JPH1190191A - Membrane detergent - Google Patents
Membrane detergentInfo
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- JPH1190191A JPH1190191A JP25217497A JP25217497A JPH1190191A JP H1190191 A JPH1190191 A JP H1190191A JP 25217497 A JP25217497 A JP 25217497A JP 25217497 A JP25217497 A JP 25217497A JP H1190191 A JPH1190191 A JP H1190191A
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Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、液体の濾過操作を
行う際の膜の洗浄、特に有機物によって汚染された膜の
洗浄に用いて好適な膜洗浄剤に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a membrane cleaning agent suitable for cleaning a membrane when performing a liquid filtration operation, and particularly for cleaning a membrane contaminated with organic substances.
【0002】[0002]
【従来の技術】膜の有機物汚染に関する洗浄剤として
は、アルカリ、界面活性剤、酸化剤(H2O2,NaCl
O)、酵素等が知られている(文献:「分離膜の汚染対
策と洗浄・回生技術」(水処理技術 p.43、Vo
l.33、No.2、1992)参照)。2. Description of the Related Art As a cleaning agent for organic contamination of a film, alkalis, surfactants, and oxidizing agents (H 2 O 2 , NaCl
O), enzymes and the like are known (Literature: "Countermeasures against contamination of separation membrane and washing / regeneration technology" (Water treatment technology p.43, Vo)
l. 33, no. 2, 1992)).
【0003】[0003]
【発明が解決しようとする課題】上述した洗浄剤の内、
有機物に対して優れた洗浄効果を示すのは、酸化剤や酵
素である。しかしながら、酵素は、タンパク質等の天然
由来の高分子に対しては有効であるが、高分子凝集剤や
界面活性剤などの天然高分子以外の有機物に対しては効
果がないという問題がある。また、H2O2やNaClO
等の酸化剤は、天然高分子以外の有機物、すなわち、高
分子凝集剤等の合成高分子や界面活性剤に対しても有効
であるが、ポリアミドやポリイミド系の耐酸化性の弱い
膜には使用できないという問題がある。さらに、酸化剤
は人体に対して有害であり、その取り扱いに対しては注
意を要する。SUMMARY OF THE INVENTION Among the above-mentioned cleaning agents,
Oxidizing agents and enzymes exhibit excellent cleaning effects on organic substances. However, there is a problem that the enzyme is effective for a naturally derived polymer such as a protein, but is not effective for an organic substance other than the natural polymer such as a polymer flocculant and a surfactant. In addition, H 2 O 2 or NaClO
The oxidizing agent such as is effective for organic substances other than natural polymers, that is, synthetic polymers such as polymer flocculants and surfactants, but for polyamide or polyimide-based films having weak oxidation resistance. There is a problem that it cannot be used. Furthermore, oxidizing agents are harmful to the human body and require careful handling.
【0004】本発明は、このような事情に鑑み、H2O2
やNaClO等の酸化剤と同等の洗浄効果を有し、且つ
ポリアミドやポリイミド系の膜にも使用できる安全な洗
浄剤を提供することを課題とする。[0004] In view of such circumstances, the present invention has been developed in view of H 2 O 2
An object of the present invention is to provide a safe cleaning agent which has a cleaning effect equivalent to that of an oxidizing agent such as NaClO or NaClO and can be used for a polyamide or polyimide film.
【0005】[0005]
【課題を解決するための手段】前記課題を解決する本発
明は、膜の洗浄に用いられる膜洗浄剤であって、L−ア
スコルビン酸、エリソルビン酸、及びこれらの水溶性塩
又はこれらの誘導体からなる群から選択される少なくと
も一種を含有することを特徴とする膜洗浄剤にある。Means for Solving the Problems The present invention for solving the above-mentioned problems is directed to a membrane cleaning agent used for cleaning a membrane, comprising L-ascorbic acid, erythorbic acid, and a water-soluble salt or derivative thereof. A membrane cleaning agent comprising at least one member selected from the group consisting of:
【0006】ここで、前記膜は、例えば、有機物によっ
て汚染されたものである。Here, the film is, for example, contaminated by an organic substance.
【0007】本発明の膜洗浄剤は、高分子、微粒子、微
生物、酵母、パルプ、汚泥などを含む流体の分離、精
製、濃縮、回収などに適用される膜処理プロセスにおい
て、各種有機物等に汚染された膜の洗浄に用いることが
できる。特に、高分子凝集剤による凝集プロセスを前処
理として適用する膜処理プロセスにおいて、高分子凝集
剤を含む各種有機物に汚染された膜の洗浄に好適に用い
ることができる。[0007] The membrane cleaning agent of the present invention contaminates various organic substances in a membrane treatment process applied to separation, purification, concentration, and recovery of fluids including polymers, fine particles, microorganisms, yeast, pulp, sludge, and the like. It can be used for cleaning a film that has been made. In particular, in a membrane treatment process in which an aggregation process using a polymer flocculant is applied as a pretreatment, the film can be suitably used for cleaning a film contaminated with various organic substances including a polymer flocculant.
