JP2009006213A - Cleaning method of membrane filtration device - Google Patents

Cleaning method of membrane filtration device Download PDF

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JP2009006213A
JP2009006213A JP2007167897A JP2007167897A JP2009006213A JP 2009006213 A JP2009006213 A JP 2009006213A JP 2007167897 A JP2007167897 A JP 2007167897A JP 2007167897 A JP2007167897 A JP 2007167897A JP 2009006213 A JP2009006213 A JP 2009006213A
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membrane
treated water
raw water
water chamber
cleaning
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Masahiro Saito
政宏 斉藤
Hiroshi Sato
大士 佐藤
Toshisuke Yamazaki
俊祐 山崎
Toshio Sano
利夫 佐野
Kenichi Saito
憲一 齋藤
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Mitsui Engineering and Shipbuilding Co Ltd
Yuasa Membrane Systems Co Ltd
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Mitsui Engineering and Shipbuilding Co Ltd
Yuasa Membrane Systems Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a cleaning method of a membrane filtration device which enables the prevention of a discharge of a chemical cleaning liquid for cleaning a membrane to the outside through treatment water. <P>SOLUTION: A membrane filtration method comprises the step of sending raw water from one side of the membrane provided in the filtration device, and of filtering with the membrane to obtain the treat water from the other side of the membrane. In the method, when the membrane is cleaned, the chemical cleaning liquid is supplied from one side of the membrane, and the chemical cleaning liquid is not to pass through the other side of the membrane, or is to be prevented from the discharge to the outside by mixing in the treat water even if the chemical cleaning liquid passes through. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、膜濾過装置の洗浄方法に関し、詳しくは、膜洗浄用の薬品洗浄液が処理水を介して外部に排出されることを防止できる膜濾過装置の洗浄方法に関する。   The present invention relates to a cleaning method for a membrane filtration device, and more particularly to a cleaning method for a membrane filtration device that can prevent a chemical cleaning solution for membrane cleaning from being discharged to the outside through treated water.

原油等を輸送する貨物用船舶には、航行時の船体の安定性を保つためにバラストタンクが設けられている。通常、原油等が積載されていないときには、バラストタンク内をバラスト水で満たし、原油等を積み込む際にバラスト水を排出することにより、船体の浮力を調整し、船体を安定化させている。このようにバラスト水は、船舶の安全な航行のために必要な水であり、通常、荷役を行う港湾の海水が利用される。その量は、世界的にみると年間100億トンを超えるといわれている。   A cargo ship that transports crude oil or the like is provided with a ballast tank in order to maintain the stability of the hull during navigation. Usually, when crude oil or the like is not loaded, the inside of the ballast tank is filled with ballast water, and when the crude oil or the like is loaded, the ballast water is discharged to adjust the buoyancy of the hull and stabilize the hull. As described above, the ballast water is water necessary for the safe navigation of the ship, and the seawater of the port that performs cargo handling is usually used. The amount is said to exceed 10 billion tons per year worldwide.

ところで、バラスト水中には、それを取水した港湾に生息する微生物や小型・大型生物の卵が混入しており、船舶の移動に伴い、これら微生物や小型・大型生物の卵が同時に異国に運ばれることになる。従って、もともとその海域には生息していなかった生物種が、既存生物種に取って代わるといった生態系の破壊が深刻化している。   By the way, the ballast water contains microorganisms and eggs of small and large organisms that inhabit the port where the water was taken. It will be. Therefore, the destruction of ecosystems, such as the replacement of existing species with species that did not originally live in the sea, has become serious.

このような背景の中、国際海事機関(IMO)の外交会議において、バラスト水処理装置等に係る定期的検査の受検義務が採択され、2009年以降の建造船から適用される。
また船舶のバラスト水及び沈殿物の規制及び管理のための条約(以下、条約という)のD−2規則に規定する排出基準(G8)は、大きさ10〜50μmのプランクトンは10個/ml;大きさ50μm以上のプランクトンは10個/m;大きさ0.5〜3μmの大腸菌は250cfu/100ml;大きさ0.5〜3μmのコレラ菌は1cfu/100ml;大きさ0.5〜3μmの腸球菌は100cfu/100mlとなる。
Against this backdrop, the diplomatic meeting of the International Maritime Organization (IMO) adopted the obligation to take periodic inspections related to ballast water treatment equipment, etc., and is applied to construction ships from 2009 onwards.
The emission standard (G8) stipulated in the D-2 regulation of the Convention for the Control and Management of Ship Ballast Water and Sediment (hereinafter referred to as the Convention) is 10 / ml for plankton with a size of 10-50 μm; Plankton with a size of 50 μm or more is 10 cells / m 3 ; Escherichia coli with a size of 0.5-3 μm is 250 cfu / 100 ml; Vibrio cholerae with a size of 0.5-3 μm is 1 cfu / 100 ml; 0.5-3 μm in size Enterococci are 100 cfu / 100 ml.

更に2005年7月22日に採択された活性物質を利用するバラスト水管理システム承認手順(G9)では、その目的について、船舶の安全、人の健康及び水環境に関して、活性物質及び一つ以上の活性物質を含む製剤の承認可能性及びバラスト水管理システムでの適用を決定するものとしている。そして、このG9では、活性物質とは有害水生生物及び病原体に対し、一般的又は特定の作用をもつウイルス又は菌類を含む物質又は生物をいう、と定義し、検証として毒性試験を義務付けようとしている。   In addition, the Ballast Water Management System Approval Procedure (G9), adopted on 22 July 2005, which uses active substances, for that purpose, with regard to ship safety, human health and water environment, the active substances and one or more The applicability of the formulation containing the active substance and its application in the ballast water management system are to be determined. And in this G9, active substances are defined as substances or organisms containing viruses or fungi that have general or specific action against harmful aquatic organisms and pathogens, and we are going to require toxicity tests as verification .

