JPH08126824A - Washing of filter membrane - Google Patents

Washing of filter membrane

Info

Publication number
JPH08126824A
JPH08126824A JP28720494A JP28720494A JPH08126824A JP H08126824 A JPH08126824 A JP H08126824A JP 28720494 A JP28720494 A JP 28720494A JP 28720494 A JP28720494 A JP 28720494A JP H08126824 A JPH08126824 A JP H08126824A
Authority
JP
Japan
Prior art keywords
membrane
treatment
washing
cleaning
filtration
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.)
Pending
Application number
JP28720494A
Other languages
Japanese (ja)
Inventor
Osamu Futamura
修 二村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ebara Corp
Original Assignee
Ebara Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ebara Corp filed Critical Ebara Corp
Priority to JP28720494A priority Critical patent/JPH08126824A/en
Publication of JPH08126824A publication Critical patent/JPH08126824A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE: To provide a washing method by which a filter membrane having high treating capacity is used for a long time, by effectively washing the stained filter membrane. CONSTITUTION: When washing a stained filter membrane, after first foreign matter stuck on the membrane is washed off with water, the filter membrane is subjected to a washing treatment in which drying treatment and chemical treatment are combined. In this washing treatment, it is preferable that, first, the chemical treatment is carried out and next the drying treatment is performed. The filter membrane is preferably the one whose surface is hydrophilic.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ろ過膜の洗浄方法に係
り、特に有機性排水を活性汚泥処理した後、膜分離によ
り処理水を得る膜分離活性汚泥法に使用されるろ過膜の
洗浄方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for cleaning a filtration membrane, and more particularly, a method for cleaning a filtration membrane used in a membrane separation activated sludge method in which organic waste water is treated with activated sludge and then treated water is obtained by membrane separation. Regarding the method.

【0002】[0002]

【従来の技術】膜分離プロセスはこれまでは高度処理を
中心とした分野で使用されてきたが、最近は活性汚泥法
の沈殿槽の代替などの二次処理の分野で使用されること
が多くなってきた。利用分野の拡大に伴い膜分離の原液
はより汚染されたものを対象とするようになってきてい
る。また、膜分離に必要な動力を低減する目的で膜本体
をろ過原液に直接浸漬してろ過を行う方法が行われてい
る。膜分離工程は通常クロスフローろ過と呼ばれる方式
で運転されており、膜表面流速を十分に確保することに
より膜表面を常に洗浄しながらろ過を行っている。しか
し、この状態でも膜内部に膜を通過しない微小固形物、
コロイド物質、等が閉塞することによりろ過能力が低下
する。膜内部の汚染物を除去してろ過能力を回復するた
めに薬液洗浄が行われており、薬液として界面活性剤、
次亜塩素酸ソーダ、水酸化ナトリウム、二酸化塩素、エ
チレンジアミン四酢酸塩のナトリウム塩、塩酸、クエン
酸等の溶液が使用されている。しかし、対象とするろ過
原液の汚染度が増加するにつれて、ろ過膜の汚染度も増
加するため、薬液洗浄による回復率が低下して、ろ過膜
の洗浄頻度が増加するとともに、ろ過膜の寿命が短くな
っている。
2. Description of the Related Art Membrane separation processes have hitherto been used in the field of high-level treatment, but recently they are often used in the field of secondary treatment such as substitution of a settling tank in the activated sludge method. It's coming. With the expansion of the field of use, the stock solution for membrane separation is becoming more contaminated. Further, in order to reduce the power required for membrane separation, a method of directly immersing the membrane main body in a filtration stock solution and performing filtration has been performed. The membrane separation step is usually operated by a method called cross-flow filtration, and filtration is performed while always cleaning the membrane surface by ensuring a sufficient membrane surface flow velocity. However, even in this state, minute solids that do not pass through the membrane inside the membrane,
The clogging of the colloidal substance, etc. reduces the filtration capacity. Chemical cleaning is performed to remove the contaminants inside the membrane and restore the filtration capacity.
Solutions of sodium hypochlorite, sodium hydroxide, chlorine dioxide, sodium salts of ethylenediaminetetraacetate, hydrochloric acid, citric acid, etc. are used. However, as the degree of contamination of the target undiluted solution increases, the degree of contamination of the filtration membrane also increases, so the recovery rate due to chemical cleaning decreases, the frequency of cleaning the filtration membrane increases, and the life of the filtration membrane increases. It's getting shorter.

