TW201902563A - Cleaning fluid, detergent, and cleaning method for water-contact member - Google Patents

Cleaning fluid, detergent, and cleaning method for water-contact member Download PDF

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TW201902563A
TW201902563A TW107108541A TW107108541A TW201902563A TW 201902563 A TW201902563 A TW 201902563A TW 107108541 A TW107108541 A TW 107108541A TW 107108541 A TW107108541 A TW 107108541A TW 201902563 A TW201902563 A TW 201902563A
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chlorine
detergent
water
compound
cleaning
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TW107108541A
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TWI734898B (en
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岩見貴子
川勝孝博
田中愛理
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日商栗田工業股份有限公司
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D65/00Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B01D65/02Membrane cleaning or sterilisation ; Membrane regeneration
    • B01D65/06Membrane cleaning or sterilisation ; Membrane regeneration with special washing compositions
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D17/00Detergent materials or soaps characterised by their shape or physical properties
    • C11D17/08Liquid soap, e.g. for dispensers; capsuled
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D7/00Compositions of detergents based essentially on non-surface-active compounds
    • C11D7/02Inorganic compounds
    • C11D7/04Water-soluble compounds
    • C11D7/08Acids
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D7/00Compositions of detergents based essentially on non-surface-active compounds
    • C11D7/02Inorganic compounds
    • C11D7/04Water-soluble compounds
    • C11D7/10Salts

Abstract

A cleaning fluid and detergent for water-contact members which both contain free chlorine and a combined-chlorine compound, wherein the molar ratio of the total chlorine (Cl2) to the nitrogen atoms N derived from the combined-chlorine compound, Cl2/N, is 1 or higher, the cleaning fluid having a pH of 9 or higher and the detergent having a pH of 12 or higher. The cleaning fluid can be prepared by diluting the detergent with water. Also provided is a cleaning method for water-contact members which comprises using the cleaning fluid to clean a water-contact member.

Description

接水構件的洗淨液、洗淨劑及洗淨方法Washing liquid for water receiving member, detergent and washing method

本發明係有關洗淨UF膜(超過濾膜)、MF膜(精密過濾膜)、過濾器、配管、壓力計、流量計等之接水構件的洗淨液、洗淨劑及洗淨方法。The present invention relates to a cleaning liquid, a detergent, and a cleaning method for cleaning a water receiving member such as a UF film (ultrafiltration membrane), an MF membrane (precision filtration membrane), a filter, a pipe, a pressure gauge, and a flow meter.

使用UF膜或MF膜之膜分離裝置(除濁膜裝置)中,分離膜會附著汙垢,因此一般係每隔30秒~60分鐘間歇性供給洗淨流體(水及/或氣體)進行膜之物理洗淨。In the membrane separation device (the membrane removal device) using the UF membrane or the MF membrane, since the separation membrane adheres to the scale, the cleaning fluid (water and/or gas) is intermittently supplied for every 30 seconds to 60 minutes. Physically washed.

但既使此物理洗淨後仍會有無法去除之污垢堆積於膜上,而逐步降低膜之過濾能力。However, even after the physical cleaning, there is still unremovable dirt accumulated on the membrane, and the filtration capacity of the membrane is gradually reduced.

故需定期或不定期使用藥品以藥品洗淨除濁膜裝置。Therefore, it is necessary to use the medicines regularly or irregularly to clean the turbid film device.

專利文獻1曾記載藉由結合氯劑洗淨易氧化劣化之膜。專利文獻1又記載,所添加之洗淨劑中氯胺化合物濃度0.005~0.5M,有效氯(Cl2) 與來自氯胺化合物之氮原子N的莫耳比(Cl2 /N)為0.1~1。因此專利文獻1之洗淨方法中,係以幾乎不存在游離氯之條件洗淨膜。Patent Document 1 describes that a film which is easily oxidized and deteriorated is washed by a chlorine-binding agent. Further, Patent Document 1 discloses that the concentration of the chloramine compound in the detergent to be added is 0.005 to 0.5 M, and the molar ratio (Cl 2 /N) of the available chlorine (Cl 2 ) to the nitrogen atom N derived from the chloramine compound is 0.1 to 1. Therefore, in the cleaning method of Patent Document 1, the film is washed under the condition that there is almost no free chlorine.

專利文獻2曾記載使用Cl2 /N大於1之結合氯劑,進行冷卻水系、排水處理水系、紙漿水系之殺菌。專利文獻2又記載殺菌處理時之游離氯濃度為0.05mg/L以上。專利文獻2未記載選擇性透過膜之洗淨劑之用途。Patent Document 2 describes the sterilization of a cooling water system, a drainage water system, and a pulp water system using a combined chlorine agent having a Cl 2 /N ratio of 1. Patent Document 2 also discloses that the concentration of free chlorine in the sterilization treatment is 0.05 mg/L or more. Patent Document 2 does not describe the use of a detergent for selectively permeable membranes.

[專利文獻1]特開2015-97991號公報   [專利文獻2]特開2009-195823號公報[Patent Document 1] JP-A-2009-195913 (Patent Document 2) JP-A-2009-195823

本發明目的為,提供洗淨效果較高之洗淨液、洗淨劑及洗淨方法。An object of the present invention is to provide a cleaning liquid, a detergent, and a cleaning method which have a high cleaning effect.

本發明之要旨如下述。The gist of the present invention is as follows.

本發明之接水構件的洗淨液為,含有游離氯與氯胺化合物之洗淨液中,全氯與來自氯胺化合物之氮原子N的莫耳比(Cl2 /N)為1以上,pH為9以上。In the cleaning liquid for the water-receiving member of the present invention, the molar ratio (Cl 2 /N) of the total chlorine to the nitrogen atom N derived from the chloramine compound is 1 or more in the cleaning liquid containing the free chlorine and the chloramine compound. The pH is 9 or more.