以上のような背景から、G8やG9の要請を満足するには、非常に厳しい殺菌あるいは除菌が必要となっている。   From the above background, very strict sterilization or sterilization is required to satisfy the requirements of G8 and G9.

従来、バラスト水の殺菌・除菌技術としては、オゾンを用いた化学的手法として、特許文献1に記載の技術が知られている。   Conventionally, as a sterilization / sterilization technique for ballast water, a technique described in Patent Document 1 is known as a chemical technique using ozone.

特許文献1は、バラスト水に蒸気の注入と併用してオゾンを注入し、しかもオゾンを微細気泡化しヒドロキシラジカルの生成を促進してオゾンの使用量を削減しつつ殺菌する技術を提案している。   Patent Document 1 proposes a technique for injecting ozone into ballast water in combination with steam injection, and further sterilizing ozone while reducing the amount of ozone used by promoting the generation of hydroxy radicals by microbubbles. .

しかし、オゾンの使用量の削減にも限界があり、このため膜処理を採用する研究が急速に進んでいる。   However, there is a limit to reducing the amount of ozone used, and research for adopting membrane treatment is progressing rapidly.

バラスト水(海水)には、生物に由来するゲル状物質が多く存在し、また、膜を目詰まりさせやすい物質が存在しているので、膜モジュールを用いてバラスト水を膜処理する場合、長期運転を実現するために膜洗浄が重要となる。   In ballast water (seawater), there are many gel-like substances derived from living organisms, and substances that can easily clog membranes. Membrane cleaning is important to realize operation.

特許文献2には、膜洗浄において酵素を用いる技術や酵素と酸化剤の併用技術が開示されている。特許文献3には、膜洗浄においてエチレンジアミン四酢酸四ナトリウム四水和物を用いる技術が開示されている。また、膜処理を行わない方法として、特許文献4にはヨウ素で処理する方法、特許文献5では次亜塩素酸ナトリウムで処理する方法が開示されている。
特開2004−160437号公報 特開平3−133947号公報 特開平11−319518号公報 特表2002−504851号公報 特開平4−322788号公報
Patent Document 2 discloses a technique for using an enzyme in membrane cleaning and a technique for using an enzyme and an oxidizing agent in combination. Patent Document 3 discloses a technique using ethylenediaminetetraacetic acid tetrasodium tetrahydrate in membrane cleaning. Moreover, as a method of not performing the membrane treatment, Patent Document 4 discloses a method of treating with iodine, and Patent Document 5 discloses a method of treating with sodium hypochlorite.
JP 2004-160437 A Japanese Patent Laid-Open No. 3-133947 JP 11-319518 A Japanese translation of PCT publication No. 2002-504851 JP-A-4-322788

しかし、特許文献2〜特許文献5に記載の技術では、化学薬品が処理水側に移行した場合には、洗浄が終わった後に、再度原水を膜処理した際に、処理水側に残留している化学薬品が処理水を介して外部に排出されるおそれがある。化学薬品が海洋に排出されると生態系に影響を与えるおそれがある問題がある。   However, in the techniques described in Patent Documents 2 to 5, when the chemical moves to the treated water side, after the cleaning is finished, when the raw water is subjected to membrane treatment again, it remains on the treated water side. There is a risk that existing chemicals will be discharged to the outside through the treated water. There are problems that can affect the ecosystem when chemicals are released into the ocean.

そこで、本発明は、膜洗浄用の薬品洗浄液が処理水を介して外部に排出されることを防止することのできる膜濾過装置の洗浄方法を提供することを課題とする。   Then, this invention makes it a subject to provide the washing | cleaning method of the membrane filtration apparatus which can prevent the chemical | medical cleaning liquid for membrane washing | cleaning being discharged | emitted outside via treated water.

また、本発明の他の課題は、以下の記載により明らかになる。   Other problems of the present invention will become apparent from the following description.

上記課題は、以下の各発明によって解決される。   The above problems are solved by the following inventions.

(請求項1)
濾過装置内に設けられた膜の一側から原水を送り、該膜で濾過して該膜の他側から処理水を得る膜濾過方法において、
該膜の洗浄に際し、前記膜の一側から薬品洗浄液を供給し、該薬品洗浄液が該膜の他側に通過しないか、あるいは通過しても処理水中に混入して外部に排出させないことを特徴とする膜の洗浄方法。
(Claim 1)
In the membrane filtration method of sending raw water from one side of the membrane provided in the filtration device and filtering the membrane to obtain treated water from the other side of the membrane,
When cleaning the membrane, a chemical cleaning solution is supplied from one side of the membrane, and the chemical cleaning solution does not pass to the other side of the membrane, or even if it passes, it is not mixed into the treated water and discharged outside. A method for cleaning the film.

