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JP2015097991A - Cleaning agent and cleaning method of permeable membrane - Google Patents

Cleaning agent and cleaning method of permeable membrane Download PDF

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JP2015097991A
JP2015097991A JP2013239029A JP2013239029A JP2015097991A JP 2015097991 A JP2015097991 A JP 2015097991A JP 2013239029 A JP2013239029 A JP 2013239029A JP 2013239029 A JP2013239029 A JP 2013239029A JP 2015097991 A JP2015097991 A JP 2015097991A
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cleaning
permeable membrane
aqueous solution
compound
surfactant
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JP6364751B2 (en
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孝博 川勝
Takahiro Kawakatsu
孝博 川勝
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Kurita Water Industries Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a cleaning agent, a cleaning liquid and a cleaning method capable of removing effectively a contaminant which cannot be removed sufficiently by a conventional cleaning liquid, when a performance such as a permeation flux or a salt rejection rate is lowered since a permeable membrane used for water treatment, especially an aromatic polyamide-based RO membrane is contaminated.SOLUTION: A permeable membrane is cleaned by using a cleaning liquid comprising an aqueous solution of pH 10 or higher containing a chloramine compound, a surfactant and an alkaline agent. As the chloramine compound, a material obtained by mixing a compound having a primary amino group with hypochlorous acid and/or hypochlorite is preferable. As the surfactant, an anionic surfactant is preferable.

Description

本発明は、水処理分野で使用される透過膜の洗浄剤、洗浄液、及び洗浄方法に関する。詳しくは、逆浸透(RO)膜、限外濾過(UF)膜、精密濾過(MF)膜といった透過膜が汚染して、透過流束や阻止率などの膜性能が低下した際に、その性能を効果的に回復させるための洗浄剤と、この洗浄剤を含む洗浄液と、この洗浄液を用いた透過膜の洗浄方法に関する。   The present invention relates to a cleaning agent, a cleaning liquid, and a cleaning method for a permeable membrane used in the field of water treatment. Specifically, when permeation membranes such as reverse osmosis (RO) membranes, ultrafiltration (UF) membranes, microfiltration (MF) membranes become contaminated and the membrane performance such as permeation flux and rejection rate decreases, the performance The present invention relates to a cleaning agent for effectively recovering water, a cleaning liquid containing the cleaning agent, and a method for cleaning a permeable membrane using the cleaning liquid.

現在、全世界的な水供給量不足の対策として、MF、UF、RO膜といった透過膜を用いたかん水の淡水化、排水回収が行われている。これらの透過膜を用いたシステムにおいて、透過膜の汚染による性能低下が問題となっており、汚染した透過膜を効果的に性能回復させる洗浄技術の開発が望まれている。   At present, as a countermeasure against the global shortage of water supply, brine desalination and drainage recovery using permeable membranes such as MF, UF, and RO membranes are being carried out. In systems using these permeable membranes, performance deterioration due to contamination of the permeable membrane is a problem, and development of a cleaning technique for effectively recovering the performance of the contaminated permeable membrane is desired.

近年、水処理用RO膜としては、低圧運転が可能で、脱塩性能に優れる芳香族ポリアミド系のRO膜が広く使われるようになってきている。しかし、芳香族ポリアミド系RO膜は、塩素に対する耐性が低いため、酢酸セルロース系のRO膜のように、運転条件下で塩素と接触させる処理を行うことができず、微生物や有機物による汚染が酢酸セルロース系のRO膜よりも起こりやすいという課題がある。一方、アルカリに対する耐性は、芳香族ポリアミド系RO膜の方が酢酸セルロース系RO膜よりも高く、pH10以上のアルカリ条件での洗浄を行うことが可能である。   In recent years, as an RO membrane for water treatment, an aromatic polyamide RO membrane capable of low-pressure operation and excellent in desalting performance has been widely used. However, since the aromatic polyamide RO membrane has low resistance to chlorine, it cannot be treated with chlorine under operating conditions like the cellulose acetate RO membrane, and contamination by microorganisms and organic matter is not acetic acid. There is a problem that it is more likely to occur than a cellulosic RO membrane. On the other hand, the resistance against alkali is higher in the aromatic polyamide RO membrane than in the cellulose acetate RO membrane, and it is possible to perform cleaning under alkaline conditions of pH 10 or higher.

このような耐アルカリ性の芳香族ポリアミドRO膜に対して、従来から知られている微生物や有機物などの膜汚染物質に有効な洗浄剤として、
アルカリ剤(水酸化ナトリウムなど)
界面活性剤(ラウリル硫酸ナトリウムなど)
キレート剤(EDTAなど)
などがある(非特許文献1)。
For such alkali-resistant aromatic polyamide RO membrane, as a cleaning agent effective for membrane contaminants such as microorganisms and organic substances known conventionally,
Alkaline agent (such as sodium hydroxide)
Surfactant (such as sodium lauryl sulfate)
Chelating agents (EDTA, etc.)
(Non-Patent Document 1).

しかし、RO膜の汚染が激しいと、上記のような薬剤では十分に洗浄を行えない場合がある。   However, when the RO membrane is severely contaminated, there may be a case where the above-mentioned chemicals cannot be sufficiently cleaned.

次亜塩素酸ナトリウムは、微生物や有機物に対して強力な薬剤であるが、先に記述したように、芳香族ポリアミド系RO膜は、塩素に対する耐性が低いため、次亜塩素酸ナトリウムは芳香族ポリアミド系RO膜の洗浄には使用されていない。また、塩素系殺菌剤を用いる場合には、還元剤を用いて遊離塩素を還元した後にRO膜に供給することが知られている(特許文献1)。   Sodium hypochlorite is a powerful agent against microorganisms and organic substances, but as described above, aromatic polyamide RO membranes have low resistance to chlorine, so sodium hypochlorite is aromatic. It is not used for cleaning polyamide RO membranes. In the case of using a chlorine-based disinfectant, it is known that free chlorine is reduced using a reducing agent and then supplied to the RO membrane (Patent Document 1).

膜モジュールを酸洗浄した後、酸化剤で殺菌洗浄を行う膜モジュールの殺菌洗浄方法が提案されている(特許文献2)。この特許文献2には、洗浄対象の透過膜の種類についての記載はなされていないが、膜の除去率(脱塩率)は初期性能で95%と記載されていることから、洗浄対象膜は酢酸セルロース系のRO膜であると考えられる。また、特許文献2には、透過流束が低下したRO膜に対して適用したことも、アルカリ条件であるとも記述されていない。   A membrane module sterilization cleaning method has been proposed in which a membrane module is subjected to acid cleaning and then sterilized cleaning with an oxidizing agent (Patent Document 2). Although this Patent Document 2 does not describe the type of permeable membrane to be cleaned, the membrane removal rate (desalting rate) is described as 95% in the initial performance. It is thought to be a cellulose acetate RO membrane. Further, Patent Document 2 does not describe that the application to an RO membrane having a reduced permeation flux is an alkaline condition.

特開平9−57067号公報JP-A-9-57067 特開平1−307407号公報JP-A-1-307407

「膜の劣化とファウリング対策 膜汚染防止・洗浄法からトラブルシューティングまで」(NTS発行)p142 2008"Membrane degradation and fouling countermeasures: From membrane contamination prevention and cleaning methods to troubleshooting" (NTS issue) p142 2008

本発明は、水処理に使用される透過膜、特に芳香族ポリアミド系RO膜が汚染して透過流束や脱塩率などの性能が低下した際に、従来の洗浄剤では十分に除去することができない汚染物質を効果的に除去することができる洗浄剤及び洗浄液と洗浄方法を提供することを課題とする。   In the present invention, when a permeation membrane used for water treatment, particularly an aromatic polyamide RO membrane is contaminated and the performance such as permeation flux and desalination rate is deteriorated, the conventional cleaning agent can sufficiently remove the permeation membrane. It is an object to provide a cleaning agent, a cleaning liquid, and a cleaning method that can effectively remove contaminants that cannot be removed.

本発明者は上記課題を解決すべく鋭意検討を重ねた結果、塩素系洗浄剤成分としてクロラミン化合物を用いることにより、透過膜に対する酸化作用が抑制され、塩素耐性の低い芳香族ポリアミド系RO膜に対しても、洗浄剤として適用可能であること、また、その際、界面活性剤を併用することにより、界面活性剤の分散効果で洗浄効果が更に高められることを見出した。本発明により提供されるクロラミン化合物と界面活性剤を含むアルカリ性の水溶液であれば、アルカリ条件における剥離効果、加水分解効果に加えて、クロラミン化合物による殺菌及び有機物分解効果、更には、界面活性剤による分散効果が相乗的に作用して良好なアルカリ洗浄効果を得ることができる。   As a result of intensive studies to solve the above problems, the inventor of the present invention uses an chloramine compound as a chlorine-based cleaning agent component to suppress an oxidative action on a permeable membrane, thereby producing an aromatic polyamide-based RO membrane with low chlorine resistance. On the other hand, it was found that the present invention can be applied as a cleaning agent, and in that case, by using a surfactant in combination, the cleaning effect can be further enhanced by the dispersing effect of the surfactant. In the case of an alkaline aqueous solution containing a chloramine compound and a surfactant provided by the present invention, in addition to the peeling effect and hydrolysis effect under alkaline conditions, the bactericidal and organic substance decomposing effects by the chloramine compound, and further by the surfactant The dispersion effect acts synergistically to obtain a good alkali cleaning effect.