本發明之洗淨液一態樣中,前述氯胺化合物為含有結合氯型磺胺酸及其鹽中所選出之至少一種磺胺酸系化合物。In one aspect of the cleaning solution of the present invention, the chloramine compound is at least one sulfanilic acid compound selected from the group consisting of a combined chlorosulfonic acid and a salt thereof.

本發明之洗淨液一態樣中,前述接水構件為MF膜、UF膜、過濾器、配管、壓力計及流量計中至少一種。In one aspect of the cleaning solution of the present invention, the water receiving member is at least one of an MF membrane, a UF membrane, a filter, a pipe, a pressure gauge, and a flow meter.

本發明之洗淨液一態樣中,洗淨液之pH為11以上。In the aspect of the washing liquid of the present invention, the pH of the washing liquid is 11 or more.

本發明之洗淨液一態樣中,氯胺化合物與氯之化合型氯濃度為100mg/L以上,游離氯濃度為20mg/L以上。In the washing liquid of the present invention, the chlorine concentration of the chloramine compound and chlorine is 100 mg/L or more, and the free chlorine concentration is 20 mg/L or more.

本發明之接水構件的洗淨劑為,含有游離氯與氯胺化合物之洗淨劑中,全氯與來自氯胺化合物之氮原子N的莫耳比(Cl2 /N)為1以上,pH為12以上。The detergent for the water-receiving member of the present invention is a detergent containing free chlorine and a chloramine compound, wherein the molar ratio (Cl 2 /N) of the total chlorine to the nitrogen atom N derived from the chloramine compound is 1 or more. The pH is 12 or more.

本發明之洗淨劑一態樣中,前述氯胺化合物為含有結合氯型磺胺酸及其鹽中所選出之至少一種磺胺酸系化合物。In one aspect of the detergent of the present invention, the chloramine compound is at least one sulfanilic acid compound selected from the group consisting of a combined chlorine sulfamic acid and a salt thereof.

本發明之洗淨劑一態樣中,其係藉由混合磺胺酸與鹼劑後,添加氯劑而生成結合氯化合物所得。In one aspect of the detergent of the present invention, it is obtained by mixing a sulfamic acid with an alkali agent and then adding a chlorine agent to form a bound chlorine compound.

本發明之洗淨劑一態樣中,相對於最終之洗淨劑重量的磺胺酸濃度為5質量%以下。In one aspect of the detergent of the present invention, the concentration of the sulfaic acid relative to the weight of the final detergent is 5% by mass or less.

本發明之洗淨劑一態樣中,前述接水構件為MF膜、UF膜、過濾器、配管、壓力計及流量計中至少一種。In one aspect of the detergent according to the present invention, the water receiving member is at least one of an MF membrane, a UF membrane, a filter, a pipe, a pressure gauge, and a flow meter.

本發明之接水構件的洗淨液為,以水稀釋上述本發明之洗淨劑所得。The washing liquid of the water receiving member of the present invention is obtained by diluting the above-described detergent of the present invention with water.

本發明之接水構件的洗淨方法為,使用本發明之洗淨液洗淨接水構件。 [發明之效果]In the method of cleaning the water receiving member of the present invention, the water receiving member is washed using the cleaning liquid of the present invention. [Effects of the Invention]

本發明之接水構件的洗淨液,洗淨劑及洗淨方法為,同時持有游離氯劑之強氧化力,與結合氯劑(氯胺化合物)相對於接水構件內部的強浸透力。因此比較結合氯劑時具有即效性,比較游離氯劑時具有較高洗淨效果。又,本發明之洗淨液及洗淨劑也具有優良殺菌效果。The washing liquid, the detergent and the washing method of the water-receiving member of the present invention have the strong oxidizing power of the free chlorine agent and the strong osmosis force of the combined chlorine agent (chloramine compound) with respect to the inside of the water-receiving member. . Therefore, it is more effective when compared with the chlorine agent, and has a higher washing effect when compared with the free chlorine agent. Further, the cleaning liquid and the detergent of the present invention also have an excellent bactericidal effect.

下面將詳細說明本發明之實施型態。The embodiment of the present invention will be described in detail below.

本發明係有關洗淨液、洗淨劑及洗淨方法之發明,但本發明中「洗淨液」與「洗淨劑」係如下述區別之物。   本發明之洗淨液係指,洗淨時所使用之液體。又,本發明之洗淨劑係指流通時所使用之製品。依情形可直接以洗淨劑作為洗淨液以供給洗淨,但一般係以水等稀釋洗淨劑後作為洗淨液使用於洗淨。The present invention relates to a cleaning liquid, a detergent, and a washing method. However, in the present invention, the "washing liquid" and the "cleaning agent" are the following differences. The washing liquid of the present invention means a liquid used for washing. Further, the detergent of the present invention means a product used at the time of circulation. In some cases, the detergent may be directly used as a washing liquid to be washed. However, the detergent is usually diluted with water or the like and used as a washing liquid for washing.

本發明之洗淨液為,含有游離氯與結合氯化合物。本發明之洗淨液為,全氯(Cl2 )與來自結合氯化合物之氮原子N的莫耳比(Cl2 /N)為1以上,pH為9以上。The cleaning solution of the present invention contains free chlorine and a combined chlorine compound. In the cleaning liquid of the present invention, the molar ratio (Cl 2 /N) of the perchlorine (Cl 2 ) to the nitrogen atom N derived from the combined chlorine compound is 1 or more, and the pH is 9 or more.