(請求項2)
前記濾過装置が、濾過槽内を仕切板により処理水室と原水室に区画し、該原水室内に、上部開口を有する多孔製の筒状支持体と該支持体の外周を被覆する袋状の膜とからなる多数の濾過筒を設置し、前記原水室に入った原水が該原水室内を上向流しながら、前記膜により濾過され処理水となって濾過筒内を上昇して前記処理水室内に集水される構造であり、且つ前記原水室に原水を供給する原水供給管及び前記処理水室に処理水を取り出す処理水排出管が接続され、該処理水排出管に開閉弁を備えていることを特徴とする請求項1記載の膜濾過装置の洗浄方法。
(Claim 2)
The filtration device divides the inside of the filtration tank into a treated water chamber and a raw water chamber by a partition plate, and in the raw water chamber, a porous cylindrical support body having an upper opening and a bag-like shape covering the outer periphery of the support body A large number of filter cylinders comprising a membrane are installed, and the raw water entering the raw water chamber flows upward in the raw water chamber, and is filtered by the membrane to be treated water and rises in the filter cylinder, thereby the treated water chamber A raw water supply pipe for supplying raw water to the raw water chamber and a treated water discharge pipe for extracting treated water to the treated water chamber, and an open / close valve is provided on the treated water discharge pipe. The method for cleaning a membrane filtration device according to claim 1.

(請求項3)
前記薬品洗浄液を膜の他側に通過しないようにする方法が、前記原水室内に供給される薬品洗浄液の圧力と、前記処理水室内の圧力を調整することを特徴とする請求項2記載の膜濾過装置の洗浄方法。
(Claim 3)
3. The membrane according to claim 2, wherein the method of preventing the chemical cleaning solution from passing through the other side of the membrane adjusts the pressure of the chemical cleaning solution supplied to the raw water chamber and the pressure of the treatment water chamber. Cleaning method for filtration device.

(請求項4)
前記濾過筒の高さをHとし、前記処理水室内の圧力をPとしたときに、1.2H≦P≦2Hの関係が成り立つように、前記原水室内に供給される薬品洗浄液の圧力と、前記処理水室内の圧力を調整することを特徴とする請求項3記載の膜濾過装置の洗浄方法。
(Claim 4)
When the height of the filter cylinder is H and the pressure in the treated water chamber is P, the pressure of the chemical cleaning liquid supplied into the raw water chamber so that the relationship of 1.2H ≦ P ≦ 2H is established, 4. The method for cleaning a membrane filtration device according to claim 3, wherein the pressure in the treated water chamber is adjusted.

(請求項5)
前記薬品洗浄液が該膜の他側から通過しても処理水中に混入して外部に排出させないようにする方法が、前記処理水排出管に設けられた開閉弁を閉じ、次に該処理水排出管内の薬品洗浄液を原水側に追い出すことを特徴とする請求項2記載の膜濾過装置の洗浄方法。
(Claim 5)
Even if the chemical cleaning liquid passes from the other side of the membrane, a method for preventing the chemical cleaning liquid from entering the treated water and discharging it to the outside closes the on-off valve provided in the treated water discharge pipe, and then discharges the treated water. 3. The method for cleaning a membrane filtration device according to claim 2, wherein the chemical cleaning liquid in the pipe is expelled to the raw water side.

(請求項6)
前記処理水排出管内の薬品洗浄液を原水側に追い出す際に、該処理水排出管に前記処理水を供給することを特徴とする請求項5記載の膜濾過装置の洗浄方法。
(Claim 6)
6. The membrane filtration apparatus cleaning method according to claim 5, wherein when the chemical cleaning liquid in the treated water discharge pipe is driven to the raw water side, the treated water is supplied to the treated water discharge pipe.

(請求項7)
前記原水が、バラスト水であり、前記処理水がバラスト処理水であることを特徴とする請求項1〜6の何れかに記載の膜濾過装置の洗浄方法。
(Claim 7)
The method for cleaning a membrane filtration device according to any one of claims 1 to 6, wherein the raw water is ballast water, and the treated water is ballast treated water.

本発明によれば、膜洗浄用の薬品洗浄液が処理水を介して外部に排出されることを防止することのできる膜濾過装置の洗浄方法を提供することができる。   ADVANTAGE OF THE INVENTION According to this invention, the washing | cleaning method of the membrane filtration apparatus which can prevent that the chemical | medical cleaning liquid for membrane washing | cleaning is discharged | emitted outside via treated water can be provided.

以下、本発明の実施の形態について図面に基づいて説明する。   Hereinafter, embodiments of the present invention will be described with reference to the drawings.

図1は本発明の方法を実施可能な膜濾過装置の一例を示す概略断面図である。   FIG. 1 is a schematic cross-sectional view showing an example of a membrane filtration apparatus capable of performing the method of the present invention.

図中、1は濾過槽であり、円筒竪型に形成されることが好ましく、該濾過槽1は仕切板2により、原水が供給される原水室101と膜処理された後の処理水が集水される処理水室102とに区画されている。   In the figure, reference numeral 1 denotes a filtration tank, which is preferably formed in a cylindrical bowl shape. The filtration tank 1 collects raw water chamber 101 to which raw water is supplied and treated water after being membrane-treated by a partition plate 2. It is divided into a treated water chamber 102 to be watered.

原水室101には原水供給口103が設けられ、処理水室102には処理水排出口104が設けられている。   The raw water chamber 101 is provided with a raw water supply port 103, and the treated water chamber 102 is provided with a treated water discharge port 104.

原水供給口103には原水供給管105が接続されている。105Aは原水供給管105に設けられた開閉弁である。   A raw water supply pipe 105 is connected to the raw water supply port 103. Reference numeral 105 </ b> A is an on-off valve provided in the raw water supply pipe 105.