【0008】また、本発明の洗浄剤を適用できる膜の種
類は特に限定されず、例えば、MF膜(精密濾過膜)、
UF膜(限外濾過膜)、NF膜(ナノ濾過膜)、RO
(逆浸透膜)などに適用できる。The type of membrane to which the cleaning agent of the present invention can be applied is not particularly limited, and examples thereof include MF membrane (microfiltration membrane),
UF membrane (ultrafiltration membrane), NF membrane (nanofiltration membrane), RO
(Reverse osmosis membrane).
【0009】膜の素材も特に限定されず、有機膜、特に
酸化剤に対して弱いポリイミド、ポリアミド系の膜にも
適用できる。The material of the film is not particularly limited, and it can be applied to an organic film, particularly a polyimide or polyamide film which is weak against an oxidizing agent.
【0010】本発明で用いるL−アスコルビン酸は還元
性を有する物質で食品添加物にも指定されており、安全
性の高い物質であり、エリソルビン酸は、L−アスコル
ビン酸の光学異性体である。また、これらの水溶性塩と
しては、ナトリウム塩、カルシウム塩などを挙げること
ができる。また、これらの誘導体としては、アスコルビ
ン酸もしくはエリソルビン酸のエステルが挙げられ、例
えば、アスコルビン酸ギ酸エステル、アスコルビン酸酢
酸エステル、アスコルビン酸プロピオン酸エステル、エ
ルソルビン酸ギ酸エステル、エルソルビン酸酢酸エステ
ル、及びエルソルビン酸プロピオン酸エステルが例示さ
れる。本発明では、これらを一種又は二種以上混合して
用いることができる。[0010] L-ascorbic acid used in the present invention is a substance having a reducing property and designated as a food additive, and is a highly safe substance. Erythorbic acid is an optical isomer of L-ascorbic acid . In addition, examples of these water-soluble salts include sodium salts and calcium salts. Examples of these derivatives include esters of ascorbic acid or erythorbic acid. Examples are propionates. In the present invention, these can be used alone or in combination of two or more.
【0011】本発明の膜洗浄剤は、基本的には、これら
の薬剤を水に溶解させた水溶液である。薬剤の濃度は特
に限定されないが、10ppm〜1.0%程度用いるの
が好ましい。The membrane cleaning agent of the present invention is basically an aqueous solution obtained by dissolving these agents in water. The concentration of the drug is not particularly limited, but it is preferable to use about 10 ppm to 1.0%.
【0012】また、本発明の膜洗浄剤は、本発明の有効
成分を阻害しない範囲で他の成分を含有してもよい。Further, the membrane cleaning agent of the present invention may contain other components as long as the active component of the present invention is not inhibited.
【0013】さらに、本発明の膜洗浄剤を用いた洗浄方
法も特に限定されず、他の洗浄剤を用いる場合と同様に
用いることができ、例えば、膜を膜洗浄剤中に浸漬した
後、水洗する等することにより、容易に行うことができ
る。[0013] Further, the cleaning method using the membrane cleaning agent of the present invention is not particularly limited, and can be used in the same manner as in the case of using other cleaning agents. For example, after immersing the film in the membrane cleaning agent, It can be easily performed by washing with water or the like.
【0014】本発明の洗浄剤は、L−アスコルビン酸及
びこれらの水溶性塩又はこれらの誘導体、エリソルビン
酸及びこれらの水溶性塩又はこれらの誘導体から選択さ
れる少なくとも一種を含有することにより、有機物、特
に、合成高分子化合物に汚染された膜を有効に洗浄す
る。これは、還元剤であるL−アスコルビン酸存在下で
水溶性高分子水溶液の粘度が低下することが知られてお
り(K.Uchidaら、Agric.Biol.Ch
em.,50,257(1986);青木修三、Che
mistry Express 6(12)、1017
(1991))、この作用に基づくものと推測される。
すなわち、L−アスコルビン酸存在下での水溶性高分子
溶液の低粘度化の詳細は不明であるが、アスコルビン酸
と水中の何らかの物質との相互作用によって活性酸素種
が生成し、その活性酸素種によって水溶性高分子が分解
するものと考えられる。[0014] The detergent of the present invention contains at least one selected from L-ascorbic acid and water-soluble salts or derivatives thereof, erythorbic acid and water-soluble salts or derivatives thereof, so that an organic substance can be obtained. In particular, a membrane contaminated with a synthetic polymer compound is effectively washed. It is known that the viscosity of a water-soluble polymer aqueous solution decreases in the presence of L-ascorbic acid as a reducing agent (K. Uchida et al., Agric. Biol. Ch.
em. , 50, 257 (1986); Shuzo Aoki, Che.
mystery Express 6 (12), 1017
(1991)), which is presumed to be based on this effect.