本發明之洗淨液較佳為,全氯濃度5,000mg-Cl2 /L以下,更佳為200~5,000mg-Cl2 /L,特佳為1,000~2,000mg-Cl2 /L,結合氯濃度100mg-Cl2 /L以上,更佳為100~4,980mg-Cl2 /L,特佳為300~1,980mg-Cl2 /L,游離氯濃度為20mg-Cl2 /L以上,更佳為20~4,900mg-Cl2 /L,特佳為20~1,700mg-Cl2 /L。Cleaning solution of the present invention is preferably, all the chlorine concentration of 5,000mg-Cl 2 / L or less, more preferably 200 ~ 5,000mg-Cl 2 / L , particularly preferably 1,000 ~ 2,000mg-Cl 2 / L , combined chlorine The concentration is 100 mg-Cl 2 /L or more, more preferably 100 to 4,980 mg-Cl 2 /L, particularly preferably 300 to 1,980 mg-Cl 2 /L, and the free chlorine concentration is 20 mg-Cl 2 /L or more, more preferably 20 to 4,900 mg-Cl 2 /L, particularly preferably 20 to 1,700 mg-Cl 2 /L.

本發明之洗淨劑為,含有游離氯與氯胺化合物之洗淨劑中,全氯(Cl2 )與來自氯胺化合物之氮原子N的莫耳比(Cl2 /N)為1以上,pH為12以上。In the detergent containing the free chlorine and the chloramine compound, the molar ratio (Cl 2 /N) of the total chlorine (Cl 2 ) to the nitrogen atom N derived from the chloramine compound is 1 or more. The pH is 12 or more.

本發明之洗淨劑中,全氯濃度(Cl2 換算濃度)較佳為10質量%以下,更佳為1~8質量%,特佳為3~8質量%。結合氯濃度(Cl2 換算濃度)為0.1質量%以上,更佳為0.5~3質量%,特佳為1~2.8質量%,游離氯濃度(Cl2 換算濃度)為0.02質量%以上,更佳為0.1~10質量%,特佳為1~5質量%。In the detergent of the present invention, the total chlorine concentration (concentration in terms of Cl 2 ) is preferably 10% by mass or less, more preferably 1 to 8% by mass, particularly preferably 3 to 8% by mass. The combined chlorine concentration (concentration in terms of Cl 2 ) is 0.1% by mass or more, more preferably 0.5 to 3% by mass, particularly preferably 1 to 2.8% by mass, and the free chlorine concentration (concentration in terms of Cl 2 ) is 0.02% by mass or more, more preferably It is 0.1 to 10% by mass, particularly preferably 1 to 5% by mass.

本發明中全氯濃度及游離氯濃度係藉由JIS K 0400-33-10:1999所規定之DPD法測定。又,結合氯濃度係由,由前述求取之全氯濃度扣除游離氯濃度所得。The total chlorine concentration and the free chlorine concentration in the present invention are measured by the DPD method prescribed in JIS K 0400-33-10:1999. Further, the combined chlorine concentration is obtained by subtracting the free chlorine concentration from the above-mentioned total chlorine concentration.

本發明可於鹼條件下使氯系洗淨液及洗淨劑適用於接水構件。本發明中除了鹼條件下藉由洗淨所得的有機物之剝離作用及加水分解作用外,可相乘附加藉由結合氯化合物之有機物分解作用,與藉由游離氯之即效性殺菌洗淨效果。因此藉由本發明可提高鹼洗淨效果,充分回復被污染之選擇性透過膜及過濾器等之性能。In the present invention, a chlorine-based cleaning solution and a detergent can be applied to a water-receiving member under alkali conditions. In the present invention, in addition to the exfoliation and hydrolysis of the organic substance obtained by the washing under the alkali condition, the decomposition of the organic substance by the combined chlorine compound and the effect of the sterilization by the free chlorine can be multiplied. . Therefore, according to the present invention, the alkali washing effect can be improved, and the performance of the contaminated selectively permeable membrane and the filter can be sufficiently recovered.

<接水構件>   接水構件如UF膜、MF膜、過濾器、配管、壓力計、流量計等,但非限定於此等。過濾器如,使用砂、無烟煤等粒狀濾材之物。   本發明以MF膜及UF膜為洗淨對象時,可有效發揮其洗淨效果。但選擇性透過膜非限於此等,本發明也適用於其他選擇性透過膜,且其膜素材無限定。又,膜之形式等無任何限制,本發明可有效適用於洗淨領域幅廣之水處理用選擇性透過膜。<Water-receiving member> The water-receiving member is, for example, a UF film, an MF film, a filter, a pipe, a pressure gauge, a flow meter, or the like, but is not limited thereto. For the filter, for example, a granular filter material such as sand or anthracite is used. In the present invention, when the MF film and the UF film are used for cleaning, the cleaning effect can be effectively exhibited. However, the selective permeable membrane is not limited thereto, and the present invention is also applicable to other selectively permeable membranes, and the membrane material is not limited. Further, the form of the film and the like are not limited, and the present invention can be effectively applied to a selective permeable membrane for water treatment in a wide range of washing applications.

<游離氯>   游離氯係使用次氯酸及/或次氯酸鹽。次氯酸鹽可使用次氯酸鈉等之次氯酸的鹼金屬鹽、次氯酸鈣等之次氯酸的鹼土類金屬鹽等。此等可單獨使用一種、或二種以上混合使用。<Free chlorine> The free chlorine system uses hypochlorous acid and/or hypochlorite. As the hypochlorite, an alkali metal salt of hypochlorous acid such as sodium hypochlorite or an alkaline earth metal salt of hypochlorous acid such as calcium hypochlorite can be used. These may be used alone or in combination of two or more.