原水は、例えば、バラスト水(海水や淡水)などが挙げられる。バラスト水として海水を原水とする場合に、濾過対象となる物質としては、動物性プランクトン、植物性プランクトン、微生物、Si、Al、Feなどの元素又はその酸化物や塩化物など無機物、その他、懸濁物質(SS)、ゲル状物質などがある。   Examples of the raw water include ballast water (seawater and fresh water). When seawater is used as the ballast water, the substances to be filtered include zooplankton, phytoplankton, microorganisms, elements such as Si, Al and Fe, inorganic substances such as oxides and chlorides, and other matters. There are suspended substances (SS), gel-like substances and the like.

処理水排出口104には処理水排出管106が接続され、該処理水排出管106には開閉弁106Aが設けられている。   A treated water discharge pipe 106 is connected to the treated water discharge port 104, and the treated water discharge pipe 106 is provided with an on-off valve 106A.

また、処理水排出管106には、処理水排出口104を通して処理水室102内に空気を供給し、該処理水室102内を加圧するための空気供給管107の一端が接続され、該空気供給管107には開閉弁107Aが設けられている。空気供給管107の他端は空気供給源3に接続されている。空気供給源3には例えばコンプレッサーを用いることができる。   The treated water discharge pipe 106 is connected to one end of an air supply pipe 107 for supplying air into the treated water chamber 102 through the treated water discharge port 104 and pressurizing the treated water chamber 102. The supply pipe 107 is provided with an on-off valve 107A. The other end of the air supply pipe 107 is connected to the air supply source 3. For example, a compressor can be used as the air supply source 3.

ここでは、空気供給管107の一端は、処理水排出管106における開閉弁106Aと処理水排出口104との間に接続されているが、処理水室102内を加圧可能であれば、濾過槽1の処理水室102に直接接続するようにしてもよい。   Here, one end of the air supply pipe 107 is connected between the on-off valve 106A and the treated water discharge port 104 in the treated water discharge pipe 106. If the inside of the treated water chamber 102 can be pressurized, filtration is performed. You may make it connect directly to the treated water chamber 102 of the tank 1. FIG.

原水室101の底部には洗浄排水排出口108が設けられている。洗浄排水排出口108には洗浄排水排出管109が接続され、該洗浄排水排出管109には開閉弁109Aが設けられている。   A cleaning drainage outlet 108 is provided at the bottom of the raw water chamber 101. A cleaning drainage discharge pipe 109 is connected to the cleaning drainage discharge port 108, and an opening / closing valve 109 </ b> A is provided in the cleaning drainage discharge pipe 109.

洗浄排水排出管109には、洗浄排水排出口108と開閉弁109Aとの間から、原水室101内に薬品洗浄設備から供給される薬品洗浄液を注入するための薬品洗浄液注入管110が接続されている。薬品洗浄液注入管110には開閉弁110Aが設けられている。   A chemical cleaning liquid injection pipe 110 for injecting a chemical cleaning liquid supplied from a chemical cleaning facility into the raw water chamber 101 is connected to the cleaning drainage discharge pipe 109 from between the cleaning drainage outlet 108 and the on-off valve 109A. Yes. The chemical cleaning liquid injection pipe 110 is provided with an on-off valve 110A.

4は仕切板2に例えば吊り下げられた濾過筒であり、該濾過筒4は多孔製の円筒形の支持体400と該支持体400の外周に被覆され袋状に形成された濾過膜401によって構成され、濾過筒4の上部は処理水室102に処理水を送液可能なように、該処理水室102側に向けて開口する上部開口402を有している。   Reference numeral 4 denotes a filter cylinder suspended, for example, on the partition plate 2, and the filter cylinder 4 is formed by a porous cylindrical support body 400 and a filter membrane 401 formed on the outer periphery of the support body 400 and formed in a bag shape. The upper part of the filtration cylinder 4 has an upper opening 402 that opens toward the treated water chamber 102 so that treated water can be fed to the treated water chamber 102.

支持体400は上部開口402を有する樹脂製円筒形であり、例えばポリエチレン製のものを用いることができる。   The support 400 has a cylindrical shape made of a resin having an upper opening 402. For example, a support made of polyethylene can be used.

支持体400の表面は網目状に形成されてもよいし、あるいは多孔状に形成されてもよい。支持体400表面の開口率は40%〜70%の範囲が好ましく、45%〜65%の範囲がより好ましく、50%〜65%の範囲が更に好ましい。   The surface of the support 400 may be formed in a mesh shape or may be formed in a porous shape. The opening ratio on the surface of the support 400 is preferably in the range of 40% to 70%, more preferably in the range of 45% to 65%, and still more preferably in the range of 50% to 65%.

濾過膜401は、精密濾過膜や限外濾過膜などを用いることができるが、好ましいのは精密濾過膜である。本発明において使用できる精密濾過膜は市販品として入手でき、例えば、ユアサメンブレンシステム製「MF膜」などを使用できる。   A microfiltration membrane, an ultrafiltration membrane, or the like can be used as the filtration membrane 401, but a microfiltration membrane is preferable. The microfiltration membrane that can be used in the present invention can be obtained as a commercial product. For example, “MF membrane” manufactured by Yuasa Membrane System can be used.

本態様では、原水室101内に、複数本の濾過筒4、4、…が吊り下げ状に配設されているが、その本数は必ずしも限定されない。   In this embodiment, a plurality of filter tubes 4, 4,... Are arranged in a suspended shape in the raw water chamber 101, but the number is not necessarily limited.