That is, although the details of lowering the viscosity of the water-soluble polymer solution in the presence of L-ascorbic acid are unknown, active oxygen species are generated by the interaction of ascorbic acid with some substance in water, and the active oxygen species is generated. It is considered that the water-soluble polymer is decomposed by this.
【0015】[0015]
【発明の実施の形態】以下本発明を実施例に基づいて説
明する。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below based on embodiments.
【0016】(実施例1)テッドエンド型撹拌式濾過試
験器(アミコン スタンダード型撹拌式セル 8400
型)にポリスルフォン系UF膜(アミコン PM10)
をセットし、純水を圧力1kg/cm2で撹拌下通水
し、純水のフラックス(水透過流束:m/D)を測定し
た。その後、濾過試験器内の純水と高分子凝集剤水溶液
(栗田工業(株)製:クリフィックスPA331 50
mg/L水溶液)とを交換し、高分子凝集剤水溶液を、
圧力1kg/cm2で撹拌下、100mL通水した。次
に、容器に残った高分子凝集剤水溶液と純水300mL
とを交換し、純水を圧力1kg/cm2で撹拌下通水
し、純水のフラックスを測定した。(Example 1) Ted end type stirring type filtration tester (Amicon standard type stirring type cell 8400)
Type) and polysulfone UF membrane (Amicon PM10)
Was set and pure water was passed under stirring at a pressure of 1 kg / cm 2 , and the flux of pure water (water flux: m / D) was measured. Thereafter, pure water and an aqueous solution of a polymer flocculant (Kurita Kogyo Co., Ltd .: Crifix PA33150) in a filtration tester are used.
mg / L aqueous solution), and the aqueous polymer flocculant aqueous solution is replaced with
100 mL of water was passed under stirring at a pressure of 1 kg / cm 2 . Next, the polymer flocculant aqueous solution remaining in the container and pure water 300 mL
And pure water was passed under stirring at a pressure of 1 kg / cm 2 , and the flux of pure water was measured.
【0017】その後、濾過試験器から膜を取り外し、膜
を100ppmのアスコルビン酸ナトリウム水溶液に一
晩浸漬した後、再び純水を圧力1kg/cm2で撹拌下
通水し、純水のフラックスを測定した。結果を表1に示
す。Thereafter, the membrane was removed from the filtration tester, and the membrane was immersed in a 100 ppm aqueous sodium ascorbate solution overnight, and then pure water was again passed under stirring at a pressure of 1 kg / cm 2 to measure the flux of pure water. did. Table 1 shows the results.
【0018】(実施例2)100ppmのアスコルビン
酸ナトリウム水溶液の代わりに、100ppmのエリソ
ルビン酸ナトリウム水溶液を用いた以外は、実施例1と
同じ操作を行った。結果を表1に示す。Example 2 The same operation as in Example 1 was performed except that a 100 ppm aqueous solution of sodium erythorbate was used instead of the 100 ppm aqueous solution of sodium ascorbate. Table 1 shows the results.
【0019】(比較例1)100ppmのアスコルビン
酸ナトリウム水溶液の代わりに、100ppmのヒドラ
ジン水溶液を用いた以外は、実施例1と同じ操作を行っ
た。結果を表1に示す。Comparative Example 1 The same operation as in Example 1 was performed except that a 100 ppm aqueous hydrazine solution was used instead of the 100 ppm sodium ascorbate aqueous solution. Table 1 shows the results.
【0020】(比較例2)100ppmのアスコルビン
酸ナトリウム水溶液の代わりに、100ppmの亜硫酸
水素ナトリウム水溶液を用いた以外は、実施例1と同じ
操作を行った。結果を表1に示す。Comparative Example 2 The same operation as in Example 1 was performed, except that a 100 ppm aqueous solution of sodium bisulfite was used instead of the 100 ppm aqueous solution of sodium ascorbate. Table 1 shows the results.
