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WO2018168641A1 - 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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Publication number
WO2018168641A1
WO2018168641A1 PCT/JP2018/008978 JP2018008978W WO2018168641A1 WO 2018168641 A1 WO2018168641 A1 WO 2018168641A1 JP 2018008978 W JP2018008978 W JP 2018008978W WO 2018168641 A1 WO2018168641 A1 WO 2018168641A1
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WIPO (PCT)
Prior art keywords
cleaning
chlorine
membrane
compound
water
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PCT/JP2018/008978
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French (fr)
Japanese (ja)
Inventor
貴子 岩見
孝博 川勝
愛理 田中
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栗田工業株式会社
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Priority to CN201880010367.8A priority Critical patent/CN110248723B/en
Priority to JP2018513034A priority patent/JP6610776B2/en
Publication of WO2018168641A1 publication Critical patent/WO2018168641A1/en

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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

Definitions

  • the present invention relates to a cleaning liquid, a cleaning agent, and a cleaning method for cleaning a wetted member such as a UF membrane (ultrafiltration membrane), an MF membrane (microfiltration membrane), a filter, a pipe, a pressure gauge, and a flow meter.
  • a wetted member such as a UF membrane (ultrafiltration membrane), an MF membrane (microfiltration membrane), a filter, a pipe, a pressure gauge, and a flow meter.
  • Patent Document 1 describes that a film that is susceptible to oxidative degradation is washed with a combined chlorine agent.
  • the concentration of the chloramine compound is 0.005 to 0.5 M, and the molar ratio (Cl 2 / N) of effective chlorine (Cl 2 ) to nitrogen atom N derived from the chloramine compound is 0.00.
  • the membrane is cleaned under conditions where almost no free chlorine exists.
  • Patent Document 2 describes that a cooling water system, a wastewater treatment water system, and a paper pulp water system are sterilized by using a combined chlorine agent having Cl 2 / N larger than 1. Patent Document 2 describes that the free chlorine concentration during the sterilization treatment is 0.05 mg / L or more. Patent Document 2 does not describe the use of the cleaning agent for the selective permeable membrane.
  • An object of the present invention is to provide a cleaning liquid, a cleaning agent, and a cleaning method having a high cleaning effect.
  • the gist of the present invention is as follows.
  • the cleaning solution for a water contact member of the present invention is a cleaning solution containing free chlorine and a chloramine compound, and the molar ratio (Cl 2 / N) of nitrogen atoms N derived from total chlorine and the chloramine compound is 1 or more, and the pH is 9 That's it.
  • the chloramine compound includes at least one sulfamic acid compound selected from bound chlorine type sulfamic acid and a salt thereof.
  • the water contact member is at least one of an MF membrane, a UF membrane, a filter, a pipe, a pressure gauge, and a flow meter.
  • the pH of the cleaning liquid is 11 or more.
  • the combined 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.
  • the cleaning agent for a water contact member of the present invention is a cleaning agent containing free chlorine and a chloramine compound, and the molar ratio (Cl 2 / N) of nitrogen atoms N derived from total chlorine and the chloramine compound is 1 or more. , PH 12 or more.
  • the chloramine compound includes at least one sulfamic acid compound selected from bound chlorine type sulfamic acid and a salt thereof.
  • the cleaning agent of the present invention it is obtained by mixing sulfamic acid and an alkali agent and then adding a chlorine agent to form a combined chlorine compound.
  • the concentration of sulfamic acid relative to the final cleaning agent weight is 5% by mass or less.
  • the water contact member is at least one of an MF membrane, a UF membrane, a filter, a pipe, a pressure gauge, and a flow meter.
  • the cleaning solution for the water contact member of the present invention is obtained by diluting the above-described cleaning agent of the present invention with water.
  • the water contact member cleaning method of the present invention cleans the water contact member using the cleaning liquid of the present invention.
  • the cleaning solution, cleaning agent, and cleaning method for the water contact member of the present invention have both the oxidizing power of the free chlorine agent and the strength of penetration of the bound chlorine agent (chloramine compound) into the water contact member. Therefore, it is more effective than the combined chlorine agent and has a higher cleaning effect than the free chlorine agent. Moreover, the cleaning liquid and the cleaning agent of the present invention also have an excellent sterilizing effect.
  • the present invention relates to a cleaning liquid, a cleaning agent, and a cleaning method.
  • cleaning liquid and “cleaning agent” are distinguished as follows.
  • the cleaning liquid is a liquid used during cleaning.
  • the cleaning agent in the present invention is a product used for distribution.
  • the cleaning agent may be used as it is as a cleaning solution, but usually the cleaning agent is diluted with water or the like and used as a cleaning solution for cleaning.
  • the cleaning liquid of the present invention contains free chlorine and a combined chlorine compound.
  • the cleaning liquid of the present invention has a molar ratio (Cl 2 / N) of nitrogen atoms N derived from total chlorine (Cl 2 ) and combined chlorine compounds of 1 or more and a pH of 9 or more.