かかる膜濾過装置において、原水の処理時、原水は、原水供給管105から原水供給口103を経由して原水室101に導入され、原水室101内を上向流して、濾過膜401を通過することによって濾過される。濾過膜401によって濾過された処理水は、濾過筒4内を更に上方に向かって進み、上部開口402から処理水室102に集水され、処理水排出口104から処理水排出管106を経由して排出される。   In such a membrane filtration device, when raw water is treated, raw water is introduced from the raw water supply pipe 105 into the raw water chamber 101 via the raw water supply port 103, flows upward in the raw water chamber 101, and passes through the filtration membrane 401. Is filtered. The treated water filtered by the filtration membrane 401 proceeds further upward in the filter cylinder 4, is collected into the treated water chamber 102 from the upper opening 402, and passes through the treated water discharge pipe 106 from the treated water discharge port 104. Discharged.

このようにして濾過膜401による原水の処理を継続すると、次第に濾過膜401の目詰まりが生じる。特に原水としてバラスト水(海水)を使用する場合、水中には生物に由来するゲル状物質が多く存在し、また、膜を目詰まりさせやすい物質が存在しているので、長期運転を実現するためには、濾過膜401の表面を薬品洗浄する膜洗浄が必要となる。   When the raw water treatment by the filtration membrane 401 is continued in this manner, the filtration membrane 401 is gradually clogged. In particular, when ballast water (seawater) is used as raw water, there are many gel-like substances derived from living organisms in the water, and there are substances that can easily clog the membrane. For this, membrane cleaning for chemical cleaning of the surface of the filtration membrane 401 is required.

使用する薬品としては、次亜塩素酸、次亜塩素酸ソーダ、過酸化水素などが挙げられる。   Examples of chemicals used include hypochlorous acid, sodium hypochlorite, and hydrogen peroxide.

濾過膜401の薬品洗浄を行うには、原水供給管105の開閉弁105Aを閉じて原水の供給を停止させ、洗浄排水排出管109から濾過槽1内の原水及び処理水を排水した後、洗浄排水排出管109の開閉弁109Aを閉じ、薬品洗浄液注入管110の開閉弁110Aを開けて原水室101内に薬品洗浄設備から薬品洗浄液Cを所定の圧力で注入する(図2)。   In order to perform chemical cleaning of the filtration membrane 401, the on-off valve 105A of the raw water supply pipe 105 is closed to stop the supply of raw water, and the raw water and treated water in the filtration tank 1 are drained from the cleaning drain discharge pipe 109, and then washed. The on-off valve 109A of the drainage discharge pipe 109 is closed, the on-off valve 110A of the chemical cleaning liquid injection pipe 110 is opened, and the chemical cleaning liquid C is injected into the raw water chamber 101 from the chemical cleaning equipment at a predetermined pressure (FIG. 2).

原水室101内に満たされた薬品洗浄液Cは、濾過膜401の表面と接触し、該濾過膜401表面に付着するゲル状物質等の付着物質を洗浄する。   The chemical cleaning liquid C filled in the raw water chamber 101 comes into contact with the surface of the filtration membrane 401 and cleans attached substances such as a gel substance adhering to the surface of the filtration membrane 401.

このとき、薬品洗浄液Cは、原水室101内に所定の圧力で注入されるため、濾過膜401を通過して濾過筒4内に浸入しようとするが、このとき、空気供給管107の開閉弁107Aを開け、空気供給源3を稼動させて空気供給管107から処理水室102内に空気を供給することにより、該処理水室102内を加圧する。   At this time, since the chemical cleaning liquid C is injected into the raw water chamber 101 at a predetermined pressure, the chemical cleaning liquid C attempts to enter the filter cylinder 4 through the filter membrane 401. At this time, the open / close valve of the air supply pipe 107 is used. The inside of the treated water chamber 102 is pressurized by opening 107A and operating the air supply source 3 to supply air from the air supply pipe 107 into the treated water chamber 102.

この処理水室102内の加圧空気は、濾過筒4の上部開口402から濾過筒4内に至り、濾過膜401の内側(処理水室102側)の全面に均一に圧力をかける。このときの加圧力は、薬品洗浄液Cの注入圧との関係において適宜調整されるが、この加圧力を適切に設定することにより、薬品洗浄液Cが濾過膜401を通過して濾過筒4内に浸入することを阻止することができる。従って、薬品洗浄液Cは処理水室102内に浸入せず、薬品洗浄液Cが処理水排出口104から外部に排出されることを防止することができる。   The pressurized air in the treated water chamber 102 reaches the inside of the filter tube 4 from the upper opening 402 of the filter tube 4, and uniformly applies pressure to the entire inner surface of the filter membrane 401 (the treated water chamber 102 side). The applied pressure at this time is appropriately adjusted in relation to the injection pressure of the chemical cleaning liquid C. By appropriately setting the applied pressure, the chemical cleaning liquid C passes through the filter membrane 401 and enters the filter cylinder 4. Intrusion can be prevented. Therefore, the chemical cleaning liquid C does not enter the treated water chamber 102, and the chemical cleaning liquid C can be prevented from being discharged from the treated water discharge port 104 to the outside.