本発明はこのような知見に基いて達成されたものであり、以下を要旨とする。   The present invention has been achieved on the basis of such findings, and the gist thereof is as follows.

[1] クロラミン化合物、界面活性剤及びアルカリ剤を含むpH13以上の水溶液よりなることを特徴とする透過膜の洗浄剤。 [1] A cleaning agent for a permeable membrane comprising an aqueous solution having a pH of 13 or more containing a chloramine compound, a surfactant and an alkali agent.

[2] [1]において、前記水溶液のpHが13以上15以下であることを特徴とする透過膜の洗浄剤。 [2] The cleaning agent for a permeable membrane according to [1], wherein the aqueous solution has a pH of 13 or more and 15 or less.

[3] [1]又は[2]において、前記水溶液中のクロラミン化合物の濃度が0.2〜2Mで、界面活性剤の濃度が0.01〜1Mで、アルカリ剤の濃度が1〜3Mであることを特徴とする透過膜の洗浄剤。 [3] In [1] or [2], the concentration of the chloramine compound in the aqueous solution is 0.2 to 2M, the concentration of the surfactant is 0.01 to 1M, and the concentration of the alkaline agent is 1 to 3M. A cleaning agent for a permeable membrane, characterized by

[4] [1]ないし[3]のいずれかにおいて、前記クロラミン化合物がモノクロロスルファミン酸を含むことを特徴とする透過膜の洗浄剤。 [4] The permeable membrane cleaning agent according to any one of [1] to [3], wherein the chloramine compound contains monochlororosulmic acid.

[5] [1]ないし[4]のいずれかにおいて、前記クロラミン化合物が、1級アミノ基を有する化合物、アンモニア及びアンモニウム塩よりなる群から選ばれる1種又は2種以上(以下「NH系化合物」と称す。)と、次亜塩素酸及び/又は次亜塩素酸塩とを混合することにより得られることを特徴とする透過膜の洗浄剤。 [5] In any one of [1] to [4], the chloramine compound is one or more selected from the group consisting of a compound having a primary amino group, ammonia and an ammonium salt (hereinafter referred to as “NH 2 system”). A permeation membrane cleaning agent obtained by mixing hypochlorous acid and / or hypochlorite.

[6] [5]において、次亜塩素酸及び/又は次亜塩素酸塩と、前記NH系化合物とを、次亜塩素酸及び/又は次亜塩素酸塩由来の有効塩素濃度(Cl)と、前記NH系化合物由来の窒素原子Nとのモル比(Cl/Nモル比)が0.1〜1となるように混合することを特徴とする透過膜の洗浄剤。 [6] In [5], hypochlorous acid and / or hypochlorite and the NH 2 -based compound are mixed with effective chlorine concentration (Cl 2) derived from hypochlorous acid and / or hypochlorite. ) And the nitrogen atom N derived from the NH 2 -based compound (Cl 2 / N molar ratio) is mixed so that the molar ratio is 0.1 to 1.

[7] [5]又は[6]において、アルカリ剤の水溶液に前記NH系化合物を添加して溶解し、得られたNH系化合物水溶液に次亜塩素酸及び/又は次亜塩素酸塩を添加して混合する工程を経て得られることを特徴とする透過膜の洗浄剤。 [7] In [5] or [6], the NH 2 -based compound is added and dissolved in an aqueous solution of an alkaline agent, and hypochlorous acid and / or hypochlorite is added to the obtained NH 2 -based compound aqueous solution. A permeable membrane cleaning agent obtained through a step of adding and mixing.

[8] [7]において、前記アルカリ剤の水溶液は、水の量が50〜90重量%であり、アルカリ剤とNH系化合物との割合がN/アルカリ金属(モル比)で0.5〜0.7となるようにNH系化合物を添加し、次亜塩素酸及び/又は次亜塩素酸塩を有効塩素(Cl)濃度5〜20重量%の水溶液として添加することを特徴とする透過膜の洗浄剤。 [8] In [7], the aqueous solution of the alkali agent has an amount of water of 50 to 90% by weight, and the ratio of the alkali agent to the NH 2 -based compound is 0.5 in terms of N / alkali metal (molar ratio). An NH 2 -based compound is added so as to be ˜0.7, and hypochlorous acid and / or hypochlorite is added as an aqueous solution having an effective chlorine (Cl 2 ) concentration of 5 to 20% by weight. Permeable membrane cleaner.

[9] [1]ないし[8]のいずれかにおいて、前記界面活性剤が分子量1000以下のアニオン系界面活性剤であることを特徴とする透過膜の洗浄剤。 [9] The cleaning agent for a permeable membrane according to any one of [1] to [8], wherein the surfactant is an anionic surfactant having a molecular weight of 1000 or less.

[10] [9]において、前記アニオン系界面活性剤が、アルキルベンゼンスルホン酸塩及びアルキル硫酸塩よりなる群から選ばれる1種又は2種以上であることを特徴とする透過膜の洗浄剤。 [10] The cleaning agent for a permeable membrane according to [9], wherein the anionic surfactant is one or more selected from the group consisting of alkylbenzene sulfonate and alkyl sulfate.

[11] [1]ないし[10]のいずれかに記載の透過膜の洗浄剤を希釈してなる、pH10以上の水溶液よりなることを特徴とする透過膜の洗浄液。 [11] A permeable membrane cleaning solution comprising an aqueous solution having a pH of 10 or higher, which is obtained by diluting the permeable membrane cleaner according to any one of [1] to [10].

[12] クロラミン化合物、界面活性剤及びアルカリ剤を含むpH10以上の水溶液よりなることを特徴とする透過膜の洗浄液。 [12] A permeable membrane cleaning solution comprising an aqueous solution having a pH of 10 or more containing a chloramine compound, a surfactant and an alkali agent.

[13] [11]又は[12]において、前記水溶液のpHが12以上13以下であることを特徴とする透過膜の洗浄液。 [13] A cleaning solution for a permeable membrane according to [11] or [12], wherein the pH of the aqueous solution is 12 or more and 13 or less.

[14] [11]ないし[13]のいずれかにおいて、前記水溶液中のクロラミン化合物の濃度が0.005〜0.5Mで、界面活性剤の濃度が0.0001〜0.05Mであることを特徴とする透過膜の洗浄液。 [14] In any one of [11] to [13], the concentration of the chloramine compound in the aqueous solution is 0.005 to 0.5M, and the concentration of the surfactant is 0.0001 to 0.05M. A permeable membrane cleaning solution.

[15] [11]ないし[14]のいずれかに記載の透過膜の洗浄液に透過膜を接触させることを特徴とする透過膜の洗浄方法。 [15] A method for cleaning a permeable membrane, comprising bringing the permeable membrane into contact with the permeable membrane cleaning liquid according to any one of [11] to [14].

本発明によれば、塩素耐性の低い芳香族ポリアミド系RO膜であっても、塩素系洗浄剤成分を適用することが可能となる。このため、アルカリ条件における剥離効果、加水分解効果に加えて、クロラミン化合物による殺菌及び有機物分解効果、更には界面活性剤による分散効果が付加され、これらの効果が相乗的に作用して良好なアルカリ洗浄効果でRO膜等の透過膜の性能を効果的に回復させることができる。   According to the present invention, a chlorine-based detergent component can be applied even to an aromatic polyamide-based RO membrane having low chlorine resistance. For this reason, in addition to the exfoliation effect and hydrolysis effect under alkaline conditions, sterilization and organic matter decomposition effects by chloramine compounds, as well as dispersion effects by surfactants, are added, and these effects act synergistically to achieve good alkali The performance of the permeable membrane such as the RO membrane can be effectively recovered by the cleaning effect.

実施例で用いた平膜試験装置の構成を示す模式図である。It is a schematic diagram which shows the structure of the flat membrane test apparatus used in the Example. 図1の平膜試験装置の密閉容器の構造を示す断面図である。It is sectional drawing which shows the structure of the airtight container of the flat membrane test apparatus of FIG.

以下に本発明の実施の形態を詳細に説明する。   Hereinafter, embodiments of the present invention will be described in detail.