【0021】(比較例3)100ppmのアスコルビン
酸ナトリウム水溶液の代わりに、純水を用いた以外は、
実施例1と同じ操作を行った。結果を表1に示す。(Comparative Example 3) Except that pure water was used instead of the 100 ppm aqueous solution of sodium ascorbate,
The same operation as in Example 1 was performed. Table 1 shows the results.
【0022】(比較例4)100ppmのアスコルビン
酸ナトリウム水溶液の代わりに、100ppmのH2O2
水溶液を用いた以外は、実施例1と同じ操作を行った。
結果を表1に示す。(Comparative Example 4) Instead of a 100 ppm aqueous solution of sodium ascorbate, 100 ppm of H 2 O 2 was used.
The same operation as in Example 1 was performed except that the aqueous solution was used.
Table 1 shows the results.
【0023】(比較例5)100ppmのアスコルビン
酸ナトリウム水溶液の代わりに、100ppmのNaC
lO水溶液を用いた以外は、実施例1と同じ操作を行っ
た。結果を表1に示す。(Comparative Example 5) Instead of a 100 ppm aqueous solution of sodium ascorbate, 100 ppm of NaC was used.
The same operation as in Example 1 was performed except that the 10 aqueous solution was used. Table 1 shows the results.
【0024】[0024]
【表1】 [Table 1]
【0025】表1に示す結果より、アスコルビン酸ナト
リウム又はエリソルビン酸ナトリウムを用いた実施例1
及び2は、酸化剤であるH2O2又はNaClOを用いた
比較例4及び5と同等以上の洗浄効果を示した。また、
還元剤であるヒドラジン又は亜硫酸水素ナトリウムを用
いた比較例1及び2よりも優れた効果を示した。したが
って、安全性の面で格段に優れている実施例1及び2が
膜洗浄剤として好適であることが確認された。From the results shown in Table 1, it can be seen that Example 1 using sodium ascorbate or sodium erysorbate was used.
And 2 showed a cleaning effect equal to or higher than Comparative Examples 4 and 5 using H 2 O 2 or NaClO as an oxidizing agent. Also,
The effect was superior to Comparative Examples 1 and 2 using hydrazine or sodium bisulfite as a reducing agent. Therefore, it was confirmed that Examples 1 and 2, which are extremely excellent in terms of safety, are suitable as a membrane cleaning agent.
【0026】(実施例3)高分子凝集剤水溶液の代わり
に、フミン酸ナトリウム50ppm及びカオリン50p
pmを含む模擬排水に硫酸バンド(硫酸アルミニウム)
80ppm及び高分子凝集剤(栗田工業(株)製:クリ
フィックスPA331)15ppmを添加して凝集させ
たものを用いた以外は実施例1と同じ操作を行った。結
果を表2に示す。Example 3 Instead of an aqueous solution of a polymer flocculant, 50 ppm of sodium humate and 50 p of kaolin were used.
Simulated wastewater containing pm in sulfuric acid band (aluminum sulfate)
The same operation as in Example 1 was performed except that 80 ppm and 15 ppm of a polymer flocculant (manufactured by Kurita Industry Co., Ltd .: Crifix PA331) were added and flocculated. Table 2 shows the results.
【0027】(比較例6)100ppmのアスコルビン
酸ナトリウム水溶液の代わりに、純水を用いた以外は、
実施例3と同じ操作を行った。結果を表2に示す。(Comparative Example 6) Except that pure water was used instead of the 100 ppm aqueous solution of sodium ascorbate,
The same operation as in Example 3 was performed. Table 2 shows the results.
【0028】(比較例7)100ppmのアスコルビン
酸ナトリウム水溶液の代わりに、H2O2水溶液を用いた
以外は、実施例3と同じ操作を行った。結果を表2に示
す。Comparative Example 7 The same operation as in Example 3 was carried out except that an aqueous solution of H 2 O 2 was used instead of the aqueous solution of 100 ppm sodium ascorbate. Table 2 shows the results.
【0029】(比較例8)100ppmのアスコルビン
酸ナトリウム水溶液の代わりに、NaClO水溶液を用
いた以外は、実施例3と同じ操作を行った。結果を表2
に示す。Comparative Example 8 The same operation as in Example 3 was performed except that an aqueous solution of NaClO was used instead of the aqueous solution of sodium ascorbate of 100 ppm. Table 2 shows the results
Shown in
【0030】[0030]
【表2】 [Table 2]
【0031】表2に示す結果より、模擬排水を用いた系
においても、アスコルビン酸ナトリウムを用いた実施例
3が、酸化剤であるH2O2又はNaClOを用いた比較
例7及び8と同等以上の洗浄効果を示すことが確認され
た。From the results shown in Table 2, in the system using the simulated wastewater, Example 3 using sodium ascorbate was equivalent to Comparative Examples 7 and 8 using H 2 O 2 or NaClO as an oxidizing agent. It was confirmed that the above cleaning effect was exhibited.