  • Cleaning solution of the present invention preferably, the total chlorine concentration 5,000mg-Cl 2 / L or less, more preferably 200 ⁇ 5,000mg-Cl 2 / L , particularly preferably 1,000 ⁇ 2,000mg-Cl 2 / L, bound chlorine concentration of 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, free chlorine concentration of 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.
  • the cleaning agent of the present invention is a cleaning agent containing free chlorine and a chloramine compound, and the molar ratio (Cl 2 / N) of total chlorine (Cl 2 ) to nitrogen atom N derived from the chloramine compound is 1 or more. , PH 12 or more.
  • the cleaning agent of the present invention preferably has a total chlorine concentration (Cl 2 equivalent concentration) of 10% by mass or less, more preferably 1 to 8% by mass, particularly preferably 3 to 8% by mass.
  • the combined chlorine concentration (Cl 2 equivalent concentration) 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 (Cl 2 equivalent concentration) is 0. 0.02% by mass or more, more preferably 0.1 to 10% by mass, particularly preferably 1 to 5% by mass.
  • the total chlorine concentration and the free chlorine concentration are measured by the DPD method defined in JIS K 0400-33-10: 1999.
  • the bound chlorine concentration is determined by subtracting the free chlorine concentration from the total chlorine concentration determined above.
  • the present invention makes it possible to apply a chlorine-based cleaning liquid and a cleaning agent to a water contact member under alkaline conditions.
  • the organic substance decomposing action by the combined chlorine compound and the immediate sterilizing and washing effect by free chlorine 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 washing
  • the water contact member examples include, but are not limited to, a UF membrane, an MF membrane, a filter, a pipe, a pressure gauge, and a flow meter.
  • the filter examples include those using granular filter media such as sand and anthracite.
  • the selective permeable membrane is not limited to these, and the present invention can be applied to other selective permeable membranes, and the membrane material is not limited.
  • hypochlorous acid and / or hypochlorite is used.
  • hypochlorite alkali metal salts of hypochlorous acid such as sodium hypochlorite, alkaline earth metal salts of hypochlorous acid such as calcium hypochlorite, and the like can be used. These may be used alone or in combination of two or more.
  • the bound chlorine compound is 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 a hydrogen atom of an amino group is substituted with a chlorine atom is preferred. Since this compound has a weak oxidizing action, it can be used as a cleaning liquid and a cleaning agent even for aromatic polyamide RO membranes with low chlorine resistance. Also penetrates and exerts a decomposing action inside.
  • the bonded chlorine compound is any one of a compound having a primary amino group, ammonia, and an ammonium salt (hereinafter referred to as “NH 2 -based compound”), hypochlorous acid and / or the following. It is preferable to produce by mixing with chlorite.
  • NH 2 -based compound an ammonium salt
  • the compound having a primary amino group include aliphatic amines, aromatic amines, sulfamic acids, sulfanilic acids, sulfamoylbenzoic acids, and amino acids.
  • ammonium salts include ammonium chloride and ammonium sulfate. These may be used alone or in combination of two or more.
  • sulfamic acid (NH 2 SO 2 OH) is preferable.
  • a stable bound chlorine compound is obtained. Since sulfamic acid does not contain carbon, it does not increase the TOC value of the cleaning agent.
  • sulfamic acid and an alkaline agent in combination, a very effective cleaning solution and cleaning agent are obtained.
  • Hypochlorite to be reacted with NH 2 compounds includes alkali metal salts of hypochlorous acid such as sodium hypochlorite, 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.
  • the weight concentration of sulfamic acid used is preferably 5% by mass or less based on the weight of the final cleaning agent. If the concentration of sulfamic acid is higher than 5% by mass, chlorine may be easily decomposed.
  • the Cl 2 / N molar ratio which is the molar ratio of available chlorine derived from free chlorine (Cl 2 ) and nitrogen atom N derived from the combined chlorine compound, is 1 or more, preferably 1 to 10, particularly preferably 1 to 5. By setting it within this range, an immediate cleaning action of free chlorine and an osmotic cleaning action of the combined chlorine compound can be obtained in a balanced manner.
  • the cleaning liquid of the present invention comprises an aqueous alkaline solution containing free chlorine and a combined chlorine compound, and has a pH of 9 or more. If the pH of the cleaning liquid is less than 9, sufficient cleaning properties cannot be obtained. The higher the pH of the cleaning solution is, the better the cleaning effect is. However, when the cleaning solution is too high, the handling property as the cleaning solution is deteriorated, and the film to be cleaned is deteriorated or the risk of corrosion of the metal is increased.
  • the pH of the cleaning liquid is preferably 11 or more and 13 or less.
  • the alkali agent used to adjust the cleaning liquid of the present invention to pH 9 or more, particularly 12 or more, is preferably an alkali metal hydroxide such as sodium hydroxide or potassium hydroxide.
  • the cleaning agent of the present invention comprises an aqueous alkaline solution containing free chlorine and bound chlorine, and has a pH of 12 or more.