特に好ましくは、図2に示すように、濾過筒4の高さをHとし、処理水室102内の圧力をPとしたときに、1.2H≦P≦2Hの関係が成り立つように、原水室101内に供給される薬品洗浄液Cの圧力と、処理水室102内の圧力を調整することである。なお、図2において、原水供給口103と洗浄排水排出口108は図示省略している。   Particularly preferably, as shown in FIG. 2, when the height of the filter cylinder 4 is H and the pressure in the treated water chamber 102 is P, the raw water is set so that the relationship of 1.2H ≦ P ≦ 2H is established. The pressure of the chemical cleaning liquid C supplied into the chamber 101 and the pressure in the treated water chamber 102 are adjusted. In FIG. 2, the raw water supply port 103 and the cleaning wastewater discharge port 108 are not shown.

処理水室102内の圧力Pがこの範囲にあるときは、原水室101内の薬品洗浄液Cが濾過膜401の内部に入ることを阻止できるため、薬品洗浄液Cを濾過膜401の表面と効率良く接触させることができ、洗浄効果を高めることができる。   When the pressure P in the treated water chamber 102 is within this range, the chemical cleaning liquid C in the raw water chamber 101 can be prevented from entering the inside of the filtration membrane 401. The cleaning effect can be enhanced.

更に処理水室102内の圧力Pが濾過筒4の高さHより所定範囲だけ大きいので、処理水室102内の空気による気泡が膜を通して原水室101内に入り、膜表面を気泡が打撃できるので、膜洗浄効果もより向上する。   Further, since the pressure P in the treated water chamber 102 is larger than the height H of the filter cylinder 4 by a predetermined range, air bubbles in the treated water chamber 102 enter the raw water chamber 101 through the membrane, and the bubbles can hit the membrane surface. Therefore, the film cleaning effect is further improved.

薬品洗浄液Cによる濾過膜401の洗浄後は、洗浄排水排出管109の開閉弁109Aを開けることにより、洗浄排水排出管109から原水室101内の薬品洗浄液Cを排出し、薬品洗浄設備に戻す。   After cleaning the filter membrane 401 with the chemical cleaning liquid C, the on-off valve 109A of the cleaning drainage discharge pipe 109 is opened to discharge the chemical cleaning liquid C in the raw water chamber 101 from the cleaning drainage discharge pipe 109 and return to the chemical cleaning equipment.

図3は本発明の方法を実施可能な膜濾過装置の他の例を示す概略断面図である。図1と同一符号の部位は同一構成の部位を示しているので、これらの詳細な説明は省略する。   FIG. 3 is a schematic cross-sectional view showing another example of a membrane filtration apparatus capable of performing the method of the present invention. The parts denoted by the same reference numerals as those in FIG. 1 indicate the parts having the same configuration, and detailed description thereof will be omitted.

この膜濾過装置において、処理水排出管106には、処理水排出口104と開閉弁106Aとの間に、処理水排出管106の開閉弁106Aを閉じた状態で、処理水排出口104から処理水室102内に洗浄水を供給するための洗浄水供給管111が接続されている。洗浄水供給管111には開閉弁111Aが設けられている。   In this membrane filtration device, the treated water discharge pipe 106 is treated from the treated water discharge port 104 with the on-off valve 106A of the treated water discharge pipe 106 closed between the treated water discharge port 104 and the on-off valve 106A. A cleaning water supply pipe 111 for supplying cleaning water into the water chamber 102 is connected. The cleaning water supply pipe 111 is provided with an on-off valve 111A.

洗浄水供給管111は、ポンプ112によって洗浄水貯留タンク113内に貯留された洗浄水Wを濾過槽1の処理水室102内に供給可能としている。   The cleaning water supply pipe 111 can supply the cleaning water W stored in the cleaning water storage tank 113 by the pump 112 into the treated water chamber 102 of the filtration tank 1.

かかる膜濾過装置において濾過膜401の薬品洗浄を行う場合、原水供給管105の開閉弁105Aを閉じて原水の供給を停止させ、洗浄排水排出管109から濾過槽1内の原水及び処理水を排水した後、洗浄排水排出管109の開閉弁109Aを閉じ、薬品洗浄液注入管110の開閉弁110Aを開けて原水室101内に薬品洗浄設備から薬品洗浄液Cを所定の圧力で注入する(図4)。   When performing chemical cleaning of the filter membrane 401 in such a membrane filtration device, the on-off valve 105A of the raw water supply pipe 105 is closed to stop the supply of raw water, and the raw water and treated water in the filtration tank 1 are drained from the cleaning drainage discharge pipe 109. After that, the on-off valve 109A of the cleaning drainage discharge pipe 109 is closed, the on-off valve 110A of the chemical cleaning liquid injection pipe 110 is opened, and the chemical cleaning liquid C is injected into the raw water chamber 101 from the chemical cleaning equipment at a predetermined pressure (FIG. 4). .

原水室101内に注入された薬品洗浄液Cは、濾過膜401の表面と接触し、該濾過膜401表面に付着するゲル状物質等の付着物質を洗浄する。   The chemical cleaning liquid C injected into the raw water chamber 101 comes into contact with the surface of the filtration membrane 401 and cleans adhered substances such as a gel substance adhering to the surface of the filtration membrane 401.

この薬品洗浄液Cは、原水室101内に所定の圧力で注入されるため、濾過膜401を通過して濾過筒4内にも浸入し、処理水室102側に浸入することになる。   Since this chemical cleaning liquid C is injected into the raw water chamber 101 at a predetermined pressure, it passes through the filter membrane 401 and also enters the filter cylinder 4 and enters the treated water chamber 102 side.