【0032】(実施例4)デッドエンド型撹拌式濾過試
験器(ステンレス製)にポリアミド系RO膜(日東電工
製:ES10)をセットし、NaClの50ppm水溶
液を圧力10.0kg/cm2で撹拌下通水し、フラッ
クスとNaClの阻止率を測定した。Example 4 A polyamide-based RO membrane (manufactured by Nitto Denko: ES10) was set in a dead-end stirring type filtration tester (made of stainless steel), and a 50 ppm aqueous solution of NaCl was stirred at a pressure of 10.0 kg / cm 2 . Water was allowed to flow down, and the rejection of flux and NaCl was measured.
【0033】そして、濾過試験器から膜を取り外し、膜
を100ppmのアスコルビン酸ナトリウム水溶液に3
時間浸漬した後、再びNaClの50ppm水溶液を圧
力10.0kg/cm2で撹拌下通水し、NaClの阻
止率を測定した。結果を表3に示す。Then, the membrane was removed from the filtration tester, and the membrane was placed in a 100 ppm aqueous sodium ascorbate solution.
After immersion for a period of time, a 50 ppm aqueous solution of NaCl was passed again with stirring at a pressure of 10.0 kg / cm 2 , and the rejection of NaCl was measured. Table 3 shows the results.
【0034】(実施例5)100ppmのアスコルビン
酸ナトリウム水溶液の代わりに、100ppmのエリソ
ルビン酸ナトリウム水溶液を用いた以外は、実施例4と
同じ操作を行った。結果を表3に示す。Example 5 The same operation as in Example 4 was performed except that a 100 ppm aqueous solution of sodium erythorbate was used instead of the 100 ppm aqueous solution of sodium ascorbate. Table 3 shows the results.
【0035】(比較例9)100ppmのアスコルビン
酸ナトリウム水溶液の代わりに、100ppmのヒドラ
ジン水溶液を用いた以外は、実施例4と同じ操作を行っ
た。結果を表3に示す。Comparative Example 9 The same operation as in Example 4 was performed except that a 100 ppm aqueous hydrazine solution was used instead of the 100 ppm aqueous sodium ascorbate solution. Table 3 shows the results.
【0036】(比較例10)100ppmのアスコルビ
ン酸ナトリウム水溶液の代わりに、100ppmの亜硫
酸水素ナトリウム水溶液を用いた以外は、実施例4と同
じ操作を行った。結果を表3に示す。Comparative Example 10 The same operation as in Example 4 was performed except that a 100 ppm aqueous solution of sodium bisulfite was used instead of the 100 ppm aqueous solution of sodium ascorbate. Table 3 shows the results.
【0037】(比較例11)100ppmのアスコルビ
ン酸ナトリウム水溶液の代わりに、純水を用いた以外
は、実施例4と同じ操作を行った。結果を表3に示す。Comparative Example 11 The same operation as in Example 4 was performed except that pure water was used instead of the 100 ppm aqueous solution of sodium ascorbate. Table 3 shows the results.
【0038】(比較例12)100ppmのアスコルビ
ン酸ナトリウム水溶液の代わりに、100ppmのH2
O2水溶液を水溶液を用いた以外は、実施例4と同じ操
作を行った。結果を表3に示す。(Comparative Example 12) Instead of a 100 ppm aqueous solution of sodium ascorbate, 100 ppm of H2 was used.
The same operation as in Example 4 was performed except that an aqueous solution of O2 was used. Table 3 shows the results.
【0039】(比較例13)100ppmのアスコルビ
ン酸ナトリウム水溶液の代わりに、100ppmのNa
ClO水溶液を用いた以外は、実施例4と同じ操作を行
った。結果を表3に示す。(Comparative Example 13) Instead of a 100 ppm aqueous solution of sodium ascorbate, 100 ppm of sodium ascorbate was used.
The same operation as in Example 4 was performed except that an aqueous ClO solution was used. Table 3 shows the results.
【0040】[0040]
【表3】 [Table 3]
【0041】表3に示す結果より、H2O2又はNaCl
Oを用いた比較例12及び13、特にNaClOを用い
た比較例13では薬剤による膜の劣化のため、NaCl
阻止率が低下したが、アスコルビン酸ナトリウム又はエ
リソルビン酸ナトリウムを用いた実施例4及び5では、
膜への影響は観察されなかった。From the results shown in Table 3, H 2 O 2 or NaCl
In Comparative Examples 12 and 13 using O, particularly in Comparative Example 13 using NaClO, NaCl was used to deteriorate the film.
