JP2610669B2 - Processing method of membrane module - Google Patents
Processing method of membrane moduleInfo
- Publication number
- JP2610669B2 JP2610669B2 JP32282488A JP32282488A JP2610669B2 JP 2610669 B2 JP2610669 B2 JP 2610669B2 JP 32282488 A JP32282488 A JP 32282488A JP 32282488 A JP32282488 A JP 32282488A JP 2610669 B2 JP2610669 B2 JP 2610669B2
- Authority
- JP
- Japan
- Prior art keywords
- membrane module
- membrane
- alcohol
- formalin
- module
- 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
Links
Description
【発明の詳細な説明】 <産業上の利用分野> 本発明は膜モジュールをホルムアルデヒド水溶液に継
続的に浸漬する場合、その直後での膜モジュールの処理
方法に関するものである。Description: TECHNICAL FIELD The present invention relates to a method for treating a membrane module immediately after the membrane module is continuously immersed in an aqueous formaldehyde solution.
<従来の技術> 食品・医薬の分野において、分離、精製、濃縮等を膜
モジュールによって行う場合、衛生上、殺菌乃至は菌の
繁殖防止が重大な問題となる。而して、膜モジュールの
比較的長期にわたる運休時には、膜モジュール内の原液
をホルマリンで置換し、原液中の栄養によって有害菌が
繁殖するのを防止している。このようにして、膜モジュ
ールを、その運休中、ホルマリンによって保存し、再運
転時には、膜モジュール内からホルマリンを排出し、膜
モジュールの膜面を純水で洗浄している。<Conventional Technology> In the field of food and medicine, when separation, purification, concentration, etc. are performed by a membrane module, sterilization or prevention of bacterial growth is a serious problem from a sanitary point of view. Thus, when the membrane module is out of service for a relatively long time, the stock solution in the membrane module is replaced with formalin to prevent harmful bacteria from growing due to nutrients in the stock solution. In this way, the membrane module is preserved in formalin during its suspension, and at the time of restart, formalin is discharged from the inside of the membrane module and the membrane surface of the membrane module is washed with pure water.
<解決しようとする課題> しかしながら、本発明者等の経験によれば、この水洗
後での膜モジュールの透過水量は運転停止時での透過水
量に較べて相当に低く、例えば、芳香族ポリアミド系逆
浸透膜を用いた逆浸透膜モジュールの場合、その低下割
合は40%にも達する。<Problem to be Solved> However, according to the experience of the present inventors, the permeated water amount of the membrane module after the water washing is considerably lower than the permeated water amount when the operation is stopped. In the case of a reverse osmosis membrane module using a reverse osmosis membrane, the reduction ratio reaches as much as 40%.
本発明の目的は、かかる知見に基づき、その問題を解
決すべく、膜モジュールを高い透過水量で運転すること
を可能にする膜モジュールの処理方法を提供することに
ある。An object of the present invention is to provide a method for treating a membrane module that enables the membrane module to be operated with a high permeated water amount, based on such knowledge, in order to solve the problem.
<課題を解決するための手段> 本発明に係る膜モジュールの処理方法は、膜モジュー
ルの膜面がホルムアルデヒド水溶液に継続的に接触され
たのち、アルカリ性に調整したアルコールによってその
膜面を処理したうえで、膜モジュールを運転することを
特徴とする方法である。<Means for Solving the Problems> In the method for treating a membrane module according to the present invention, after the membrane surface of the membrane module is continuously contacted with an aqueous formaldehyde solution, the membrane surface is treated with an alcohol adjusted to be alkaline. And operating the membrane module.
本発明は、半透膜を用いた膜モジュールに適用される
が、特に逆浸透膜を用いたモジュールに効果があり、就
中、芳香族ポリアミド系逆浸透膜に有効である。The present invention is applied to a membrane module using a semipermeable membrane, and is particularly effective for a module using a reverse osmosis membrane, and is particularly effective for an aromatic polyamide-based reverse osmosis membrane.
上記、膜面がホルムアルデヒド水溶液に継続的に接触
される場合とは、通常、膜モジュールの比較的長期に互
る運転停止時、膜モジュール内の残存原液(例えば、食
品加工原料液)を排出し、その排出あとにホルマリン
(ホルルアルデヒドの37%水溶液)を充填し、この状態
で膜モジュールを保存する場合をいう。The above-mentioned case where the membrane surface is continuously contacted with the aqueous formaldehyde solution usually means that when the operation of the membrane module is stopped for a relatively long time, the remaining undiluted liquid (for example, a food processing raw material liquid) in the membrane module is discharged. After that, it is filled with formalin (a 37% aqueous solution of formalaldehyde), and the membrane module is stored in this state.
アルカリ性に調整したアルコールによる膜面の処理に
は、ホルマリンに接触した膜面の当該アルコールに浸漬
する方法、或いは、当該アルコールを無加圧状態で循環
させる方法を用いることができる。For the treatment of the film surface with the alcohol adjusted to be alkaline, a method of immersing the film surface in contact with formalin in the alcohol or a method of circulating the alcohol in a non-pressurized state can be used.
アルコールにはエタノール、メタノール等を用いるこ
とができ、アルカリ化のためにアルカリ性物質には、水
酸化ナトリウム、ヒドラジン、アンモニア等を用いるこ
とができる。Ethanol, methanol and the like can be used as the alcohol, and sodium hydroxide, hydrazine, ammonia and the like can be used as the alkaline substance for alkalinization.