本発明の透過膜の洗浄剤は、クロラミン化合物、界面活性剤及びアルカリ剤を含むpH13以上の水溶液よりなるものである。本発明の透過膜の洗浄液は、この洗浄剤を希釈してなるpH10以上の水溶液よりなる。以下において、本発明の透過膜の洗浄剤、及びこれを希釈してなる洗浄液を「クロラミン化合物/界面活性剤含有アルカリ水溶液」と称す場合がある。   The cleaning agent for a permeable membrane of the present invention comprises an aqueous solution having a pH of 13 or more containing a chloramine compound, a surfactant and an alkali agent. The cleaning liquid for the permeable membrane of the present invention comprises an aqueous solution having a pH of 10 or more obtained by diluting the cleaning agent. Hereinafter, the cleaning agent for a permeable membrane of the present invention and a cleaning solution obtained by diluting the same may be referred to as “chloramine compound / surfactant-containing alkaline aqueous solution”.

<洗浄機構>
クロラミン化合物としては、以下の反応式(1),(2)に示すような反応で次亜塩素酸(HOCl)と1級アミノ基を有する化合物(XNH)とを反応させて得られる、アミノ基の水素原子が塩素原子に置換した化合物(XNHCl)が好ましい。この化合物は、膜に対する酸化作用が弱いため、塩素耐性の低い芳香族ポリアミド系RO膜であっても洗浄剤として用いることが可能となる。
XNH+HOCl⇔XNHCl+HO (1)
XNH+OCl⇔XNHCl+OH (2)
<Washing mechanism>
As the chloramine compound, an amino acid obtained by reacting hypochlorous acid (HOCl) with a compound having a primary amino group (XNH 2 ) by the reaction shown in the following reaction formulas (1) and (2), A compound (XNHCl) in which the hydrogen atom of the group is substituted with a chlorine atom is preferred. Since this compound has a weak oxidizing action on the membrane, even an aromatic polyamide RO membrane with low chlorine resistance can be used as a cleaning agent.
XNH 2 + HOCl⇔XNHCl + H 2 O (1)
XNH 2 + OCl ⇔XNHCl + OH (2)

本発明は、アルカリ条件下における塩素系洗浄剤のRO膜等の透過膜の洗浄への適用を可能とする。本発明では、アルカリ条件での洗浄による有機物の剥離作用や加水分解作用に、クロラミン化合物による殺菌及び有機物分解作用と、界面活性剤による分散作用が相乗的に付加される。このため、本発明によれば、アルカリ洗浄の効果を高め、汚染した透過膜の性能を効果的に回復させることができる。   The present invention enables application of a chlorine-based cleaning agent to cleaning of a permeable membrane such as an RO membrane under alkaline conditions. In the present invention, the sterilization and organic substance decomposition action by the chloramine compound and the dispersing action by the surfactant are synergistically added to the organic substance peeling action and hydrolysis action by washing under alkaline conditions. For this reason, according to this invention, the effect of alkali cleaning can be improved and the performance of the contaminated permeable membrane can be recovered effectively.

<透過膜>
本発明は、RO膜、特に塩素耐性の低い芳香族ポリアミド系RO膜(ナノ濾過(NF)膜を含む)を洗浄対象とする場合に、その洗浄効果が有効に発揮される。ただし、洗浄対象の透過膜は何ら芳香族ポリアミド系RO膜等のRO膜に限定されず、本発明は、UF膜、MF膜にも適用することができ、その膜素材も限定されない。また、膜の形式等にも何ら制限はなく、本発明は、幅広い分野における水処理用透過膜の洗浄に有効に適用される。
<Permeation membrane>
In the present invention, when an RO membrane, particularly an aromatic polyamide RO membrane having a low chlorine resistance (including a nanofiltration (NF) membrane) is to be cleaned, the cleaning effect is effectively exhibited. However, the permeable membrane to be cleaned is not limited to an RO membrane such as an aromatic polyamide RO membrane, and the present invention can be applied to a UF membrane and an MF membrane, and the membrane material is not limited. Moreover, there is no restriction | limiting also in the form of a film | membrane etc., This invention is applied effectively for the washing | cleaning of the permeable membrane for water treatment in a wide field | area.

<クロラミン化合物>
本発明において、塩素系洗浄剤成分として用いるクロラミン化合物は、1級アミノ基を有する化合物、アンモニア、及びアンモニウム塩のいずれか(以下、これらを「NH系化合物」と称す。)と、次亜塩素酸及び/又は次亜塩素酸塩とを混合することにより生成させることが好ましい。1級アミノ基を有する化合物としては、脂肪族アミン、芳香族アミン、スルファミン酸、スルファニル酸、スルファモイル安息香酸、アミノ酸などを挙げることができる。また、アンモニウム塩としては、塩化アンモニウム、硫酸アンモニウム等が挙げられる。これらは、1種を単独で用いてもよく、2種以上を混合して用いてもよい。これらのNH系化合物の中でもスルファミン酸(NHSOOH)が好ましい。スルファミン酸を用いてモノクロロスルファミンを生成させると安定なクロラミン化合物となる。スルファミン酸は、炭素を含まないため洗浄剤のTOC値を増加させない。スルファミン酸とアルカリ剤とを併用することで、非常に有効な洗浄剤となる。
<Chloramine compound>
In the present invention, the chloramine compound used as the chlorine-based cleaning agent component is either a compound having a primary amino group, ammonia, or an ammonium salt (hereinafter referred to as “NH 2 -based compound”), hypochlorous. It is preferable to produce by mixing chloric acid and / or hypochlorite. Examples of the compound having a primary amino group include aliphatic amines, aromatic amines, sulfamic acids, sulfanilic acids, sulfamoylbenzoic acids, and amino acids. Examples of ammonium salts include ammonium chloride and ammonium sulfate. These may be used alone or in combination of two or more. Of these NH 2 compounds, sulfamic acid (NH 2 SO 2 OH) is preferable. When monochlororosulfamine is produced using sulfamic acid, it becomes a stable chloramine compound. Since sulfamic acid does not contain carbon, it does not increase the TOC value of the cleaning agent. By using sulfamic acid and an alkaline agent in combination, a very effective cleaning agent is obtained.

一方、NH系化合物と反応させる次亜塩素酸塩としては、次亜塩素酸ナトリウム等の次亜塩素酸のアルカリ金属塩、次亜塩素酸カルシウム等の次亜塩素酸のアルカリ土類金属塩等を用いることができる。これらは1種を単独で用いてもよく、2種以上を混合して用いてもよい。 On the other hand, hypochlorite to be reacted with NH 2 -based compounds includes alkali metal salts of hypochlorous acid such as sodium hypochlorite and alkaline earth metal salts of hypochlorous acid such as calcium hypochlorite. Etc. can be used. These may be used alone or in combination of two or more.

NH系化合物と次亜塩素酸及び/又は次亜塩素酸塩を混合してクロラミン化合物を生成させる場合、NH系化合物と次亜塩素酸及び/又は次亜塩素酸塩とは、次亜塩素酸及び/又は次亜塩素酸塩由来の有効塩素(Cl)と、NH系化合物由来の窒素原子Nとのモル比であるCl/Nモル比が、0.1〜1となるように用いることが、クロラミンの生成効率と安定性の点において好ましい。 When an NH 2 -based compound and hypochlorous acid and / or hypochlorite are mixed to produce a chloramine compound, the NH 2 -based compound and hypochlorous acid and / or hypochlorite are hypochlorous acid. The Cl 2 / N molar ratio, which is the molar ratio between the effective chlorine (Cl 2 ) derived from chloric acid and / or hypochlorite and the nitrogen atom N derived from the NH 2 compound, is 0.1 to 1. It is preferable to use the chloramine in view of the production efficiency and stability of chloramine.

Cl/Nモル比が上記上限よりも大きいと遊離塩素が生成する可能性があり、上記下限よりも小さいと使用したNH系化合物に対してクロラミンの生成効率が低くなる。
なおこの場合、次亜塩素酸及び/又は次亜塩素酸塩の量がクロラミン化合物/界面活性剤含有アルカリ水溶液中のクロラミン化合物量となる。
If the Cl 2 / N molar ratio is larger than the above upper limit, free chlorine may be generated. If the Cl 2 / N molar ratio is smaller than the above lower limit, the production efficiency of chloramine is lowered with respect to the NH 2 -based compound used.
In this case, the amount of hypochlorous acid and / or hypochlorite is the amount of chloramine compound in the chloramine compound / surfactant-containing alkaline aqueous solution.

<アルカリ剤>
本発明の洗浄剤に用いるアルカリ剤は、クロラミン化合物/界面活性剤含有アルカリ水溶液中において可溶性を維持することができるものであり、水酸化ナトリウム、水酸化カリウム等のアルカリ金属の水酸化物を用いることができる。これらは1種を単独で用いてもよく、2種以上を混合して用いてもよい。
<Alkaline agent>
The alkaline agent used in the cleaning agent of the present invention can maintain solubility in a chloramine compound / surfactant-containing alkaline aqueous solution, and uses alkali metal hydroxides such as sodium hydroxide and potassium hydroxide. be able to. These may be used alone or in combination of two or more.