<結合氯化合物>   結合氯化合物較佳為,如下述反應式(1)、(2)所示之反應般使次氯酸(HOCl)與具有一級胺基之化合物(XNH2 )反應所得的胺基之氫原子被氯原子取代之化合物(XNHCl)。此化合物因氧化作用較弱,故既使耐氯性較低之芳香族聚醯胺系RO膜也可作為洗淨液及洗淨劑用,又,即使相對於多糖類般黏度較高之污染物,也可浸透而於內部發揮分解作用。 <Bound Chloride Compound> The bound chlorine compound is preferably an amine obtained by reacting hypochlorous acid (HOCl) with a compound having a primary amine group (XNH 2 ) as shown in the following reaction formulas (1) and (2). A compound (XNHCl) in which a hydrogen atom is replaced by a chlorine atom. Since this compound is weak in oxidation, the aromatic polyamine-based RO membrane having low chlorine resistance can also be used as a cleaning liquid and a detergent, and even if it has a higher viscosity than a polysaccharide. The substance can also be impregnated and exert a decomposition inside.

本發明中結合氯化合物較佳為,藉由混合具有一級胺基之化合物、氨及銨鹽中任一種(以下將此等稱為「NH2 系化合物」),與次氯酸及/或次氯酸鹽而生成。具有一級胺基之化合物如,脂肪族胺、芳香族胺、磺胺酸、對胺基苯磺酸、胺磺醯苯甲酸、胺基酸等。又,銨鹽如,氯化銨、硫酸銨等。此等可單獨使用一種,或二種以上混合使用。此等NH2 系化合物中又以磺胺酸(NH2 SO2 OH)為佳。使用磺胺酸生成單氯磺醯胺時可得安定之結合氯化合物。磺胺酸因不含碳故不會增加洗淨劑之TOC值。併用磺胺酸與鹼劑可得非常有效之洗淨液及洗淨劑。In the present invention, it is preferred to incorporate a chlorine compound by mixing any one of a compound having a primary amine group, ammonia, and an ammonium salt (hereinafter referred to as "NH 2 -based compound"), and hypochlorous acid and/or Produced by chlorate. A compound having a primary amine group such as an aliphatic amine, an aromatic amine, a sulfanilic acid, a p-aminobenzenesulfonic acid, an amidoxime benzoic acid, an amino acid or the like. Further, the ammonium salt is, for example, ammonium chloride or ammonium sulfate. These may be used alone or in combination of two or more. Among these NH 2 -based compounds, sulfamic acid (NH 2 SO 2 OH) is preferred. When a sulfanilic acid is used to form monochlorosulfonamide, a stable combined chlorine compound can be obtained. Sulfamic acid does not increase the TOC value of the detergent because it does not contain carbon. A very effective cleaning solution and detergent can be obtained by using sulfamic acid and an alkali agent.

與NH2 系化合物反應之次氯酸鹽可使用次氯酸鈉等之次氯酸的鹼金屬鹽、次氯酸鈣等之次氯酸的鹼土類金屬鹽等。此等可單獨使用一種,或二種以上混合使用。   形成結合氯之具有氮原子的化合物係使用磺胺酸時,相對於最終洗淨劑之重量,磺胺酸所使用的重量濃度較佳為5質量%以下。磺胺酸之濃度大於5質量%時易使氯分解。As the hypochlorite to be reacted with the NH 2 -based compound, an alkali metal salt of hypochlorous acid such as sodium hypochlorite or an alkaline earth metal salt of hypochlorous acid such as calcium hypochlorite can be used. These may be used alone or in combination of two or more. When a sulfamic acid is used as the compound having a nitrogen atom in combination with chlorine, the weight concentration of the sulfamic acid used is preferably 5% by mass or less based on the weight of the final detergent. When the concentration of sulfamic acid is more than 5% by mass, chlorine is easily decomposed.

<游離氯與結合氯化合物之比例>   本發明中來自游離氯之有效氯(Cl2 )與來自結合氯化合物之氮原子N的莫耳比(Cl2 /N莫耳比)為1以上,較佳為1~10,特佳為1~5。藉由此範圍可得良好的游離氯之即效性洗淨作用與結合氯化合物之浸透性洗淨作用的平衡性。<Ratio of free chlorine and bound chlorine compound> In the present invention, the molar ratio (Cl 2 /N molar ratio) of the available chlorine (Cl 2 ) derived from free chlorine to the nitrogen atom N derived from the bound chlorine compound is 1 or more. Good for 1 to 10, especially for 1 to 5. By this range, a good balance between the immediate cleaning effect of free chlorine and the permeation cleaning action of the combined chlorine compound can be obtained.

<pH>   本發明之洗淨液係由含有游離氯及結合氯化合物之鹼水溶液所形成,且pH為9以上。洗淨液之pH未達9時,無法得到充分之洗淨性。洗淨液之pH較高時洗淨效果較優良。但過高時作為洗淨液用之處理性較差,會使洗淨之膜劣化,且提高腐蝕金屬之危險性。洗淨液之pH較佳為11以上13以下。<pH> The washing liquid of the present invention is formed of an aqueous alkali solution containing free chlorine and a chlorine-binding compound, and has a pH of 9 or more. When the pH of the washing liquid is less than 9, the sufficient detergency cannot be obtained. When the pH of the washing liquid is high, the washing effect is excellent. However, when it is too high, it is less rational to use as a cleaning liquid, which will deteriorate the washed film and increase the risk of corrosion of the metal. The pH of the washing liquid is preferably 11 or more and 13 or less.

使本發明之洗淨液的pH為9以上,特別是12以上之所使用的鹼劑較佳為氫氧化鈉、氫氧化鉀等之鹼金屬的氫氧化物。The pH of the cleaning liquid of the present invention is preferably 9 or more, and particularly preferably 12 or more. The alkali agent used is an alkali metal hydroxide such as sodium hydroxide or potassium hydroxide.