【0003】[0003]

【発明が解決しようとする課題】本発明は、上記従来技
術に鑑みてなされたもので、汚染されたろ過膜を効果的
に洗浄することにより、ろ過膜を長期間使用することが
できる洗浄方法を提供することを課題とする。
DISCLOSURE OF THE INVENTION The present invention has been made in view of the above-mentioned prior art, and it is a method for cleaning a filter membrane which can be used for a long period of time by effectively cleaning the contaminated filter membrane. The challenge is to provide.

【0004】[0004]

【課題を解決するための手段】上記課題を解決するため
に、本発明では、汚染されたろ過膜を洗浄するに際し
て、まず、膜に付着した異物を水により洗い落とした
後、ろ過膜を乾燥処理と薬液処理とを組み合わせて洗浄
処理することを特徴とするろ過膜洗浄方法としたもので
ある。前記のろ過膜洗浄方法において、薬液処理と乾燥
処理の組み合わせは任意であり、乾燥処理の終了後薬液
処理を行ってもよいが、薬液処理終了後最終工程として
乾燥処理を行うのが、洗浄後の膜を保存する上で有利と
なる。上記のように、本発明では、汚染が進行して洗浄
が必要になった膜は、その表面に付着した汚泥・ゴミ等
の異物を水により洗い落とした後、薬液洗浄処理と乾燥
処理を行う。
In order to solve the above-mentioned problems, in the present invention, when cleaning a contaminated filter membrane, first, foreign substances attached to the membrane are washed off with water, and then the filter membrane is dried. And a chemical solution treatment are combined to carry out a washing treatment. In the filtration membrane cleaning method, the combination of the chemical treatment and the drying treatment is optional, and the chemical treatment may be performed after the completion of the drying treatment, but the drying treatment is performed as the final step after the completion of the chemical treatment after the cleaning. It is advantageous for storing the membrane. As described above, according to the present invention, the membrane that has been required to be washed due to the progress of contamination is washed with water to remove foreign substances such as sludge and dust, and then subjected to chemical cleaning treatment and drying treatment.

【0005】乾燥処理の方法は大気中に放置して自然乾
燥を行う方法や、温度管理された乾燥器内で乾燥する方
法など、通常の乾燥方法を採用すればよい。乾燥方式の
違いは必要とする時間とエネルギーの違いにすぎない。
薬液洗浄処理は汚染した膜を薬液に浸漬することにより
行われる。使用される薬品は特に限定するものではない
が、薬品の安全性、後処理の容易さ、コスト等から考慮
すると、アルキルベンゼンスルホン酸塩、アルファスル
ホ脂肪酸塩等の界面活性剤を使用することが良い。当
然、従来使用されてきたアルカリ等の薬品も使用する事
ができる。また、薬液の温度を上げて高温で処理するこ
とは非常に有効である。本発明で使用される膜はポリエ
チレン、塩化ビニル、等公知の材料を使用した、精密ろ
過・限外ろ過性を有する膜であり、膜表面の親水化処理
が施されていることが望ましい。適用分野は特に限定さ
れるものではないが、有機性排水を活性汚泥処理した後
の活性汚泥の分離工程に使用された膜が本方法に適して
いる。
As a method for the drying treatment, an ordinary drying method such as a method of performing natural drying by leaving it in the air or a method of drying in a temperature-controlled dryer may be adopted. The difference in drying method is only the difference in time and energy required.
The chemical cleaning process is performed by immersing the contaminated film in the chemical. The chemicals used are not particularly limited, but considering the safety of the chemicals, the ease of post-treatment, the cost, etc., it is preferable to use a surfactant such as an alkylbenzene sulfonate or an alpha sulfo fatty acid salt. . Of course, conventionally used chemicals such as alkali can also be used. In addition, it is very effective to raise the temperature of the chemical liquid and treat it at a high temperature. The membrane used in the present invention is a membrane using a known material such as polyethylene or vinyl chloride and having microfiltration / ultrafiltration properties, and it is desirable that the surface of the membrane be hydrophilized. The application field is not particularly limited, but the membrane used in the step of separating activated sludge after treating organic wastewater with activated sludge is suitable for the present method.