アルコールをアルカリ性に調整するには、濃度10〜10
0%のアルコールにアルカリ性物質を添加してPH9〜12に
調整すればよい。To adjust the alcohol to alkaline, the concentration should be 10 to 10
The pH may be adjusted to 9 to 12 by adding an alkaline substance to 0% alcohol.
<実施例の説明> 以下、本発明の実施例について説明する。<Description of Examples> Hereinafter, examples of the present invention will be described.
実施例 1 使用膜モジュールは、膜として膜面積7m2の芳香族ポ
リアミド系逆浸透膜を用いたスパイラル形であり、運転
圧は15Kgf/cm2、初期透過水量(原水は水道水)は5.2m3
/d at25℃である。Example 1 The membrane module used was a spiral type using an aromatic polyamide reverse osmosis membrane having a membrane area of 7 m 2 as the membrane, the operating pressure was 15 kgf / cm 2 , and the initial permeate water amount (raw water was tap water) was 5.2 m 3.
/ d at 25 ° C.
この膜モジュールの運転により、水道水を5日間、純
水処理し、次いで運転を停止し、残存水を0.5%ホルマ
リンで置換し、この状態を7日間保持した。この7日後
において、ホルマリンを排出し、透過水量を測定したと
ころ、初期透過水量の60%であった。By operating this membrane module, tap water was treated with pure water for 5 days, then the operation was stopped, the remaining water was replaced with 0.5% formalin, and this state was maintained for 7 days. Seven days later, formalin was discharged, and the amount of permeated water was measured. As a result, it was 60% of the initial permeated water amount.
そこで、濃度50%のエタノールを水酸化ナトリウムに
よりPH=11に調整し、このアルコールにモジュールの膜
面を30分間浸漬し、その後、純水によって10分間水洗し
た。この水洗後に、逆浸透膜の透過水量を測定したこ
ろ、初期透過水量にまで回復していた。Therefore, 50% ethanol was adjusted to PH = 11 with sodium hydroxide, the membrane surface of the module was immersed in this alcohol for 30 minutes, and then washed with pure water for 10 minutes. After the water washing, when the amount of permeated water of the reverse osmosis membrane was measured, it had recovered to the initial amount of permeated water.
実施例 2 実施例1に対し、アルコールとして、濃度50%のエタ
ノールをヒドラジンにより、P=10に調整したものを使
用し、このアルコールにモジュール膜面を浸漬せる時間
を60分とした以外は、実施例1は同様とした。この場
合、透過水量は初期透過水量の95%にまで回復してい
た。Example 2 The same procedure as in Example 1 was performed except that ethanol having a concentration of 50% was adjusted to P = 10 with hydrazine as alcohol, and the time for immersing the module membrane surface in this alcohol was set to 60 minutes. Example 1 was the same. In this case, the permeated water amount had recovered to 95% of the initial permeated water amount.
比較例 実施例1に対し、アルコールによる浸漬処理を省略
し、ホルマリンを排出後、直に、膜面を純水によって10
分間水洗した以外は実施例1と同様とした。この水洗後
の透過水量は初期透過水量の62%にすぎづ、ホルマリン
の7日浸漬後の透過水量60%に対する改善は僅かであっ
た。Comparative Example Compared with Example 1, the immersion treatment with alcohol was omitted, and after discharging the formalin, the membrane surface was immediately washed with pure water.
The same procedure as in Example 1 was carried out except that the sample was washed with water for minutes. The amount of permeated water after this water washing was only 62% of the initial permeated water amount, and the improvement was little compared to the permeated water amount of 60% after immersion in formalin for 7 days.
上述した通り、本発明に係る膜モジュールの処理方法
によれば、膜モジュールの膜面がホルムアルデヒド水溶
液に継続的に接触される場合でも、アルカリ性る調整し
たアルコールによる膜面処理によって透過性能よく回復
でき、膜モジュールの運転機関中、ホルマリン浸漬によ
る菌の繁殖防止を良好に行い得る。As described above, according to the method for treating a membrane module according to the present invention, even when the membrane surface of the membrane module is continuously contacted with an aqueous formaldehyde solution, the membrane surface can be recovered with good permeability by treating the membrane with an alcohol adjusted to be alkaline. In addition, during the operation of the membrane module, the growth of bacteria by immersion in formalin can be effectively prevented.
Claims (1)
溶液に継続的に接触されたのち、アルカリ性に調整した
アルコールによってその膜面を処理したうえで、膜モジ
ュールを運転することを特徴とする膜モジュールの処理
方法。1. The membrane module according to claim 1, wherein, after the membrane surface of the membrane module is continuously contacted with an aqueous formaldehyde solution, the membrane surface is treated with an alcohol adjusted to be alkaline, and then the membrane module is operated. Processing method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32282488A JP2610669B2 (en) | 1988-12-20 | 1988-12-20 | Processing method of membrane module |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32282488A JP2610669B2 (en) | 1988-12-20 | 1988-12-20 | Processing method of membrane module |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02169016A JPH02169016A (en) | 1990-06-29 |
JP2610669B2 true JP2610669B2 (en) | 1997-05-14 |
Family
ID=18148018
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP32282488A Expired - Lifetime JP2610669B2 (en) | 1988-12-20 | 1988-12-20 | Processing method of membrane module |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2610669B2 (en) |
-
1988
- 1988-12-20 JP JP32282488A patent/JP2610669B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH02169016A (en) | 1990-06-29 |
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