<界面活性剤>
本発明で用いる界面活性剤としては、洗浄効果の面から、分子量1000以下のものが好ましい。分子量が過度に大きい界面活性剤では洗浄効果が得られないだけでなく、膜を汚染する場合がある。
<Surfactant>
As the surfactant used in the present invention, those having a molecular weight of 1000 or less are preferable from the viewpoint of cleaning effect. A surfactant having an excessively high molecular weight may not only provide a cleaning effect, but may contaminate the membrane.

界面活性剤としては、ドデシルベンゼンスルホン酸ナトリウム等のアルキルベンゼンスルホン酸塩、ラウリル硫酸ナトリウム等のアルキル硫酸塩といったアニオン系界面活性剤、ジエチレングリコールモノメチルエーテルなどのポリアルキレングリコールモノアルキルエーテルのようなノニオン系界面活性剤などの1種又は2種以上を用いることができる。これらのうち、特に分散効果の面でアニオン系界面活性剤が好ましい。   Surfactants include anionic surfactants such as alkyl benzene sulfonates such as sodium dodecylbenzene sulfonate, alkyl sulfates such as sodium lauryl sulfate, and nonionic interfaces such as polyalkylene glycol monoalkyl ethers such as diethylene glycol monomethyl ether. 1 type (s) or 2 or more types, such as an activator, can be used. Among these, an anionic surfactant is particularly preferable in terms of dispersion effect.

<pH・クロラミン化合物濃度・界面活性剤濃度>
本発明の洗浄液は、クロラミン化合物/界面活性剤含有アルカリ水溶液よりなり、pHが10以上であることを特徴とする。洗浄液のpHが10未満であると、透過流束を十分に回復させることができない。洗浄液のpHは高い方が洗浄効果に優れるが、高過ぎると、洗浄液としての取り扱い性が悪くなり、RO膜等の透過膜が劣化する危険性が高くなる。洗浄液のpHは好ましくは12以上13以下である。
<PH / chloramine compound concentration / surfactant concentration>
The cleaning liquid of the present invention comprises a chloramine compound / surfactant-containing alkaline aqueous solution, and has a pH of 10 or more. If the pH of the cleaning liquid is less than 10, the permeation flux cannot be sufficiently recovered. The higher the pH of the cleaning liquid is, the better the cleaning effect is. However, when the pH is too high, the handling property as the cleaning liquid is deteriorated and the risk of deterioration of the permeable membrane such as the RO membrane is increased. The pH of the cleaning liquid is preferably 12 or more and 13 or less.

このクロラミン化合物/界面活性剤含有アルカリ水溶液よりなる洗浄液中のクロラミン化合物濃度は0.005〜0.5Mであることが好ましく、特に0.01〜0.2Mであることが好ましい。洗浄液のクロラミン化合物濃度が低過ぎると十分な洗浄効果を得ることができず、高過ぎるとRO膜等の透過膜を劣化させるおそれがある。クロラミン化合物濃度0.005〜0.5Mとは全塩素濃度で355〜35,500mg−Cl/Lに相当する濃度である。全塩素濃度はJIS K0400−33−10.1999等で規定するDPD法により測定することができる。 The concentration of the chloramine compound in the cleaning liquid comprising the chloramine compound / surfactant-containing alkaline aqueous solution is preferably 0.005 to 0.5M, and particularly preferably 0.01 to 0.2M. If the concentration of the chloramine compound in the cleaning liquid is too low, a sufficient cleaning effect cannot be obtained, and if it is too high, the permeable membrane such as the RO membrane may be deteriorated. A chloramine compound concentration of 0.005 to 0.5 M is a concentration corresponding to a total chlorine concentration of 355 to 35,500 mg-Cl 2 / L. The total chlorine concentration can be measured by the DPD method specified in JIS K0400-33-10.1999.

クロラミン化合物は、従来、透過膜のスライムコントロール剤として用いられている。スライムコントロール剤としてのクロラミン化合物は、通常、全塩素濃度として0.05〜50mg−Cl/L程度の低濃度で用いられる。その際のpHは10未満である。これに対し、本発明の洗浄液は、クロラミン化合物を上記のような高濃度で含有し、pH10以上の高いアルカリ性を有し高い洗浄効果を有する。 Chloramine compounds are conventionally used as a slime control agent for permeable membranes. The chloramine compound as the slime control agent is usually used at a low concentration of about 0.05 to 50 mg-Cl 2 / L as the total chlorine concentration. The pH at that time is less than 10. On the other hand, the cleaning liquid of the present invention contains the chloramine compound at a high concentration as described above, has a high alkalinity of pH 10 or higher, and has a high cleaning effect.

また、クロラミン化合物/界面活性剤含有アルカリ水溶液よりなる本発明の洗浄液中の界面活性剤濃度は、0.0001〜0.05Mであることが好ましく、特に0.001〜0.02Mであることが好ましい。界面活性剤濃度が低過ぎると界面活性剤による分散効果、洗浄作用の向上効果を十分に得ることができず、高過ぎるとむしろ界面活性剤の会合が強くなって洗浄効果を低下させるおそれがある。   Further, the surfactant concentration in the cleaning liquid of the present invention comprising a chloramine compound / surfactant-containing alkaline aqueous solution is preferably 0.0001 to 0.05M, particularly preferably 0.001 to 0.02M. preferable. If the surfactant concentration is too low, the dispersion effect by the surfactant and the effect of improving the cleaning action cannot be sufficiently obtained. If the surfactant concentration is too high, the association of the surfactant becomes rather strong and the cleaning effect may be lowered. .

本発明の洗浄剤は、クロラミン化合物と界面活性剤とアルカリ剤を含むpH13以上、好ましくはpH13〜15の水溶液よりなることが好ましく、また、該水溶液中のクロラミン化合物濃度は0.2〜2M、特に1〜2Mで、アルカリ剤濃度は1〜3Mで、界面活性剤濃度は0.01〜1M、特に0.03〜0.3Mであることが好ましい。この洗浄剤は、上述のようなpH、クロラミン化合物及び界面活性剤濃度の本発明の洗浄液を調製する際に、水(好ましくは純水)で希釈される。   The cleaning agent of the present invention is preferably composed of an aqueous solution containing a chloramine compound, a surfactant, and an alkali agent at a pH of 13 or more, preferably a pH of 13 to 15, and the chloramine compound concentration in the aqueous solution is 0.2 to 2M. In particular, it is preferably 1 to 2M, the alkali agent concentration is 1 to 3M, and the surfactant concentration is 0.01 to 1M, particularly 0.03 to 0.3M. This cleaning agent is diluted with water (preferably pure water) when preparing the cleaning liquid of the present invention having the above-mentioned pH, chloramine compound and surfactant concentration.

<洗浄剤及び洗浄液の製造方法>
本発明の洗浄剤は、前述のアルカリ剤の水溶液にスルファミン酸等のNH系化合物を添加して溶解し、得られたNH系化合物水溶液に、次亜塩素酸及び/又は次亜塩素酸塩を添加して混合することにより調製することができる。上記アルカリ剤の水溶液は、水の量を50〜90重量%とすることが好ましい。界面活性剤は、洗浄剤の調製工程のうち、いずれの工程で添加されてもよく、前述のアルカリ剤の水溶液に予め含まれていてもよく、また、NH系化合物水溶液に次亜塩素酸及び/又は次亜塩素酸塩を添加する際に添加してもよく、次亜塩素酸及び/又は次亜塩素酸塩の添加の前後で添加してもよい。好ましくは、界面活性剤は次亜塩素酸及び/又は次亜塩素酸塩の添加の後に添加される。
<Manufacturing method of cleaning agent and cleaning liquid>
The cleaning agent of the present invention is prepared by adding and dissolving an NH 2 -based compound such as sulfamic acid in the aqueous solution of the alkali agent described above, and adding hypochlorous acid and / or hypochlorous acid to the resulting NH 2 -based compound aqueous solution. It can be prepared by adding salt and mixing. It is preferable that the amount of water in the aqueous solution of the alkali agent is 50 to 90% by weight. The surfactant may be added in any of the cleaning agent preparation steps, may be included in advance in the aqueous solution of the alkali agent, and hypochlorous acid in the NH 2 -based compound aqueous solution. And / or may be added when hypochlorite is added, or may be added before or after the addition of hypochlorous acid and / or hypochlorite. Preferably, the surfactant is added after the addition of hypochlorous acid and / or hypochlorite.