【0006】[0006]

【作用】本発明は従来行われてきた薬品洗浄に、乾燥工
程を組み合わせることにより、ろ過膜を洗浄することを
特徴とするろ過膜洗浄方法である。乾燥工程を組み込む
ことにより、低濃度で人体に安全な薬品による洗浄で効
果的に膜のろ過性能を回復することが可能になる。乾燥
工程によるろ過膜の洗浄原理の解明は今後の研究に期待
するが、付着した汚染物が乾燥により収縮剥離すること
により、その洗浄効果が上がるものと推定する。
The present invention is a method for cleaning a filtration membrane, characterized in that the filtration membrane is washed by combining a conventional chemical washing with a drying step. By incorporating a drying process, it becomes possible to effectively recover the filtration performance of the membrane by washing with a chemical that is low in concentration and safe for the human body. Although future research is expected to elucidate the principle of cleaning the filtration membrane by the drying process, it is presumed that the cleaning effect will be improved by contracting and peeling the adhered contaminants by drying.

【0007】[0007]

【実施例】以下、本発明を実施例により具体的に説明す
るが、本発明はこれらに限定されるものではない。 実施例1 本発明による乾燥処理を組み込んだ洗浄と、比較例とし
て従来の薬液洗浄のみの洗浄による試験を行った。ろ過
膜は、ポリエチレン製の中空糸膜で膜表面を親水性に加
工したものを使用した。同中空糸膜を下水の活性汚泥処
理曝気槽に浸漬設置し、吸引により膜内を負圧にするこ
とによって、処理水を取り出した。活性汚泥の分離工程
に使用した膜は、約1年間使用した膜である。乾燥処理
は自然乾燥で、6時間放置後、アルキルベンゼンスルホ
ン酸ナトリウムを主体とした洗剤(商品名「アタッ
ク」)で薬液処理した。その結果を表1に示す。
EXAMPLES The present invention will now be specifically described with reference to examples, but the present invention is not limited thereto. Example 1 A test was carried out by cleaning including the drying treatment according to the present invention and, as a comparative example, cleaning using only conventional chemical cleaning. As the filtration membrane, a polyethylene hollow fiber membrane whose surface was processed to be hydrophilic was used. The hollow fiber membrane was immersed in a sewage activated sludge treatment aeration tank, and a negative pressure was applied to the inside of the membrane by suction to take out the treated water. The membrane used in the activated sludge separation process is the membrane used for about one year. The drying treatment was natural drying, and after standing for 6 hours, chemical treatment was performed with a detergent mainly containing sodium alkylbenzenesulfonate (trade name "Attack"). Table 1 shows the results.

【0008】[0008]

【表1】 表1において、ろ過圧力の回復率は、下記式から計算し
た。 回復率=(汚染膜のろ過圧力−洗浄後のろ過圧力)/
(汚染膜のろ過圧力−新膜のろ過圧力) 従来法では回復率が60%であったが、本発明によると
回復率は83%になった。本発明により従来のアルカリ
や酸、塩素等に比べてより安全な薬品を使用して、汚染
した膜を効果的に洗浄することができた。
[Table 1] In Table 1, the recovery rate of filtration pressure was calculated from the following formula. Recovery rate = (filtration pressure of contaminated membrane-filtration pressure after washing) /
(Filtration pressure of contaminated membrane-Filtration pressure of new membrane) The recovery rate was 60% in the conventional method, but according to the present invention, the recovery rate was 83%. According to the present invention, it is possible to effectively clean a contaminated film by using a safer chemical than conventional alkalis, acids, chlorine and the like.