本發明之洗淨劑為,由含有游離氯及結合氯之鹼水溶液所形成,且pH為12以上。洗淨劑之pH未達12時保存安定性較差,可能使稀釋使用時之洗淨效果不足。洗淨劑之pH較佳為13以上。洗淨劑之pH過高時會降低全氯濃度,而使與稀釋時之pH的平衡性變差。本發明之洗淨劑的pH上限為14。The detergent of the present invention is formed from an aqueous solution containing free chlorine and a combined chlorine, and has a pH of 12 or more. When the pH of the detergent is less than 12, the storage stability is poor, and the cleaning effect during dilution may be insufficient. The pH of the detergent is preferably 13 or more. When the pH of the detergent is too high, the total chlorine concentration is lowered, and the balance with the pH at the time of dilution is deteriorated. The pH limit of the detergent of the present invention is 14.

<洗淨液及洗淨劑之製造方法>   本發明之洗淨液及洗淨劑可藉由,將磺胺酸等之NH2 系化合物加入前述鹼劑之水溶液中,溶解後將次氯酸及/或次氯酸鹽加入所得之NH2 系化合物水溶液中混合而調製結合氯化合物水溶液,其後將次氯酸及/或次氯酸鹽加入此結合氯化合物水溶液中混合所得。<Method for Producing Cleaning Liquid and Detergent> The cleaning solution and the cleaning agent of the present invention can be obtained by adding an NH 2 -based compound such as sulfamic acid to an aqueous solution of the alkaline agent, and dissolving hypochlorous acid and / or hypochlorite is added to the obtained aqueous solution of the NH 2 -based compound to prepare an aqueous solution of the combined chlorine compound, and then hypochlorous acid and/or hypochlorite is added to the aqueous solution of the combined chlorine compound to obtain a mixture.

磺胺酸等之具有一級胺基的化合物可以鹽之形態添加。此鹽可使用磺胺酸鈉、磺胺酸鉀、磺胺酸銨等。A compound having a primary amine group such as sulfamic acid may be added in the form of a salt. As the salt, sodium sulfamate, potassium sulfamate, ammonium sulfamate or the like can be used.

本發明之洗淨液可由,必要時以水,較佳以純水稀釋上述般製造之洗淨劑所得。The cleaning solution of the present invention can be obtained by, if necessary, diluting the above-mentioned detergent prepared with water, preferably pure water.

<其他成份>   本發明所使用之洗淨液及洗淨劑於無損其洗淨效果之範圍內,可添加其他洗淨劑成分。<Other components> The cleaning liquid and the detergent used in the present invention may be added with other detergent components within a range in which the cleaning effect is not impaired.

例如為了提高膜污染物質之剝離效果,可添加一種或二種以上表面活性劑,或EDTA(伸乙基二胺四乙酸)、EGTA(乙二醇雙(胺基乙基醚)四乙酸)、IDA(亞胺基二乙酸)等之螯合劑等的其他洗淨劑成分。For example, in order to improve the peeling effect of the membrane fouling substance, one or more surfactants may be added, or EDTA (ethylene diamine tetraacetic acid), EGTA (ethylene glycol bis(aminoethyl ether) tetraacetic acid), Another detergent component such as a chelating agent such as IDA (iminodiacetic acid).

<洗淨方法>   使用本發明之洗淨液洗淨接水構件的方法中,係使接水構件接觸此洗淨液。接水構件為MF膜或UF膜時,係於結束膜裝置通水後,將洗淨液導入膜裝置內。洗淨液可由膜裝置之原水送入口導入,或由處理水出口側導入再擠壓至原水側。將洗淨液導入裝置後,將膜浸漬於洗淨液內,或使洗淨液循環。使洗淨液循環時,可將空氣吹入洗淨液中。包括浸漬與循環,洗淨液接觸選擇性透過膜之時間較佳為1~24小時,特佳為1~18小時。膜以外之接水構件時洗淨液接觸接水構件之時間也較佳為1~24小時,特佳為1~18小時。 [實施例]<Washing method> In the method of washing the water receiving member using the washing liquid of the present invention, the water receiving member is brought into contact with the washing liquid. When the water receiving member is an MF membrane or a UF membrane, the cleaning liquid is introduced into the membrane device after the membrane device is passed through the water. The washing liquid may be introduced from the raw water supply port of the membrane device, or introduced from the treated water outlet side and then pressed to the raw water side. After introducing the cleaning liquid into the apparatus, the membrane is immersed in the cleaning liquid or the washing liquid is circulated. When circulating the cleaning solution, air can be blown into the cleaning solution. Including immersion and circulation, the time during which the cleaning solution contacts the selectively permeable membrane is preferably from 1 to 24 hours, particularly preferably from 1 to 18 hours. The time during which the washing liquid contacts the water receiving member in the water-receiving member other than the film is also preferably from 1 to 24 hours, particularly preferably from 1 to 18 hours. [Examples]

[比較例1~4、實施例1]   使用由東麗股份公司製UF中空系膜組件(HFU-2008,膜素材PVDF,孔徑0.01μm)所得之膜(有效膜長100mm),製作膜一張組件(單系組件)。其後以圖1所示之單系組件用通水裝置使千葉縣五井市原地區之工業用水(以下稱為山倉工水)通過而污染膜。[Comparative Examples 1 to 4, Example 1] A film (effective film length: 100 mm) obtained by using a UF hollow membrane module (HFU-2008, membrane material PVDF, pore size: 0.01 μm) manufactured by Toray Co., Ltd. was used to prepare a film. Component (single component). Then, the industrial water used in the original area of the Fukui City, Chiba Prefecture (hereinafter referred to as Yamakura Kogyo) was passed through the water-passing device in the single-component assembly shown in Fig. 1 to contaminate the membrane.