スルファミン酸等の1級アミノ基を有する化合物は、塩の形で添加してもよい。この塩としては、クロラミン化合物/界面活性剤含有アルカリ水溶液としたときに可溶性のものが挙げられ、スルファミン酸ナトリウム、スルファミン酸カリウム、スルファミン酸アンモニウム等を用いることができる。NH系化合物は、本発明の洗浄剤中のクロラミン化合物濃度が上記濃度となるように添加される。NH系化合物の添加量は、アルカリ剤とNH系化合物との含有割合が、N/アルカリ金属(モル比)で0.5〜0.7とするのが好ましい。NH系化合物は、粉末状態で、あるいは水溶液の状態で添加することができる。NH系化合物としてスルファミン酸塩を用いる場合、スルファミン酸塩に含まれるアルカリ金属の量は、アルカリとして加算される。水溶液を用いる場合は、水溶液に含まれる水の量は、前記アルカリ水溶液の水の量として加算される。 A compound having a primary amino group such as sulfamic acid may be added in the form of a salt. Examples of the salt include those that are soluble in a chloramine compound / surfactant-containing alkaline aqueous solution, and sodium sulfamate, potassium sulfamate, ammonium sulfamate, and the like can be used. The NH 2 -based compound is added so that the chloramine compound concentration in the cleaning agent of the present invention is the above concentration. Amount of NH 2 compound, the content ratio of the alkaline agent and the NH 2 compound is preferably set to 0.5 to 0.7 with N / alkali metal (molar ratio). The NH 2 -based compound can be added in a powder state or in an aqueous solution state. When using a sulfamate as the NH 2 -based compound, the amount of alkali metal contained in the sulfamate is added as an alkali. When an aqueous solution is used, the amount of water contained in the aqueous solution is added as the amount of water in the alkaline aqueous solution.

一方、次亜塩素酸及び/又は次亜塩素酸塩は、有効塩素(Cl)濃度として5〜20重量%、好ましくは10〜15重量%の水溶液として添加するのが好ましい。次亜塩素酸及び/又は次亜塩素酸塩は、本発明の洗浄剤中のクロラミン化合物濃度が上記濃度となるように、また、NH系化合物と次亜塩素酸及び/又は次亜塩素酸塩との含有割合が、前述のCl/Nモル比となるように添加される。これにより発泡や塩素臭の発生はなく、反応性、安定性、取扱性、無塩素臭等に優れた水溶液製剤からなる本発明の洗浄剤を効率よく製造することができる。この場合でも、次亜塩素酸及び/又は次亜塩素酸塩は徐々に添加して混合するのが好ましい。 On the other hand, hypochlorous acid and / or hypochlorite is preferably added as an aqueous solution having an effective chlorine (Cl 2 ) concentration of 5 to 20 wt%, preferably 10 to 15 wt%. Hypochlorous acid and / or hypochlorite is used so that the concentration of the chloramine compound in the cleaning agent of the present invention is the above concentration, and the NH 2 -based compound and hypochlorous acid and / or hypochlorous acid. It is added so that the content ratio with the salt is the aforementioned Cl 2 / N molar ratio. Thereby, there is no generation | occurrence | production of foaming and a chlorine odor, and the cleaning agent of this invention which consists of aqueous solution formulation excellent in reactivity, stability, handleability, a chlorine-free odor, etc. can be manufactured efficiently. Even in this case, it is preferable to gradually add and mix hypochlorous acid and / or hypochlorite.

本発明の洗浄液は、このようにして製造された本発明の洗浄剤を水、好ましくは純水でpH10以上で、前述の好適なクロラミン化合物及び界面活性剤濃度となるように希釈することにより製造される。ただし、本発明の洗浄液は本発明の洗浄剤を経ることなく、直接上記と同様の方法で製造することもできる。   The cleaning liquid of the present invention is produced by diluting the thus-prepared cleaning agent of the present invention with water, preferably pure water, at a pH of 10 or more so as to have the above-mentioned preferred chloramine compound and surfactant concentrations. Is done. However, the cleaning liquid of the present invention can also be produced directly by the same method as above without passing through the cleaning agent of the present invention.

<その他の洗浄剤成分>
本発明で用いる洗浄剤又は洗浄液には、その洗浄効果を損なわない範囲において、他の洗浄剤成分を添加してもよい。
例えば、膜汚染物質の剥離効果を高めるために、EDTA(エチレンジアミン四酢酸)、EGTA(エチレングリコールビス(アミノエチルエーテル)四酢酸)、IDA(イミノ二酢酸)等のキレート剤などの他の洗浄剤成分の1種又は2種以上を添加してもよい。
<Other cleaning ingredients>
To the cleaning agent or cleaning liquid used in the present invention, other cleaning component may be added as long as the cleaning effect is not impaired.
For example, other cleaning agents such as chelating agents such as EDTA (ethylenediaminetetraacetic acid), EGTA (ethyleneglycolbis (aminoethylether) tetraacetic acid), IDA (iminodiacetic acid), etc. in order to enhance the peeling effect of membrane contaminants One or more components may be added.

また、分子量1000以下、好ましくは分子量60〜1000のポリオール化合物を併用することにより、RO膜等の透過膜への浸透と汚染物質の溶解の作用で更に洗浄効果を高めることができる。ここで、ポリオール化合物の分子量が1000を超えるとRO膜等の透過膜汚染に寄与する可能性がある。分子量1000以下のポリオール化合物としては、例えばエチレングリコール、プロピレングリコール、ポリエチレングリコール(重合度2〜22)等を用いることができる。これらのポリオール化合物は、1種を単独で用いてもよく、2種以上を混合して用いてもよい。
このようなポリオール化合物は、本発明の洗浄剤又は洗浄液に添加してもよく、以下のアルカリ水溶液や酸水溶液に添加して用いてもよい。
In addition, by using a polyol compound having a molecular weight of 1000 or less, preferably a molecular weight of 60 to 1000, the cleaning effect can be further enhanced by the permeation into the permeable membrane such as the RO membrane and the dissolution of the contaminant. Here, when the molecular weight of the polyol compound exceeds 1000, there is a possibility of contributing to permeable membrane contamination such as RO membrane. As the polyol compound having a molecular weight of 1000 or less, for example, ethylene glycol, propylene glycol, polyethylene glycol (degree of polymerization 2 to 22) and the like can be used. These polyol compounds may be used individually by 1 type, and 2 or more types may be mixed and used for them.
Such a polyol compound may be added to the cleaning agent or cleaning liquid of the present invention, or may be used by adding to the following alkaline aqueous solution or acid aqueous solution.

また、本発明による透過膜の洗浄に前後して、他の洗浄液による膜洗浄を行ってもよい。他の洗浄液による膜洗浄を組み合わせることにより洗浄効果をより一層高めることができる。   In addition, before and after cleaning the permeable membrane according to the present invention, membrane cleaning with another cleaning liquid may be performed. The cleaning effect can be further enhanced by combining film cleaning with other cleaning liquids.

本発明の洗浄液であるクロラミン化合物/界面活性剤含有アルカリ水溶液による洗浄に先立ち、或いは、クロラミン化合物/界面活性剤含有アルカリ水溶液による洗浄後に、クロラミン化合物及び界面活性剤を含まないアルカリ水溶液による洗浄を行うことができる。このアルカリ水溶液のアルカリ剤としては、クロラミン化合物/界面活性剤含有アルカリ水溶液のアルカリ剤として前記したものを用いることができる。このアルカリ水溶液のpHは、洗浄効果と取り扱い性の面から、pH10以上、特にpH12〜13であることが好ましい。   Prior to washing with the chloramine compound / surfactant-containing alkaline aqueous solution, which is the cleaning liquid of the present invention, or after washing with the chloramine compound / surfactant-containing alkaline aqueous solution, washing with an alkaline aqueous solution not containing the chloramine compound / surfactant is performed. be able to. As the alkali agent of the alkaline aqueous solution, those described above as the alkaline agent of the chloramine compound / surfactant-containing alkaline aqueous solution can be used. The pH of the alkaline aqueous solution is preferably pH 10 or more, particularly pH 12 to 13 in terms of cleaning effect and handleability.

また、スケールや金属コロイド除去に有効な酸洗浄を行ってもよく、その酸洗浄には、塩酸、硝酸、クエン酸、シュウ酸などの酸の1種又は2種以上を含む水溶液を用いることができる。この酸水溶液のpHは、洗浄効果と取り扱い性の面から、pH4以下、特にpH1〜3であることが好ましい。   Further, acid cleaning effective for removing scales and metal colloids may be performed. For the acid cleaning, an aqueous solution containing one or more acids such as hydrochloric acid, nitric acid, citric acid, and oxalic acid is used. it can. The pH of the acid aqueous solution is preferably pH 4 or less, particularly preferably pH 1 to 3, in terms of cleaning effect and handleability.