Although the rejection rate decreased, in Examples 4 and 5 using sodium ascorbate or sodium erythorbate,
No effect on the membrane was observed.
【0042】(実施例6)純水を圧力4kg/cm2、
水量10L/minでポリスルフォン系UF膜(日東電
工製:NTU−3020)に通水し、30分通水後のフ
ラックスを測定した。モジュールは長さ500mmで、
直径が11.5mmの2本入り管型である。Example 6 Pure water was applied at a pressure of 4 kg / cm 2 ,
Water was passed through a polysulfone-based UF membrane (NTU-3020 manufactured by Nitto Denko) at a water flow rate of 10 L / min, and the flux after 30 minutes of water flow was measured. The module is 500mm long,
It is a two-tube type with a diameter of 11.5 mm.
【0043】次いで、表4に示す水質の下水二次処理水
にPAC(ポリ塩化アルミニウム)10mg/Lを添加
して懸濁物質を凝結させた液を圧力4kg/cm2、水
量10L/minにて1週間通水し、再び純水を圧力4
kg/cm2、水量10L/minで通水し、30分通
水後のフラックスを測定した。Next, 10 mg / L of PAC (polyaluminum chloride) was added to the sewage secondary treatment water having the water quality shown in Table 4 to condense the suspended solid to a pressure of 4 kg / cm 2 and a water volume of 10 L / min. Water for one week, and then apply pure water again at a pressure of 4
Water was passed at a flow rate of 10 L / min at a flow rate of 10 kg / cm 2 , and the flux after 30 minutes of water flow was measured.
【0044】その後、この膜をアスコルビン酸Na20
0mg/L水溶液に20時間接触させ、再び純水のフラ
ックスを先と同じ条件で測定した。結果を表5に示す。Thereafter, this membrane was coated with Na20 ascorbate.
It was brought into contact with a 0 mg / L aqueous solution for 20 hours, and the flux of pure water was measured again under the same conditions as above. Table 5 shows the results.
【0045】(実施例7)200ppmのアスコルビン
酸ナトリウム水溶液の代わりに、200ppmのエリソ
ルビン酸Na水溶液を用いた以外は、実施例4と同じ操
作を行った。結果を表5に示す。Example 7 The same operation as in Example 4 was performed, except that a 200 ppm aqueous solution of sodium erythorbate was used instead of the 200 ppm aqueous solution of sodium ascorbate. Table 5 shows the results.
【0046】(比較例14)200ppmのアスコルビ
ン酸ナトリウム水溶液の代わりに、100ppmの亜硫
酸水素ナトリウム水溶液を用いた以外は、実施例6と同
じ操作を行った。結果を表5に示す。Comparative Example 14 The same operation as in Example 6 was performed, except that a 100 ppm aqueous solution of sodium bisulfite was used instead of the 200 ppm aqueous solution of sodium ascorbate. Table 5 shows the results.
【0047】(比較例15)200ppmのアスコルビ
ン酸ナトリウム水溶液の代わりに、200ppmのNa
ClO水溶液を用いた以外は、実施例6と同じ操作を行
った。結果を表5に示す。(Comparative Example 15) Instead of a 200 ppm sodium ascorbate aqueous solution, 200 ppm Na ascorbate was used.
The same operation as in Example 6 was performed except that an aqueous ClO solution was used. Table 5 shows the results.
【0048】[0048]
【表4】 [Table 4]
【0049】[0049]
【表5】 [Table 5]
【0050】表5に示す結果より、下水二次処理水を用
いた系においても、アスコルビン酸ナトリウム又はエリ
ソルビン酸ナトリウムを用いた実施例6及び7が、酸化
剤であるNaClOを用いた比較例15と同等の洗浄効
果を示すことが確認された。From the results shown in Table 5, even in the system using the sewage secondary treatment water, Examples 6 and 7 using sodium ascorbate or sodium erysorbate were compared with Comparative Example 15 using NaClO as an oxidizing agent. It was confirmed that the same cleaning effect was obtained.
【0051】(実施例8)純水を圧力1.0kg/cm
2、水量2.0L/minでポリオレフィン系MO膜
(日東電工製:孔径0.4μm)に通水し、30分通水
後のフラックスを測定した。モジュールは膜面積64c
m2の平膜である。次いで、濃度12%の菌体培養液を
ポリビニルアミジン(クリフィックスCP111)20
00mg/L、ポリアクリル酸(クリフロックPA32
2)1000mg/Lで凝集処理させたものを100メ
ッシュの濾布を透過させ、透過液を、圧力1.0kg/
cm2、水量2.0L/minにて4時間通水し、再び
純水を圧力1kg/cm2、水量2.0L/minで通
水し、30分通水後のフラックスを測定した。Example 8 Pure water was applied at a pressure of 1.0 kg / cm.
