can be shortened, and the subsequent cleaning processing time can be shortened by reducing the hydrogen peroxide concentration. The time required for startup can be greatly reduced. (ii) By lowering the concentration of hydrogen peroxide, the drug cost can be significantly reduced. (iii) By reducing the concentration of hydrogen peroxide, the risk of work is greatly reduced. (iv) No heat-resistant material is required for the piping material, etc., and it can be effectively applied to conventional members such as vinyl chloride piping. And the like, and is industrially extremely advantageous.
【0039】特に、請求項2の方法によれば、送水ポン
プの発熱を利用して、過酸化水素溶液を容易かつ効率的
に、低コストにて加温することができ、極めて有利であ
る。In particular, according to the method of claim 2, the heat of the water pump can be used to heat the hydrogen peroxide solution easily and efficiently at low cost, which is extremely advantageous.
【図1】実施例1において殺菌処理を行なった二次純水
製造装置の系統図である。FIG. 1 is a system diagram of a secondary pure water production apparatus that has been sterilized in Example 1.
1 タンク 2 ポンプ 3 紫外線殺菌装置 4 混床式イオン交換塔 5 限外膜分離装置 1 tank 2 pumps 3 UV sterilizer 4 Mixed bed type ion exchange tower 5 Ultramembrane separation device
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI B08B 3/08 B08B 3/08 Z (58)調査した分野(Int.Cl.7,DB名) C02F 1/50 A61L 2/16 B01D 65/00 B08B 3/08 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI B08B 3/08 B08B 3/08 Z (58) Fields investigated (Int.Cl. 7 , DB name) C02F 1/50 A61L 2 / 16 B01D 65/00 B08B 3/08
Claims (2)
内部及び/又はこれと連絡する配管の内部を、過酸化水
素と接触させて殺菌する方法において、 0.01〜0.1重量%の過酸化水素のみを含む溶液を
30〜60℃に加温して使用することを特徴とする殺菌
方法。1. A method of sterilizing by contacting the inside of a water treatment device for producing pure water or ultrapure water and / or the inside of a pipe communicating therewith with hydrogen peroxide to sterilize, A sterilization method comprising heating a solution containing only hydrogen peroxide in a weight percentage to 30 to 60 ° C. before use.
することにより、該過酸化水素溶液を送水ポンプの発熱
で加温する請求項1に記載の殺菌方法。2. The sterilization method according to claim 1, wherein the hydrogen peroxide solution is circulated by a water supply pump to heat the hydrogen peroxide solution by heat generation of the water supply pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001244030A JP3480458B2 (en) | 2001-08-10 | 2001-08-10 | Sterilization method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001244030A JP3480458B2 (en) | 2001-08-10 | 2001-08-10 | Sterilization method |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP22715892A Division JP3237222B2 (en) | 1992-08-26 | 1992-08-26 | Sterilization method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2002166283A JP2002166283A (en) | 2002-06-11 |
| JP3480458B2 true JP3480458B2 (en) | 2003-12-22 |
Family
ID=19074027
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2001244030A Expired - Lifetime JP3480458B2 (en) | 2001-08-10 | 2001-08-10 | Sterilization method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3480458B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7018529B2 (en) | 2003-03-14 | 2006-03-28 | Kurita Water Industries Ltd. | System for producing ultrapure water |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101407831B1 (en) * | 2007-03-30 | 2014-06-17 | 쿠리타 고교 가부시키가이샤 | Method of cleaning sterilization of ultrapure water production system |
| SG11201600470XA (en) | 2013-07-24 | 2016-02-26 | Kurita Water Ind Ltd | Ultrapure water production system, ultrapure water production feed system, and method for cleaning thereof |
-
2001
- 2001-08-10 JP JP2001244030A patent/JP3480458B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7018529B2 (en) | 2003-03-14 | 2006-03-28 | Kurita Water Industries Ltd. | System for producing ultrapure water |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2002166283A (en) | 2002-06-11 |
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