<洗浄方法>
本発明の洗浄液である前記クロラミン化合物/界面活性剤含有アルカリ水溶液を用いて透過膜を洗浄する方法としては、このクロラミン化合物/界面活性剤含有アルカリ水溶液に透過膜を接触させればよく、特に制限はない。通常、透過膜モジュールの原水側にクロラミン化合物/界面活性剤含有アルカリ水溶液を導入して静置する浸漬洗浄が行われる。この浸漬洗浄に際して、透過膜に接触しているクロラミン化合物/界面活性剤含有アルカリ水溶液のpHが10以上、好ましくは12〜13でクロラミン化合物濃度が0.005〜0.5M、特に0.01〜0.2Mで、界面活性剤濃度が0.0001〜0.05M、特に0.001〜0.02Mである。
<Washing method>
As a method for cleaning the permeable membrane using the chloramine compound / surfactant-containing alkaline aqueous solution, which is the cleaning liquid of the present invention, the permeable membrane may be brought into contact with the chloramine compound / surfactant-containing alkaline aqueous solution, and the method is particularly limited. There is no. Usually, immersion cleaning is performed by introducing a chloramine compound / surfactant-containing alkaline aqueous solution to the raw water side of the permeable membrane module and allowing to stand. In this immersion cleaning, the pH of the chloramine compound / surfactant-containing alkaline aqueous solution in contact with the permeable membrane is 10 or more, preferably 12 to 13, and the chloramine compound concentration is 0.005 to 0.5 M, particularly 0.01 to. At 0.2M, the surfactant concentration is 0.0001-0.05M, especially 0.001-0.02M.

クロラミン化合物/界面活性剤含有アルカリ水溶液による洗浄の前後で、前述のアルカリ水溶液や酸水溶液を用いて洗浄を行う場合も、通常の場合、上記と同様の浸漬洗浄が採用される。   When washing is performed using the aforementioned alkaline aqueous solution or acid aqueous solution before and after washing with the chloramine compound / surfactant-containing alkaline aqueous solution, the same immersion washing as described above is usually employed.

クロラミン化合物/界面活性剤含有アルカリ水溶液、その他の洗浄液による浸漬洗浄時間には特に制限はなく、目的とする膜性能の回復率が得られる程度であればよいが、通常2〜24時間程度である。   There is no particular limitation on the immersion cleaning time with the chloramine compound / surfactant-containing alkaline aqueous solution or other cleaning liquid, and it is sufficient that the recovery rate of the target film performance is obtained, but it is usually about 2 to 24 hours. .

クロラミン化合物/界面活性剤含有アルカリ水溶液による洗浄と、アルカリ水溶液及び/又は酸水溶液による洗浄とを組み合わせて行う場合、その洗浄手順には特に制限はない。酸水溶液による酸洗浄は、クロラミン化合物/界面活性剤含有アルカリ水溶液による洗浄前に行うと、塩素に対して触媒効果を引き起こす可能性のある金属の低減、除去を行うことができる。アルカリ水溶液によるアルカリ洗浄は、クロラミン化合物/界面活性剤含有アルカリ水溶液による洗浄の前に行ってもよく、後に行ってもよい。アルカリ水溶液によるアルカリ洗浄をクロラミン化合物/界面活性剤含有アルカリ水溶液による洗浄の後に行うと、膜劣化のリスクのない追加洗浄効果を得ることができる。   When washing with a chloramine compound / surfactant-containing alkaline aqueous solution and washing with an alkaline aqueous solution and / or an aqueous acid solution are performed in combination, the washing procedure is not particularly limited. If the acid cleaning with the acid aqueous solution is performed before the cleaning with the chloramine compound / surfactant-containing alkaline aqueous solution, it is possible to reduce and remove metals that may cause a catalytic effect on chlorine. The alkali cleaning with the aqueous alkali solution may be performed before or after the cleaning with the chloramine compound / surfactant-containing alkaline aqueous solution. When the alkali cleaning with the aqueous alkali solution is performed after the cleaning with the chloramine compound / surfactant-containing alkaline aqueous solution, an additional cleaning effect without risk of film deterioration can be obtained.

上記の洗浄液による洗浄後は、通常、純水等の高純度水を通水して仕上げ洗浄を行う。その後、透過膜システムの運転を再開する。   After washing with the above-described washing liquid, finishing washing is usually performed by passing high-purity water such as pure water. Thereafter, the operation of the permeable membrane system is resumed.

以下に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。   Hereinafter, the present invention will be described more specifically with reference to Examples and Comparative Examples.

以下の実施例及び比較例では、図1,2に示す平膜試験装置を用いてRO膜の洗浄効果を調べた。
この平膜試験装置において、RO膜供給水は、配管11より高圧ポンプ4で、密閉容器1のRO膜をセットした平膜セル2の下側の原水室1Aに供給される。図2に示すように、密閉容器1は、原水室1A側の下ケース1aと、透過水室1B側の上ケース1bとで構成され、下ケース1aと上ケース1bとの間に、平膜セル2がOリング8を介して固定されている。平膜セル2はRO膜2Aの透過水側が多孔質支持板2Bで支持された構成とされている。平膜セル2の下側の原水室1A内はスターラー3で攪拌子5を回転させることにより攪拌される。RO膜透過水は平膜セル2の上側の透過水室1Bを経て配管12より取り出される。濃縮水は配管13より取り出される。密閉容器1内の圧力は、給水配管11に設けた圧力計6と、濃縮水取出配管13に設けた圧力調整バルブ7により調整される。
In the following examples and comparative examples, the cleaning effect of the RO membrane was examined using the flat membrane test apparatus shown in FIGS.
In this flat membrane test apparatus, RO membrane supply water is supplied from a pipe 11 to a raw water chamber 1A below the flat membrane cell 2 in which the RO membrane of the sealed container 1 is set by a high-pressure pump 4. As shown in FIG. 2, the sealed container 1 is composed of a lower case 1a on the raw water chamber 1A side and an upper case 1b on the permeate water chamber 1B side, and a flat membrane is formed between the lower case 1a and the upper case 1b. The cell 2 is fixed via an O-ring 8. The flat membrane cell 2 is configured such that the permeate side of the RO membrane 2A is supported by the porous support plate 2B. The raw water chamber 1 </ b> A below the flat membrane cell 2 is stirred by rotating the stirring bar 5 with a stirrer 3. The RO membrane permeated water is taken out from the pipe 12 through the permeated water chamber 1B on the upper side of the flat membrane cell 2. The concentrated water is taken out from the pipe 13. The pressure in the sealed container 1 is adjusted by a pressure gauge 6 provided in the water supply pipe 11 and a pressure adjusting valve 7 provided in the concentrated water outlet pipe 13.

[実施例1,2、比較例1〜4]
以下の洗浄液を用いて、以下に示す洗浄試験を行った。
[Examples 1 and 2 and Comparative Examples 1 to 4]
The following cleaning tests were performed using the following cleaning solutions.

<洗浄液>
実施例1:0.02Mモノクロロスルファミン酸及び0.0043Mドデシルベンゼンスルホン酸ナトリウムを含むpH12の水酸化ナトリウム水溶液
実施例2:0.02Mモノクロロスルファミン酸及び0.0052Mラウリル硫酸ナトリウムを含むpH12の水酸化ナトリウム水溶液
比較例1:pH12の水酸化ナトリウム水溶液
比較例2:0.0043Mドデシルベンゼンスルホン酸ナトリウムを含むpH12の水酸化ナトリウム水溶液
比較例3:0.0052Mラウリル硫酸ナトリウムを含むpH12の水酸化ナトリウム水溶液
比較例4:0.02Mモノクロロスルファミン酸を含むpH12の水酸化ナトリウム水溶液
<Cleaning liquid>
Example 1: Aqueous pH 12 sodium hydroxide solution containing 0.02M monochlororosulphamic acid and 0.0043M sodium dodecylbenzenesulfonate Example 2: Hydroxylation pH 12 containing 0.02M monochlorosulfuramic acid and 0.0052M sodium lauryl sulfate Sodium aqueous solution Comparative example 1: pH 12 sodium hydroxide aqueous solution Comparative example 2: pH 43 sodium hydroxide aqueous solution containing 0.0043 M sodium dodecylbenzenesulfonate Comparative example 3: pH 12 sodium hydroxide aqueous solution containing 0.0052 M sodium lauryl sulfate Comparative Example 4: pH 12 sodium hydroxide aqueous solution containing 0.02M monochlororosulmic acid

<洗浄試験>
日東電工社製芳香族ポリアミド系RO膜「ES20」を、図1,2に示す平膜試験装置に装填し、0.75MPa、25℃の条件で、汚染前の純水透過流束を測定した。その後、ノニオン界面活性剤を含むセミクリーンKG(横浜油脂工業社製)を375倍に希釈して、0.75MPa、25℃の条件で、72時間通水してRO膜を汚染させた。汚染後のRO膜の純水透過流束を同条件で測定した後、各洗浄液を供給して容器内を洗浄液で満たし、17時間浸漬させて洗浄した。浸漬洗浄後純水を供給して容器内の洗浄液を純水で押し出した後、洗浄後のRO膜の純水透過流束を同条件で測定した。結果を表1に示す。
<Cleaning test>
The aromatic polyamide RO membrane “ES20” manufactured by Nitto Denko Corporation was loaded into the flat membrane test apparatus shown in FIGS. 1 and 2 and the pure water permeation flux before contamination was measured under the conditions of 0.75 MPa and 25 ° C. . Thereafter, semi-clean KG containing nonionic surfactant (manufactured by Yokohama Oils & Fats Industry Co., Ltd.) was diluted 375 times, and water was passed for 72 hours under the conditions of 0.75 MPa and 25 ° C. to contaminate the RO membrane. After measuring the pure water permeation flux of the RO membrane after the contamination under the same conditions, each cleaning solution was supplied to fill the container with the cleaning solution and immersed for 17 hours for cleaning. After immersion cleaning, pure water was supplied and the cleaning liquid in the container was pushed out with pure water, and the pure water permeation flux of the RO membrane after cleaning was measured under the same conditions. The results are shown in Table 1.