【0009】実施例2 下水を対象にした膜分離活性汚泥法に使用した中空糸膜
の繰り返し洗浄試験を行った。洗浄操作は汚染した膜を
水洗浄により付着物を除去した後、界面活性剤0.1%
水溶液で2時間浸漬洗浄、2日間自然乾燥で行った。洗
浄と連続ろ過を繰り返したときのろ過圧力の変化を図1
に示す。本発明による洗浄を繰り返し行うことにより、
長期間安定してろ過を継続することができた。
Example 2 A repeated cleaning test was conducted on a hollow fiber membrane used in a membrane separation activated sludge method for sewage. The washing operation is to wash the contaminated membrane with water to remove the deposits, and then add 0.1% of surfactant.
It was immersed in an aqueous solution for 2 hours, washed, and naturally dried for 2 days. Fig. 1 shows the change in filtration pressure when washing and continuous filtration are repeated.
Shown in By repeating the washing according to the present invention,
The filtration could be continued stably for a long period of time.

【0010】[0010]

【発明の効果】本発明によるろ過膜の洗浄方法は、ろ過
膜の汚染を効果的に回復することができ、ろ過膜を長期
間使用することが可能になった。本発明により安全な薬
品を使用して効果的に洗浄することが可能になったた
め、ろ過膜の維持管理が容易に、かつ経済的に行うこと
ができる。
The method of cleaning a filtration membrane according to the present invention can effectively recover the contamination of the filtration membrane, and the filtration membrane can be used for a long period of time. According to the present invention, since safe chemicals can be used for effective cleaning, maintenance of the filtration membrane can be performed easily and economically.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明による繰り返し洗浄操作とろ過圧力の関
係を示すグラフ。
FIG. 1 is a graph showing the relationship between repeated washing operation and filtration pressure according to the present invention.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 汚染されたろ過膜を洗浄するに際して、
まず、膜に付着した異物を水により洗い落とした後、ろ
過膜を乾燥処理と薬液処理とを組み合わせて洗浄処理す
ることを特徴とするろ過膜洗浄方法。
1. When cleaning a contaminated filtration membrane,
First, a method for washing a filtration membrane, which comprises washing away foreign matter attached to the membrane with water, and then subjecting the filtration membrane to a washing treatment by combining a drying treatment and a chemical treatment.
【請求項2】 前記洗浄処理は、まず、薬液処理を行
い、次に乾燥処理を行うことを特徴とする請求項1記載
のろ過膜洗浄方法。
2. The filtration membrane cleaning method according to claim 1, wherein the cleaning treatment is performed by first performing a chemical treatment and then performing a drying treatment.
【請求項3】 ろ過膜は、表面が親水性であることを特
徴とする請求項1又は2記載のろ過膜洗浄方法。
3. The method of cleaning a filtration membrane according to claim 1, wherein the surface of the filtration membrane is hydrophilic.
【請求項4】 汚染されたろ過膜は、活性汚泥混合液を
ろ過したものであることを特徴とする請求項1、2又は
3記載のろ過膜洗浄方法。
4. The method for cleaning a filtration membrane according to claim 1, 2 or 3, wherein the contaminated filtration membrane is obtained by filtering an activated sludge mixed solution.
JP28720494A 1994-10-28 1994-10-28 Washing of filter membrane Pending JPH08126824A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28720494A JPH08126824A (en) 1994-10-28 1994-10-28 Washing of filter membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28720494A JPH08126824A (en) 1994-10-28 1994-10-28 Washing of filter membrane

Publications (1)

Publication Number Publication Date
JPH08126824A true JPH08126824A (en) 1996-05-21

Family

ID=17714414

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28720494A Pending JPH08126824A (en) 1994-10-28 1994-10-28 Washing of filter membrane

Country Status (1)

Country Link
JP (1) JPH08126824A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019171956A1 (en) * 2018-03-05 2019-09-12 栗田工業株式会社 Method for cleaning membrane separation apparatus

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019171956A1 (en) * 2018-03-05 2019-09-12 栗田工業株式会社 Method for cleaning membrane separation apparatus
JP2019150789A (en) * 2018-03-05 2019-09-12 栗田工業株式会社 Washing method of membrane separator
CN111565825A (en) * 2018-03-05 2020-08-21 栗田工业株式会社 Method for cleaning membrane separation device
CN111565825B (en) * 2018-03-05 2021-09-10 栗田工业株式会社 Method for cleaning membrane separation device

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