薬品洗浄液Cによる濾過膜401の洗浄後は、洗浄排水排出管109の開閉弁109Aを開けることにより、洗浄排水排出管109から原水室101内の薬品洗浄液Cを排出し、薬品洗浄設備に戻す。   After cleaning the filter membrane 401 with the chemical cleaning liquid C, the on-off valve 109A of the cleaning drainage discharge pipe 109 is opened to discharge the chemical cleaning liquid C in the raw water chamber 101 from the cleaning drainage discharge pipe 109 and return to the chemical cleaning equipment.

このとき、処理水排出管106の開閉弁106Aを閉じた状態で、洗浄水供給管111の開閉弁111を開け、供給ポンプ112を稼動させて洗浄水貯留タンク113内の洗浄水Wを処理水排出管106を通って処理水室102内に供給することにより、濾過槽1内の薬品洗浄液Cを原水室101側に追い出す(図5)。   At this time, with the on-off valve 106A of the treated water discharge pipe 106 closed, the on-off valve 111 of the cleaning water supply pipe 111 is opened, the supply pump 112 is operated, and the cleaning water W in the cleaning water storage tank 113 is treated with the treated water. By supplying into the treated water chamber 102 through the discharge pipe 106, the chemical cleaning liquid C in the filtration tank 1 is driven to the raw water chamber 101 side (FIG. 5).

これにより、薬品洗浄液Cが濾過膜401を通過して濾過筒4内から処理水室102側に浸入しても、薬品洗浄液Cが処理水排出管106を通って濾過槽1の外部に排出されることを防止することができる。   Thereby, even if the chemical cleaning liquid C passes through the filter membrane 401 and enters the treated water chamber 102 from the inside of the filter cylinder 4, the chemical cleaning liquid C is discharged to the outside of the filtration tank 1 through the treated water discharge pipe 106. Can be prevented.

しかも、薬品洗浄液Cが処理水排出管106内に浸入しても、洗浄水Wを供給することによって洗浄され、処理水室102を通って原水室101側に追い出されるため、処理水排出管106を通って排出される処理水中に薬品洗浄液Cが混入するおそれはない。   Moreover, even if the chemical cleaning liquid C enters the treated water discharge pipe 106, it is cleaned by supplying the cleaning water W and is expelled to the raw water chamber 101 side through the treated water chamber 102. There is no possibility that the chemical cleaning liquid C is mixed into the treated water discharged through the water.

洗浄水貯留タンク113内に貯留される洗浄水Wには、バラスト処理水を使用することも好ましい。この場合、処理水排出管106の途中に分岐管を設け、処理水室102から処理水排出管106を通って外部に取り出された処理水の一部を、該分岐管から洗浄水貯留タンク113に供給するようにすればよい。なお、図4、5において、原水供給口103は図示省略している。   It is also preferable to use ballast treated water as the cleaning water W stored in the cleaning water storage tank 113. In this case, a branch pipe is provided in the middle of the treated water discharge pipe 106, and a part of the treated water taken out from the treated water chamber 102 through the treated water discharge pipe 106 to the outside is washed water storage tank 113. It is sufficient to supply to. 4 and 5, the raw water supply port 103 is not shown.

本発明の方法を実施可能な膜濾過装置の一例を示す概略断面図Schematic cross-sectional view showing an example of a membrane filtration apparatus capable of performing the method of the present invention 図1に示す膜濾過装置における膜洗浄方法を示す説明図Explanatory drawing which shows the membrane cleaning method in the membrane filtration apparatus shown in FIG. 本発明の方法を実施可能な膜濾過装置の他の例を示す概略断面図Schematic sectional view showing another example of a membrane filtration device capable of performing the method of the present invention 図3に示す膜濾過装置における膜洗浄方法を示す説明図Explanatory drawing which shows the membrane cleaning method in the membrane filtration apparatus shown in FIG. 図3に示す膜濾過装置における膜洗浄方法を示す説明図Explanatory drawing which shows the membrane cleaning method in the membrane filtration apparatus shown in FIG.

符号の説明Explanation of symbols

1:濾過槽
101:原水室
102:処理水室
103:原水供給口
104:処理水排出口
105:原水供給管
105A:開閉弁
106:処理水排出管
106A:開閉弁
107:空気供給管
107A:開閉弁
108:洗浄排水排出口
109:洗浄排水排出管
109A:開閉弁
110:薬品洗浄液注入管
110A:開閉弁
111:洗浄水供給管
111A:開閉弁
112:ポンプ
113:洗浄水貯留タンク
2:仕切板
3:空気供給源
4:濾過筒
400:支持体
401:濾過膜
402:上部開口
C:薬品洗浄液
W:洗浄水
1: Filtration tank 101: Raw water chamber 102: Treated water chamber 103: Raw water supply port 104: Treated water discharge port 105: Raw water supply pipe 105A: On-off valve 106: Treated water discharge pipe 106A: On-off valve 107: Air supply pipe 107A: On-off valve 108: Cleaning drain discharge port 109: Cleaning drain discharge pipe 109A: On-off valve 110: Chemical cleaning liquid injection pipe 110A: On-off valve 111: Wash water supply pipe 111A: On-off valve 112: Pump 113: Wash water storage tank 2: Partition Plate 3: Air supply source 4: Filter cylinder 400: Support body 401: Filtration membrane 402: Upper opening C: Chemical cleaning liquid W: Cleaning water

Claims (7)