Figure 2015097991
Figure 2015097991

表1より、クロラミン化合物と界面活性剤を含むアルカリ水溶液よりなる本発明の洗浄液を用いた実施例1,2では、透過流束を汚染前の透過流束に近い状態にまで回復させることができることが分かる。これに対して、アルカリ水溶液を用いた比較例1、界面活性剤を含むアルカリ水溶液を用いた比較例2,3では、透過流束の回復率が低く、また、クロラミン化合物を含むアルカリ水溶液を用いた比較例4では、これら比較例1〜3よりも洗浄効果に優れるが、この比較例4に対して、更に界面活性剤を併用した実施例1,2ではより高い洗浄効果が得られる。   From Table 1, in Examples 1 and 2 using the cleaning liquid of the present invention comprising an aqueous alkali solution containing a chloramine compound and a surfactant, the permeation flux can be recovered to a state close to the permeation flux before contamination. I understand. In contrast, Comparative Example 1 using an aqueous alkali solution and Comparative Examples 2 and 3 using an aqueous alkali solution containing a surfactant have a low permeation flux recovery rate, and an alkaline aqueous solution containing a chloramine compound is used. In Comparative Example 4, the cleaning effect is superior to those of Comparative Examples 1 to 3, but in comparison with Comparative Example 4, Examples 1 and 2 in which a surfactant is used in combination provide a higher cleaning effect.

[実施例3、比較例5,6]
以下の洗浄液を用いて、以下に示す洗浄試験を行った。
[Example 3, Comparative Examples 5 and 6]
The following cleaning tests were performed using the following cleaning solutions.

<洗浄液>
実施例3:1M次亜塩素酸ナトリウム、1.85Mスルファミン酸、0.1Mラウリル硫酸ナトリウム及び2.8M水酸化ナトリウムを含む水溶液よりなる洗浄剤を、2%に希釈して調製したpH12.3の水溶液
比較例5:pH12.3の水酸化ナトリウム水溶液
比較例6:1M次亜塩素酸ナトリウム、1.85Mスルファミン酸及び2.8M水酸化ナトリウムを含む水溶液よりなる洗浄剤を、2%に希釈して調製したpH12.3の水溶液
<Cleaning liquid>
Example 3 A pH of 12.3 prepared by diluting an aqueous solution containing 1 M sodium hypochlorite, 1.85 M sulfamic acid, 0.1 M sodium lauryl sulfate and 2.8 M sodium hydroxide to 2%. Comparative Example 5: Sodium hydroxide aqueous solution of pH 12.3 Comparative Example 6: A detergent comprising an aqueous solution containing 1 M sodium hypochlorite, 1.85 M sulfamic acid and 2.8 M sodium hydroxide was diluted to 2% PH 12.3 prepared aqueous solution

なお、上記の実施例3及び比較例6の洗浄剤は、1Mの次亜塩素酸ナトリウムと1.85Mのスルファミン酸を含むため、Cl濃度としては1Mであり、Cl/Nモル比=1/1.85=0.54である。 Since the cleaning agents of Example 3 and Comparative Example 6 above contain 1M sodium hypochlorite and 1.85M sulfamic acid, the Cl 2 concentration is 1M, and the Cl 2 / N molar ratio = 1 / 1.85 = 0.54.

<洗浄試験>
日東電工社製芳香族ポリアミド系RO膜「ES20」を試験研究所の排水回収システムにおけるRO膜分離装置に装填し、半年間運転した。運転後のRO膜をRO膜分離装置から取り出して解体し、平膜試料を入手した。平膜試料を円形に切り取り、図1,2の平膜試験装置に設置して、まず、0.75MPa、25℃の条件で、洗浄前の純水透過流束を測定した。その後、各洗浄液を供給して実施例1におけると同様に17時間の浸漬洗浄を行い、洗浄後の純水透過流束を同条件で測定した。結果を表2に示す。
<Cleaning test>
An aromatic polyamide RO membrane “ES20” manufactured by Nitto Denko Corporation was loaded into the RO membrane separation device in the wastewater collection system of the test laboratory and operated for six months. The RO membrane after operation was taken out from the RO membrane separator and disassembled to obtain a flat membrane sample. A flat membrane sample was cut into a circle and installed in the flat membrane test apparatus shown in FIGS. 1 and 2, and first, the pure water permeation flux before washing was measured under the conditions of 0.75 MPa and 25 ° C. Thereafter, each cleaning solution was supplied and immersion cleaning was performed for 17 hours in the same manner as in Example 1, and the pure water permeation flux after cleaning was measured under the same conditions. The results are shown in Table 2.

Figure 2015097991
Figure 2015097991

表2より明らかなように、アルカリ水溶液を用いた比較例5よりもクロラミン化合物を含むアルカリ水溶液を用いた比較例6の方が洗浄効果に優れるが、更に界面活性剤を併用した実施例3では、各段に優れた洗浄効果が得られる。   As is clear from Table 2, Comparative Example 6 using an aqueous alkali solution containing a chloramine compound is superior in cleaning effect to Comparative Example 5 using an aqueous alkaline solution, but in Example 3 using a surfactant in combination, Excellent cleaning effect can be obtained at each stage.

1 容器
2 平膜セル
2A RO膜
2B 多孔質支持板
3 スターラー
4 高圧ポンプ
5 攪拌子
6 圧力計
7 圧力調整バルブ
8 Oリング
DESCRIPTION OF SYMBOLS 1 Container 2 Flat membrane cell 2A RO membrane 2B Porous support plate 3 Stirrer 4 High pressure pump 5 Stirrer 6 Pressure gauge 7 Pressure adjustment valve 8 O-ring

Claims (15)