2. Water was passed through a polyolefin-based MO membrane (manufactured by Nitto Denko: pore size 0.4 μm) at a water flow rate of 2.0 L / min, and the flux after 30 minutes of water flow was measured. Module has a membrane area of 64c
m 2 flat membrane. Next, a cell culture solution having a concentration of 12% was added to polyvinylamidine (Crifix CP111) 20
00mg / L, polyacrylic acid (Cliffloc PA32
2) What was agglomerated at 1000 mg / L was passed through a 100-mesh filter cloth, and the permeated liquid was pressured at 1.0 kg / L.
cm 2, and 4 hours water passage at water 2.0L / min, the pure water pressure 1 kg / cm 2, and passed water at water 2.0L / min again to measure the flux after 30 minutes through the water.
【0052】その後、この膜をアスコルビン酸ナトリウ
ム500mg/L水溶液に20時間以上接触させ、再
び、純水のフラックスを先と同じ条件で測定した。結果
を表6に示す。Thereafter, this membrane was brought into contact with a 500 mg / L aqueous solution of sodium ascorbate for 20 hours or more, and the flux of pure water was measured again under the same conditions as above. Table 6 shows the results.
【0053】(比較例16)500ppmのアスコルビ
ン酸ナトリウム水溶液の代わりに、500ppmの亜硫
酸水素ナトリウム水溶液を用いた以外は、実施例8と同
じ操作を行った。結果を表6に示す。Comparative Example 16 The same operation as in Example 8 was performed except that a 500 ppm aqueous solution of sodium bisulfite was used instead of the 500 ppm aqueous solution of sodium ascorbate. Table 6 shows the results.
【0054】(比較例17)500ppmのアスコルビ
ン酸ナトリウム水溶液の代わりに、200ppmのNa
ClO水溶液を用いた以外は、実施例8と同じ操作を行
った。結果を表6に示す。(Comparative Example 17) Instead of a 500 ppm sodium ascorbate aqueous solution, 200 ppm Na ascorbate was used.
The same operation as in Example 8 was performed except that an aqueous ClO solution was used. Table 6 shows the results.
【0055】[0055]
【表6】 [Table 6]
【0056】表6に示す結果より、培養液通水を行った
系においても、アスコルビン酸ナトリウムを用いた実施
例8が、酸化剤であるNaClOを用いた比較例17と
同等の洗浄効果を示すことが確認された。From the results shown in Table 6, even in the system in which the culture solution was passed, the cleaning effect of Example 8 using sodium ascorbate was equivalent to that of Comparative Example 17 using NaClO as an oxidizing agent. It was confirmed that.
【0057】(実施例9)図1に示すように、排水を、
凝集槽1、生物濾過膜2,UF膜3およびRO膜4によ
り順次処理する処理フローにおいて、金属加工工場の排
水を、圧力15kg/cm、水量10L/Dにて、ポリ
アミド系RO膜4(栗田工業(株)製:KROA−21
22;純水の標準透過水量は1.0m/Dである)に通
水した。定期的に水フラッシングや界面活性剤を用いた
洗浄剤での洗浄を実施しながら、2000時間運転し
た。この結果、フラックスは、1.0m/Dであったも
のが、0.4m/Dまで低下した。(Embodiment 9) As shown in FIG.
In a processing flow in which the coagulation tank 1, the biological filtration membrane 2, the UF membrane 3 and the RO membrane 4 are sequentially processed, the wastewater from the metal processing plant is subjected to a polyamide RO membrane 4 (Kurita) at a pressure of 15 kg / cm and a water volume of 10 L / D. Industrial Co., Ltd .: KROA-21
22; the standard amount of pure water permeated is 1.0 m / D). The operation was performed for 2000 hours while periodically performing water flushing and cleaning with a detergent using a surfactant. As a result, the flux decreased from 1.0 m / D to 0.4 m / D.
【0058】この汚染されたRO膜を、濃度200pp
mのアスコルビン酸ナトリウム溶液に10時間接触させ
た。その後、純水を圧力10kg/cm2、水量10L
/minにて1時間通水し、フラックスを測定した。こ
の結果を表7に示す。The contaminated RO film was treated at a concentration of 200 pp.
m of sodium ascorbate solution for 10 hours. Then, pure water is supplied at a pressure of 10 kg / cm 2 and a water volume of 10 L.