膜1係配置於上下兩端以由灌封材料所形成之保持構件3a、3b把持的管柱2內。將膜1之上端埋設於保持構件3a內,膜1之下端係貫通保持構件3b而連通於管柱2下方之室4。通過配管5、泵6及閥7,將山倉工水供給至管柱2之下方(保持構件3b之上側),又,透過水係由管柱2下端之室4通過閥8、配管9而流出。濃縮水係由管柱2之上方(保持構件3a正下方)通過配管10,閥11而流出。逆洗水係於通過配管12、泵13及閥14,導入至管柱2之下端的室4內,而流入膜2內。逆流排水係由配管10通過分支之配管15、閥16而流出。The film 1 is disposed in the column 2 held by the holding members 3a and 3b formed of the potting material at the upper and lower ends. The upper end of the membrane 1 is embedded in the holding member 3a, and the lower end of the membrane 1 passes through the holding member 3b to communicate with the chamber 4 below the tubular string 2. The pipe 5, the pump 6 and the valve 7 supply the Yamakura water below the pipe string 2 (on the upper side of the holding member 3b), and the permeated water system flows out from the chamber 4 at the lower end of the pipe string 2 through the valve 8 and the pipe 9. . The concentrated water is discharged from the upper side of the column 2 (directly below the holding member 3a) through the pipe 10 and the valve 11. The backwash water is introduced into the chamber 4 at the lower end of the column 2 through the pipe 12, the pump 13, and the valve 14, and flows into the film 2. The countercurrent drainage system flows out from the pipe 10 through the branch pipe 15 and the valve 16.

為了膜污染而通水係以下述4步驟為1循環,重覆200循環之方式進行。   步驟1:填水力(30秒)   步驟2:過濾(透過流量2~4m3 /m2 /d,28分鐘)   步驟3:逆洗(水量0.6~1.4mL/min,30秒)   步驟4:排水(30)秒The water-passing system was carried out in the following four steps for the membrane fouling, and was repeated for 200 cycles. Step 1: Filling water (30 seconds) Step 2: Filtration (permeate flow rate 2 to 4 m 3 /m 2 /d, 28 minutes) Step 3: Backwash (water volume 0.6 to 1.4 mL/min, 30 seconds) Step 4: Drainage (30 seconds

使純水通過污染後之膜時測定透過流量4m3 /m2 /d之膜間差壓,作為洗淨前之膜間差壓值。其後將表1所示之洗淨液導入管柱2內實施浸漬。浸漬一定時間後排出藥水,以純水洗滌後使純水通過再測定透過流量4m3 /m2 /d之膜間差壓,作為該一定時間之膜間差壓值。測定膜間差壓後再度導入藥液,重覆操作至通算浸漬時間為6~8小時。又,每次導入之藥液係重新調製。膜間差壓值之測定結果(浸漬時間與膜間差壓值之關係)如圖2所示。又,任一洗淨液均為pH12,全氯濃度約1200mg。游離氯濃度係由DPD法測定。When the pure water was passed through the film after the contamination, the inter-membrane differential pressure of the permeation flow rate of 4 m 3 /m 2 /d was measured as the inter-membrane differential pressure value before washing. Thereafter, the cleaning liquid shown in Table 1 was introduced into the column 2 to perform immersion. After immersing for a certain period of time, the syrup was discharged, and after washing with pure water, the pure water was passed through and the inter-membrane differential pressure of the permeation flow rate of 4 m 3 /m 2 /d was measured to obtain the inter-membrane differential pressure value for the predetermined period of time. After the differential pressure between the membranes was measured, the chemical solution was introduced again, and the operation was repeated until the total immersion time was 6 to 8 hours. Moreover, the liquid medicine introduced each time is re-modulated. The measurement result of the differential pressure value between the membranes (the relationship between the immersion time and the differential pressure value between the membranes) is shown in Fig. 2 . Further, any of the washing liquids has a pH of 12 and a total chlorine concentration of about 1200 mg. The free chlorine concentration was determined by the DPD method.

[考察]   藉由比較例1之次氯酸鈉進行洗淨時,會明顯降低洗淨後立即之差壓(即效性高),但最終到達差壓比比較例2~4之結合氯劑高,故洗淨效果比結合氯劑差。藉由比較例2~4之結合氯劑進行洗淨時,會降低洗淨時最終到達差壓而洗淨效果高,但洗淨即效性比比較例1之次氯酸鈉差。藉由實施例1之洗淨液(結合氯+游離氯劑)進行洗淨時,可具有與次氯酸鈉同等之即效性,另兼備有與化和氯劑同等之洗淨效果。[Investigation] When the washing was carried out by the sodium hypochlorite of Comparative Example 1, the differential pressure immediately after washing (highly effective) was significantly lowered, but the final differential pressure was higher than that of Comparative Examples 2 to 4, so The cleaning effect is worse than the combined chlorine agent. When the cleaning was carried out by the combined chlorine agents of Comparative Examples 2 to 4, the differential pressure was finally lowered at the time of washing, and the washing effect was high, but the cleaning effect was inferior to that of the sodium hypochlorite of Comparative Example 1. When it is washed by the washing liquid of Example 1 (in combination with chlorine + free chlorine agent), it has the same effect as that of sodium hypochlorite, and has the same washing effect as the chemical and chlorine agent.

[比較例5,實施例2~4]   除了洗淨液如表2所示者外,以與比較例1~4及實施例1相同之條件進行膜洗淨。(但實驗日不同於比較例1~4及實施例1,故原水之水質若干不同,膜污染狀況也若干不同)。又,任一洗淨液均為pH12,全氯濃度約1200mg-Cl2 /L。結果如圖3所示。[Comparative Example 5, Examples 2 to 4] Film washing was carried out under the same conditions as in Comparative Examples 1 to 4 and Example 1 except that the cleaning liquid was as shown in Table 2. (However, the experimental day is different from Comparative Examples 1 to 4 and Example 1, so the water quality of the raw water is somewhat different, and the membrane contamination status is also somewhat different). Further, any of the cleaning solutions has a pH of 12 and a total chlorine concentration of about 1200 mg-Cl 2 /L. The result is shown in Figure 3.