濾過装置内に設けられた膜の一側から原水を送り、該膜で濾過して該膜の他側から処理水を得る膜濾過方法において、
該膜の洗浄に際し、前記膜の一側から薬品洗浄液を供給し、該薬品洗浄液が該膜の他側に通過しないか、あるいは通過しても処理水中に混入して外部に排出させないことを特徴とする膜の洗浄方法。
In the membrane filtration method of sending raw water from one side of the membrane provided in the filtration device and filtering the membrane to obtain treated water from the other side of the membrane,
When cleaning the membrane, a chemical cleaning solution is supplied from one side of the membrane, and the chemical cleaning solution does not pass to the other side of the membrane, or even if it passes, it is not mixed into the treated water and discharged outside. A method for cleaning the film.
前記濾過装置が、濾過槽内を仕切板により処理水室と原水室に区画し、該原水室内に、上部開口を有する多孔製の筒状支持体と該支持体の外周を被覆する袋状の膜とからなる多数の濾過筒を設置し、前記原水室に入った原水が該原水室内を上向流しながら、前記膜により濾過され処理水となって濾過筒内を上昇して前記処理水室内に集水される構造であり、且つ前記原水室に原水を供給する原水供給管及び前記処理水室に処理水を取り出す処理水排出管が接続され、該処理水排出管に開閉弁を備えていることを特徴とする請求項1記載の膜濾過装置の洗浄方法。   The filtration device divides the inside of the filtration tank into a treated water chamber and a raw water chamber by a partition plate, and in the raw water chamber, a porous cylindrical support body having an upper opening and a bag-like shape covering the outer periphery of the support body A large number of filter cylinders comprising a membrane are installed, and the raw water entering the raw water chamber flows upward in the raw water chamber, and is filtered by the membrane to be treated water and rises in the filter cylinder, thereby the treated water chamber A raw water supply pipe for supplying raw water to the raw water chamber and a treated water discharge pipe for extracting treated water to the treated water chamber, and an open / close valve is provided on the treated water discharge pipe. The method for cleaning a membrane filtration device according to claim 1. 前記薬品洗浄液を膜の他側に通過しないようにする方法が、前記原水室内に供給される薬品洗浄液の圧力と、前記処理水室内の圧力を調整することを特徴とする請求項2記載の膜濾過装置の洗浄方法。   3. The membrane according to claim 2, wherein the method of preventing the chemical cleaning solution from passing through the other side of the membrane adjusts the pressure of the chemical cleaning solution supplied to the raw water chamber and the pressure of the treatment water chamber. Cleaning method for filtration device. 前記濾過筒の高さをHとし、前記処理水室内の圧力をPとしたときに、1.2H≦P≦2Hの関係が成り立つように、前記原水室内に供給される薬品洗浄液の圧力と、前記処理水室内の圧力を調整することを特徴とする請求項3記載の膜濾過装置の洗浄方法。   When the height of the filter cylinder is H and the pressure in the treated water chamber is P, the pressure of the chemical cleaning liquid supplied into the raw water chamber so that the relationship of 1.2H ≦ P ≦ 2H is established, The method for cleaning a membrane filtration device according to claim 3, wherein the pressure in the treated water chamber is adjusted. 前記薬品洗浄液が該膜の他側から通過しても処理水中に混入して外部に排出させないようにする方法が、前記処理水排出管に設けられた開閉弁を閉じ、次に該処理水排出管内の薬品洗浄液を原水側に追い出すことを特徴とする請求項2記載の膜濾過装置の洗浄方法。   Even if the chemical cleaning liquid passes from the other side of the membrane, the method for preventing the chemical cleaning liquid from entering the treated water and discharging it to the outside closes the on-off valve provided in the treated water discharge pipe, and then discharges the treated water. 3. The method for cleaning a membrane filtration device according to claim 2, wherein the chemical cleaning liquid in the pipe is expelled to the raw water side. 前記処理水排出管内の薬品洗浄液を原水側に追い出す際に、該処理水排出管に前記処理水を供給することを特徴とする請求項5記載の膜濾過装置の洗浄方法。   6. The method for cleaning a membrane filtration device according to claim 5, wherein when the chemical cleaning liquid in the treated water discharge pipe is driven to the raw water side, the treated water is supplied to the treated water discharge pipe. 前記原水が、バラスト水であり、前記処理水がバラスト処理水であることを特徴とする請求項1〜6の何れかに記載の膜濾過装置の洗浄方法。   The method for cleaning a membrane filtration device according to claim 1, wherein the raw water is ballast water, and the treated water is ballast treated water.
JP2007167897A 2007-06-26 2007-06-26 Cleaning method of membrane filtration device Withdrawn JP2009006213A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009241040A (en) * 2008-03-31 2009-10-22 Mitsui Eng & Shipbuild Co Ltd Method and apparatus for regenerating membrane for manufacturing ballast water
WO2011071047A1 (en) * 2009-12-07 2011-06-16 三井造船株式会社 Method for cleaning membrane cartridge for ballast water treatment and method for cleaning filter

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009241040A (en) * 2008-03-31 2009-10-22 Mitsui Eng & Shipbuild Co Ltd Method and apparatus for regenerating membrane for manufacturing ballast water
WO2011071047A1 (en) * 2009-12-07 2011-06-16 三井造船株式会社 Method for cleaning membrane cartridge for ballast water treatment and method for cleaning filter
JP5395194B2 (en) * 2009-12-07 2014-01-22 三井造船株式会社 Cleaning method for ballast water treatment membrane cartridge and cleaning method for filter

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