/ Min. For 1 hour, and the flux was measured. Table 7 shows the results.
【0059】(比較例18)汚染されたRO膜を、濃度
200ppmのアスコルビン酸ナトリウム溶液に接触さ
せる代わりに、純水に10時間接触させた以外は、実施
例9と同様の操作を行った。この結果を表7に示す。Comparative Example 18 The same operation as in Example 9 was performed, except that the contaminated RO film was contacted with pure water for 10 hours instead of being brought into contact with a 200 ppm concentration of sodium ascorbate solution. Table 7 shows the results.
【0060】(比較例19)汚染されたRO膜を、濃度
200ppmのアスコルビン酸ナトリウム溶液に接触さ
せる代わりに、0.1%ヒドラジン及び0.3%ドデシ
ルベンゼンスルフォン酸ナトリウム(pH9.0)溶液
に10時間接触させた以外は、実施例9と同様の操作を
行った。この結果を表7に示す。Comparative Example 19 Instead of contacting a contaminated RO membrane with a 200 ppm sodium ascorbate solution, a 0.1% hydrazine and 0.3% sodium dodecylbenzenesulfonate (pH 9.0) solution was used. The same operation as in Example 9 was performed except that the contact was performed for 10 hours. Table 7 shows the results.
【0061】[0061]
【表7】 [Table 7]
【0062】表7に示す結果より、金属加工工場排水を
用いた系においても、アスコルビン酸ナトリウムを用い
た実施例9が、ヒドラジン及びドデシルベンジルスルフ
ォン酸ナトリウムを用いた比較例19より高い洗浄効果
を示すことが確認された。From the results shown in Table 7, even in the system using the wastewater from the metalworking plant, the cleaning effect of Example 9 using sodium ascorbate was higher than that of Comparative Example 19 using hydrazine and sodium dodecylbenzylsulfonate. Was confirmed.
【0063】[0063]
【発明の効果】以上、実施例と共に説明したように、ア
スコルビン酸及びエルソルビン酸又はこれらの水溶性塩
又はこれらの誘導体を含有する本発明の膜洗浄剤は、各
種有機物で汚染された膜に対しても酸化剤と同等の膜洗
浄効果を示し、酸化剤で劣化してしまうポリアミド系の
膜に対しても用いることができ、安全性の高いものであ
る。As described above, the membrane cleaning agent of the present invention containing ascorbic acid and ersorbic acid or a water-soluble salt thereof or a derivative thereof, as described above with reference to the examples, can be used for a film contaminated with various organic substances. However, it exhibits the same film cleaning effect as an oxidizing agent, and can be used for a polyamide-based film which is degraded by the oxidizing agent, and has high safety.
【図1】本発明の実施例9に用いた処理フローを示す図
である。FIG. 1 is a diagram showing a processing flow used in Embodiment 9 of the present invention.
1 凝集槽 2 生物濾過膜 3 UF膜 4 RO膜 DESCRIPTION OF SYMBOLS 1 Coagulation tank 2 Biological filtration membrane 3 UF membrane 4 RO membrane
Claims (2)
て、L−アスコルビン酸、エリソルビン酸、及びこれら
の水溶性塩又はこれらの誘導体からなる群から選択され
る少なくとも一種を含有することを特徴とする膜洗浄
剤。1. A membrane cleaning agent used for cleaning a membrane, comprising at least one selected from the group consisting of L-ascorbic acid, erythorbic acid, a water-soluble salt thereof, and a derivative thereof. Characterized membrane cleaning agent.
って汚染されたものであることを特徴とする膜洗浄剤。2. The film cleaning agent according to claim 1, wherein the film is contaminated by an organic substance.
Priority Applications (1)
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JP25217497A JPH1190191A (en) | 1997-09-17 | 1997-09-17 | Membrane detergent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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JP25217497A JPH1190191A (en) | 1997-09-17 | 1997-09-17 | Membrane detergent |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH1190191A true JPH1190191A (en) | 1999-04-06 |
Family
ID=17233531
Family Applications (1)
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---|---|---|---|
JP25217497A Pending JPH1190191A (en) | 1997-09-17 | 1997-09-17 | Membrane detergent |
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Country | Link |
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JP (1) | JPH1190191A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001083293A (en) * | 1999-09-16 | 2001-03-30 | Hitachi Ltd | Method for washing pleated filter |
-
1997
- 1997-09-17 JP JP25217497A patent/JPH1190191A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001083293A (en) * | 1999-09-16 | 2001-03-30 | Hitachi Ltd | Method for washing pleated filter |
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