[考察]   實施例2~4為,具有與比較例5之次氯酸鈉同等之即效性,且最終到達差壓中具有比次氯酸鈉低之膜間差壓(較高洗淨效果)。[Investigation] Examples 2 to 4 have the same effect as the sodium hypochlorite of Comparative Example 5, and have a film-to-membrane differential pressure (higher washing effect) lower than that of sodium hypochlorite in the final arrival differential pressure.

[比較例6~8,實施例5]   將表3所示之洗淨劑稀釋為總氯濃度1000mg-Cl2 /L後,製備藉由NaOH將pH調整為12之洗淨液。   又,將藥液洗淨步驟中通算浸漬時間設為400min。除此之外進行與前述比較例及實施例相同之實驗。但實驗日不同於前述比較例及實施例,故原水之水質若干不同,且膜之污染狀況也若干不同。[Comparative Examples 6 to 8, Example 5] After the detergent shown in Table 3 was diluted to a total chlorine concentration of 1000 mg-Cl 2 /L, a washing liquid having a pH adjusted to 12 by NaOH was prepared. Further, the immersion time in the chemical liquid washing step was set to 400 min. Except for this, the same experiment as the above Comparative Examples and Examples was carried out. However, the experimental day is different from the above comparative examples and examples, so the water quality of the raw water is somewhat different, and the pollution state of the membrane is also somewhat different.

圖4係表示洗淨時間與差壓之關係。由此得知將實施例5之洗淨劑稀釋所調製的洗淨液可最快速降低差壓,且到達差壓較低。比較例6之到達差壓仍較高,比較例7、比較例8之到達差壓近似實施例5,但差壓降低速度慢。Figure 4 shows the relationship between the cleaning time and the differential pressure. From this, it was found that the cleaning solution prepared by diluting the detergent of Example 5 can reduce the differential pressure most rapidly and reach a lower differential pressure. The arrival differential pressure of Comparative Example 6 was still high, and the arrival differential pressure of Comparative Example 7 and Comparative Example 8 was similar to that of Example 5, but the differential pressure reduction rate was slow.

<實驗例1~3>   下面將評估水溶液之殺菌效果。將下述之劑稀釋使有效氯為一定濃度後,接觸評估菌15min或1h,再測定生菌數。所使用之評估菌為Aspergillus niger。   實驗例1:次氯酸鈉水溶液(有效氯12%)   實驗例2:磺胺酸系結合氯劑Cl2 /N比=0.56 pH14.0之水溶液   實驗例3:磺胺酸系游離氯、結合氯劑Cl2 /N比=2.08 pH14.1之水溶液<Experimental Examples 1 to 3> Next, the bactericidal effect of the aqueous solution was evaluated. After diluting the following agents to a certain concentration of available chlorine, the exposed bacteria were exposed for 15 minutes or 1 hour, and the number of bacteria was measured. The evaluation strain used was Aspergillus niger. Experimental Example 1: Sodium hypochlorite aqueous solution (effective chlorine 12%) Experimental Example 2: Sulfamic acid-based combined chlorine agent Cl 2 /N ratio = 0.56 Aqueous solution of pH 14.0 Experimental Example 3: Sulfamic acid-based free chlorine, combined with chlorine agent Cl 2 / N ratio = 2.08 aqueous solution of pH 14.1

15min之結果如圖5所示。1h之結果如圖6所示。由此確認相對於實驗例1、3以有效氯濃度10m/L可於15min完全殺菌,實驗例2以有效氯200mg/L,即使於1h後幾乎菌仍生存。實驗例1雖具有高殺菌效果,但藥劑與上述比較例6相同,故洗淨效果差。   由上述得知,本發明之洗淨殺菌劑具有較高洗淨效果與殺菌效果。The result of 15 min is shown in Figure 5. The result of 1h is shown in Fig. 6. From this, it was confirmed that the effective chlorine concentration of 10 m/L was completely sterilized at 15 minutes with respect to the experimental examples 1 and 3. In the experimental example 2, the effective chlorine was 200 mg/L, and even after 1 hour, almost the bacteria survived. In Experimental Example 1, although the bactericidal effect was high, the drug was the same as that of Comparative Example 6, and the washing effect was poor. From the above, it is known that the detergent sterilizing agent of the present invention has a high washing effect and a sterilizing effect.

[氯分解率之測定實驗]   使用磺胺酸,次氯酸鈉水溶液(有效氯12質量%)、48%氫氧化鈉及純水依表4所示添加製造洗淨劑。磺胺酸之重量濃度為2.5~5.0質量%。添加(i)~(iv)所得之洗淨劑的磺胺酸莫耳濃度與殘存之有效氯莫耳濃度的關係,及氯之分解率如圖7所示。如圖7所示般磺胺酸之重量濃度愈高,氯之分解率愈大。磺胺酸之重量濃度為5.0質量%時,(有效氯莫耳濃度)/(磺胺酸莫耳濃度)之比僅超過1為1.01之程度。因此磺胺酸之重量濃度較佳為5.0質量%以下。氯之分解率較大的原因推測為,易生成不安定之二氯磺胺酸。[Experimental Test of Chlorine Decomposition Rate] A detergent was added as shown in Table 4 using sulfanilic acid, sodium hypochlorite aqueous solution (effective chlorine 12% by mass), 48% sodium hydroxide, and pure water. The weight concentration of the sulfamic acid is 2.5 to 5.0% by mass. The relationship between the concentration of sulfamate molars of the detergent obtained by adding (i) to (iv) and the residual effective chloromol concentration, and the decomposition rate of chlorine are shown in Fig. 7. As shown in Fig. 7, the higher the weight concentration of sulfamic acid, the greater the decomposition rate of chlorine. When the weight concentration of sulfamic acid is 5.0% by mass, the ratio of (effective chloromol concentration) / (sulfuric acid molar concentration) is only more than 1 to 1.01. Therefore, the weight concentration of the sulfamic acid is preferably 5.0% by mass or less. The reason why the decomposition rate of chlorine is large is presumed to be that it is easy to generate unstable dichlorosulfonamide.