クロラミン化合物、界面活性剤及びアルカリ剤を含むpH13以上の水溶液よりなることを特徴とする透過膜の洗浄剤。   A cleaning agent for a permeable membrane comprising an aqueous solution having a pH of 13 or more containing a chloramine compound, a surfactant and an alkali agent. 請求項1において、前記水溶液のpHが13以上15以下であることを特徴とする透過膜の洗浄剤。   The cleaning agent for a permeable membrane according to claim 1, wherein the pH of the aqueous solution is 13 or more and 15 or less. 請求項1又は2において、前記水溶液中のクロラミン化合物の濃度が0.2〜2Mで、界面活性剤の濃度が0.01〜1Mで、アルカリ剤の濃度が1〜3Mであることを特徴とする透過膜の洗浄剤。   In Claim 1 or 2, The density | concentration of the chloramine compound in the said aqueous solution is 0.2-2M, the density | concentration of surfactant is 0.01-1M, and the density | concentration of an alkaline agent is 1-3M, It is characterized by the above-mentioned. Permeable membrane cleaner. 請求項1ないし3のいずれか1項において、前記クロラミン化合物がモノクロロスルファミン酸を含むことを特徴とする透過膜の洗浄剤。   The cleaning agent for a permeable membrane according to any one of claims 1 to 3, wherein the chloramine compound contains monochlororosulmic acid. 請求項1ないし4のいずれか1項において、前記クロラミン化合物が、1級アミノ基を有する化合物、アンモニア及びアンモニウム塩よりなる群から選ばれる1種又は2種以上(以下「NH系化合物」と称す。)と、次亜塩素酸及び/又は次亜塩素酸塩とを混合することにより得られることを特徴とする透過膜の洗浄剤。 5. The chloramine compound according to claim 1, wherein the chloramine compound is selected from the group consisting of a compound having a primary amino group, ammonia and an ammonium salt (hereinafter referred to as “NH 2 -based compound”). And a hypochlorous acid and / or hypochlorite. 請求項5において、次亜塩素酸及び/又は次亜塩素酸塩と、前記NH系化合物とを、次亜塩素酸及び/又は次亜塩素酸塩由来の有効塩素濃度(Cl)と、前記NH系化合物由来の窒素原子Nとのモル比(Cl/Nモル比)が0.1〜1となるように混合することを特徴とする透過膜の洗浄剤。 In claim 5, hypochlorous acid and / or hypochlorite and the NH 2 -based compound, hypochlorous acid and / or hypochlorite-derived effective chlorine concentration (Cl 2 ), A cleaning agent for a permeable membrane, which is mixed so that a molar ratio (Cl 2 / N molar ratio) with a nitrogen atom N derived from the NH 2 -based compound is 0.1 to 1. 請求項5又は6において、アルカリ剤の水溶液に前記NH系化合物を添加して溶解し、得られたNH系化合物水溶液に次亜塩素酸及び/又は次亜塩素酸塩を添加して混合する工程を経て得られることを特徴とする透過膜の洗浄剤。 Mixture according to claim 5 or 6, and dissolved by addition of the NH 2 compound in an aqueous solution of an alkaline agent, the NH 2 compound aqueous solution obtained by adding hypochlorite and / or hypochlorite A permeable membrane cleaning agent obtained by the step of: 請求項7において、前記アルカリ剤の水溶液は、水の量が50〜90重量%であり、アルカリ剤とNH系化合物との割合がN/アルカリ金属(モル比)で0.5〜0.7となるようにNH系化合物を添加し、次亜塩素酸及び/又は次亜塩素酸塩を有効塩素(Cl)濃度5〜20重量%の水溶液として添加することを特徴とする透過膜の洗浄剤。 8. The aqueous solution of the alkali agent according to claim 7, wherein the amount of water is 50 to 90% by weight, and the ratio of the alkali agent to the NH 2 -based compound is 0.5 to 0.00 in terms of N / alkali metal (molar ratio). 7. A permeable membrane characterized in that an NH 2 -based compound is added so as to be 7, and hypochlorous acid and / or hypochlorite is added as an aqueous solution having an effective chlorine (Cl 2 ) concentration of 5 to 20% by weight. Cleaning agent. 請求項1ないし8のいずれか1項において、前記界面活性剤が分子量1000以下のアニオン系界面活性剤であることを特徴とする透過膜の洗浄剤。   The permeable membrane cleaning agent according to any one of claims 1 to 8, wherein the surfactant is an anionic surfactant having a molecular weight of 1000 or less. 請求項9において、前記アニオン系界面活性剤が、アルキルベンゼンスルホン酸塩及びアルキル硫酸塩よりなる群から選ばれる1種又は2種以上であることを特徴とする透過膜の洗浄剤。   The cleaning agent for a permeable membrane according to claim 9, wherein the anionic surfactant is one or more selected from the group consisting of alkylbenzene sulfonate and alkyl sulfate. 請求項1ないし10のいずれか1項に記載の透過膜の洗浄剤を希釈してなる、pH10以上の水溶液よりなることを特徴とする透過膜の洗浄液。   A cleaning solution for a permeable membrane comprising an aqueous solution having a pH of 10 or more obtained by diluting the permeable membrane cleaner according to any one of claims 1 to 10. クロラミン化合物、界面活性剤及びアルカリ剤を含むpH10以上の水溶液よりなることを特徴とする透過膜の洗浄液。   A cleaning solution for a permeable membrane comprising an aqueous solution having a pH of 10 or more containing a chloramine compound, a surfactant and an alkali agent. 請求項11又は12において、前記水溶液のpHが12以上13以下であることを特徴とする透過膜の洗浄液。   13. The permeable membrane cleaning solution according to claim 11, wherein the aqueous solution has a pH of 12 or more and 13 or less. 請求項11ないし13のいずれか1項において、前記水溶液中のクロラミン化合物の濃度が0.005〜0.5Mで、界面活性剤の濃度が0.0001〜0.05Mであることを特徴とする透過膜の洗浄液。   The chloramine compound concentration in the aqueous solution according to any one of claims 11 to 13 is 0.005-0.5M, and the surfactant concentration is 0.0001-0.05M. Permeation membrane cleaning solution. 請求項11ないし14のいずれか1項に記載の透過膜の洗浄液に透過膜を接触させることを特徴とする透過膜の洗浄方法。   A method for cleaning a permeable membrane, comprising bringing the permeable membrane into contact with the permeable membrane cleaning liquid according to any one of claims 11 to 14.
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WO2018168641A1 (en) * 2017-03-15 2018-09-20 栗田工業株式会社 Cleaning fluid, detergent, and cleaning method for water-contact member
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JP7136385B1 (en) * 2021-09-29 2022-09-13 栗田工業株式会社 Cleaning agent, cleaning liquid and cleaning method for aromatic polyamide reverse osmosis membrane
WO2023053504A1 (en) 2021-09-29 2023-04-06 栗田工業株式会社 Cleaning agent, cleaning liquid and cleaning method for aromatic polyamide reverse osmosis membranes

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6779706B2 (en) * 2016-08-23 2020-11-04 オルガノ株式会社 Water treatment method using reverse osmosis membrane

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56111052A (en) * 1980-02-05 1981-09-02 Tokuyama Soda Co Ltd Washing method of ion exchange membrane
JPH03115A (en) * 1989-05-12 1991-01-07 E I Du Pont De Nemours & Co Preventing reverse osmosis membrane from contamination with living thing
JP2001294895A (en) * 2000-04-13 2001-10-23 Miura Co Ltd Membrane detergent
JP2003164737A (en) * 2001-11-30 2003-06-10 Ebara Corp Washing method for separation membrane and washing apparatus adapted thereto
WO2006057311A1 (en) * 2004-11-24 2006-06-01 Maruishi Pharmaceutical Co., Ltd. Hypochlorous acid based sterilizer composition
JP2006263510A (en) * 2005-03-22 2006-10-05 Kurita Water Ind Ltd Slime preventing agent for membrane separation and membrane separation method
JP2010201312A (en) * 2009-03-02 2010-09-16 Kurita Water Ind Ltd Membrane separation method
US20120021062A1 (en) * 2006-12-29 2012-01-26 Amit Gupta Methods for the on-site production of chloramine and uses thereof
JP2013031839A (en) * 2011-07-06 2013-02-14 Mitsubishi Rayon Co Ltd Filtration membrane washing agent and method for washing filtration membrane

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56111052A (en) * 1980-02-05 1981-09-02 Tokuyama Soda Co Ltd Washing method of ion exchange membrane
JPH03115A (en) * 1989-05-12 1991-01-07 E I Du Pont De Nemours & Co Preventing reverse osmosis membrane from contamination with living thing
US4988444A (en) * 1989-05-12 1991-01-29 E. I. Du Pont De Nemours And Company Prevention of biofouling of reverse osmosis membranes
JP2001294895A (en) * 2000-04-13 2001-10-23 Miura Co Ltd Membrane detergent
JP2003164737A (en) * 2001-11-30 2003-06-10 Ebara Corp Washing method for separation membrane and washing apparatus adapted thereto
WO2006057311A1 (en) * 2004-11-24 2006-06-01 Maruishi Pharmaceutical Co., Ltd. Hypochlorous acid based sterilizer composition
JP2006263510A (en) * 2005-03-22 2006-10-05 Kurita Water Ind Ltd Slime preventing agent for membrane separation and membrane separation method
US20120021062A1 (en) * 2006-12-29 2012-01-26 Amit Gupta Methods for the on-site production of chloramine and uses thereof
JP2010201312A (en) * 2009-03-02 2010-09-16 Kurita Water Ind Ltd Membrane separation method
JP2013031839A (en) * 2011-07-06 2013-02-14 Mitsubishi Rayon Co Ltd Filtration membrane washing agent and method for washing filtration membrane

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105214506A (en) * 2015-10-23 2016-01-06 邯钢集团邯宝钢铁有限公司 The high-efficiency washing method of milipore filter in the process of Metallurgical Waste Water advanced desalination
WO2018168641A1 (en) * 2017-03-15 2018-09-20 栗田工業株式会社 Cleaning fluid, detergent, and cleaning method for water-contact member
JPWO2018168641A1 (en) * 2017-03-15 2019-03-28 栗田工業株式会社 Cleaning liquid, cleaning agent and cleaning method for wetted parts
CN110248723A (en) * 2017-03-15 2019-09-17 栗田工业株式会社 Cleaning solution, detergent and the washing methods of water contact member
CN110248723B (en) * 2017-03-15 2020-09-11 栗田工业株式会社 Cleaning liquid for water contact member, cleaning agent and cleaning method
KR20200015461A (en) 2017-05-29 2020-02-12 쿠리타 고교 가부시키가이샤 Treatment method and water treatment method of non-ionic surfactant-containing water
JP7136385B1 (en) * 2021-09-29 2022-09-13 栗田工業株式会社 Cleaning agent, cleaning liquid and cleaning method for aromatic polyamide reverse osmosis membrane
WO2023053504A1 (en) 2021-09-29 2023-04-06 栗田工業株式会社 Cleaning agent, cleaning liquid and cleaning method for aromatic polyamide reverse osmosis membranes
KR20240070500A (en) 2021-09-29 2024-05-21 쿠리타 고교 가부시키가이샤 Cleaning agent, cleaning solution and cleaning method for aromatic polyamide-based reverse osmosis membrane
CN114130204A (en) * 2021-12-11 2022-03-04 青岛沁安化工科技有限公司 Forward osmosis, reverse osmosis and nanofiltration membrane anti-attenuation medicament and preparation method thereof
CN114130204B (en) * 2021-12-11 2022-11-15 青岛沁安化工科技有限公司 Forward osmosis, reverse osmosis and nanofiltration membrane anti-attenuation medicament and preparation method thereof

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