以上係使用特定態樣詳細說明本發明,但本領域具有通常知識者應知於未脫離本發明之意圖與範圍內可實施各種變更。   本申請係基於2017年3月15日所申請之日本專利申請2017-050165,引用其全部內容而援用。The present invention has been described in detail with reference to the specific embodiments thereof. The present application is based on Japanese Patent Application No. 2017-050165, filed on Jan.

1‧‧‧選擇性透過膜1‧‧‧Selective permeable membrane

2‧‧‧管柱2‧‧‧ column

圖1為,表示實施例所使用之試驗裝置結構的模式圖。   圖2為,表示實施例及比較例之結果的曲線圖。   圖3為,表示實施例及比較例之結果的曲線圖。   圖4為,表示實施例及比較例之結果的曲線圖。   圖5為,表示實施例及比較例之結果的曲線圖。   圖6為,表示實驗結果之曲線圖。   圖7為,表示實驗結果之曲線圖。Fig. 1 is a schematic view showing the structure of a test apparatus used in the embodiment. Fig. 2 is a graph showing the results of Examples and Comparative Examples. Fig. 3 is a graph showing the results of Examples and Comparative Examples. Fig. 4 is a graph showing the results of Examples and Comparative Examples. Fig. 5 is a graph showing the results of Examples and Comparative Examples. Fig. 6 is a graph showing experimental results. Fig. 7 is a graph showing experimental results.

Claims (12)

一種接水構件之洗淨液,其為含有游離氯與氯胺化合物之洗淨液中,全氯與來自氯胺化合物之氮原子N的莫耳比(Cl2 /N)為1以上,pH為9以上。A cleaning solution for a water-receiving member, which is a cleaning solution containing free chlorine and a chloramine compound, wherein a molar ratio (Cl 2 /N) of total chlorine to a nitrogen atom N derived from a chloramine compound is 1 or more, pH It is 9 or more. 如請求項1之洗淨液,其中前述氯胺化合物為含有由結合氯型磺胺酸及其鹽中所選出之至少一種的磺胺酸系化合物。The cleaning solution according to claim 1, wherein the chloramine compound is a sulfamic acid-based compound containing at least one selected from the group consisting of a chlorosulfic acid and a salt thereof. 如請求項1或2之洗淨液,其中前述接水構件為MF膜、UF膜、過濾器、配管、壓力計及流量計中至少一種。The cleaning solution according to claim 1 or 2, wherein the water receiving member is at least one of an MF membrane, a UF membrane, a filter, a pipe, a pressure gauge, and a flow meter. 如請求項1~3中任一項之洗淨液,其中pH為11以上。The cleaning solution according to any one of claims 1 to 3, wherein the pH is 11 or more. 一種洗淨液,其特徵為如請求項1~4中任一項中,氯胺化合物與氯之結合型氯濃度為100mg/L以上,游離氯濃度為20mg/L以上。A cleaning liquid characterized in that, in any one of claims 1 to 4, the chlorine concentration of the chloramine compound and chlorine is 100 mg/L or more, and the free chlorine concentration is 20 mg/L or more. 一種接水構件之洗淨劑,其為含有游離氯與氯胺化合物之洗淨劑中,全氯與來自氯胺化合物之氮原子N的莫耳比(Cl2 /N)為1以上,pH為12以上。A detergent for a water-receiving member, which is a detergent containing free chlorine and a chloramine compound, wherein a molar ratio (Cl 2 /N) of total chlorine to a nitrogen atom N derived from a chloramine compound is 1 or more, pH It is 12 or more. 如請求項6之洗淨劑,其中前述氯胺化合物為含有由結合氯型磺胺酸及其鹽中所選出之至少一種的磺胺酸系化合物。The detergent according to claim 6, wherein the chloramine compound is a sulfamic acid-based compound containing at least one selected from the group consisting of a chlorosulfic acid and a salt thereof. 如請求項6或7之洗淨劑,其係藉由混合磺胺酸與鹼劑後,添加氯劑而生成結合氯化合物所得。A detergent according to claim 6 or 7, which is obtained by mixing a sulfamic acid with an alkali agent and then adding a chlorine agent to form a bound chlorine compound. 如請求項7或8之洗淨劑,其中相對於最終之洗淨劑的重量,磺胺酸之濃度為5質量%以下。The detergent according to claim 7 or 8, wherein the concentration of the sulfamic acid is 5% by mass or less based on the weight of the final detergent. 如請求項6~9中任一項之洗淨劑,其中前述接水構件為MF膜、UF膜、過濾器、配管、壓力計及流量計中至少一種。The detergent according to any one of claims 6 to 9, wherein the water receiving member is at least one of an MF membrane, a UF membrane, a filter, a pipe, a pressure gauge, and a flow meter. 一種接水構件之洗淨液,其為以水稀釋如請求項6~9中任一項之洗淨劑所得。A cleaning solution for a water-receiving member obtained by diluting the detergent according to any one of claims 6 to 9 with water. 一種接水構件之洗淨方法,其為使用如請求項1~5及請求項11中任一項之洗淨液洗淨接水構件。A cleaning method for a water receiving member, which is to wash the water receiving member using the cleaning liquid according to any one of claims 1 to 5 and claim 11.
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