  • the pH of the cleaning agent is preferably 13 or more. If the pH of the cleaning agent is too high, the total chlorine concentration becomes low, and the balance with the pH when diluted is poor.
  • the upper limit of the pH of the cleaning agent of the present invention is 14.
  • the cleaning liquid and cleaning agent of the present invention are 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.
  • a combined chlorine compound aqueous solution can be prepared by adding and mixing chlorate, and hypochlorous acid and / or hypochlorite can be added to and mixed with this combined chlorine compound aqueous solution. .
  • a compound having a primary amino group such as sulfamic acid may be added in the form of a salt.
  • a salt sodium sulfamate, potassium sulfamate, ammonium sulfamate, etc. can be used.
  • the cleaning liquid of the present invention may be obtained by diluting the cleaning agent produced as described above with water, preferably with pure water as necessary.
  • surfactants and chelating agents such as EDTA (ethylenediaminetetraacetic acid), EGTA (ethyleneglycolbis (aminoethylether) tetraacetic acid), IDA (iminodiacetic acid), etc. to enhance the peeling effect of membrane contaminants You may add 1 type, or 2 or more types of the other washing
  • EDTA ethylenediaminetetraacetic acid
  • EGTA ethyleneglycolbis (aminoethylether) tetraacetic acid
  • IDA iminodiacetic acid
  • the water contact member is brought into contact with the cleaning liquid.
  • the cleaning liquid is introduced into the membrane device.
  • the cleaning liquid may be introduced from the raw water inlet of the membrane device, or may be introduced from the treated water outlet and pushed out to the raw water side.
  • the membrane is immersed in the cleaning liquid or the cleaning liquid is circulated. When the cleaning liquid is circulated, air may be blown into the cleaning liquid.
  • the contact time between the cleaning solution and the selective permeable membrane is preferably about 1 to 24 hours, particularly about 1 to 18 hours. Also in the case of a water contact member other than a membrane, the contact time between the cleaning liquid and the water contact member is preferably about 1 to 24 hours, particularly about 1 to 18 hours.
  • Example 1 Using a membrane (effective membrane length 100 mm) obtained from a UF hollow fiber membrane module (HFU-2008, membrane material PVDF, pore diameter 0.01 ⁇ m) manufactured by Toray Industries, Inc., a single membrane module (single yarn module) was created. . Thereafter, the membrane was contaminated by passing water for industrial use (hereinafter referred to as “Yamakura Kosui”) in the Hara area of Goi City, Chiba Prefecture with the single-thread module water flow device shown in FIG.
  • Yamakura Kosui contaminated by passing water for industrial use
  • the membrane 1 is arranged in the column 2 with its upper and lower ends held by holding members 3a and 3b made of a potting material.
  • the upper end of the film 1 is embedded in the holding member 3a.
  • the lower end of the membrane 1 passes through the holding member 3b and communicates with the chamber 4 below the column 2.
  • Yamakura industrial water is supplied to the lower part of the column 2 (above the holding member 3b) via the pipe 5, the pump 6 and the valve 7, and the permeated water passes through the valve 8 and the pipe 9 from the chamber 4 at the lower end of the column 2. Leaked.
  • the concentrated water flows out from the upper part of the column 2 (just 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 membrane 2.
  • the backwash drainage flows out through the pipe 15 and the valve 16 branched from the pipe 10.
  • Process 1 Water filling (30 seconds)
  • Step 2 Filtration (permeation flux 2-4 m 3 / m 2 / d, 28 minutes)
  • Step 3 Backwash (water volume 0.6-1.4 mL / min, 30 seconds)
  • Process 4 Drainage (30 seconds)
  • the measurement result of the transmembrane pressure value (relation between the immersion time and the transmembrane pressure value) is shown in FIG.
  • Each cleaning solution has a pH of 12 and a total chlorine concentration of about 1200 mg. Free chlorine concentration was measured by the DPD method.
  • Fig. 4 shows the relationship between cleaning time and differential pressure. It can be seen that the cleaning liquid prepared by diluting the cleaning agent of Example 5 has the fastest difference pressure drop and the lowest ultimate pressure difference. In Comparative Example 6, the ultimate differential pressure remains high. In Comparative Examples 7 and 8, the ultimate differential pressure is close to that of Example 5, but the method of decreasing the differential pressure is slow.
  • FIG. 7 shows the relationship between the molar concentration of sulfamic acid and the residual effective molar concentration of chlorine in the detergents obtained by the formulations (i) to (iv), and the decomposition rate of chlorine. As shown in FIG. 7, the higher the weight concentration of sulfamic acid, the greater the decomposition rate of chlorine.
  • the weight concentration of sulfamic acid is 5.0 mass%
  • the ratio of (effective chlorine molar concentration) / (sulfamic acid molar concentration) is 1.01, which is slightly over 1. Accordingly, the weight concentration of sulfamic acid is preferably 5.0% by mass or less. The reason why the decomposition rate of chlorine increases is presumably because unstable dichlorosulfamic acid is easily formed.

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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

接水部材の洗浄液、洗浄剤および洗浄方法Cleaning liquid, cleaning agent and cleaning method for wetted parts
 本発明は、UF膜(限外濾過膜)やMF膜(精密濾過膜)、濾過器、配管、圧力計、流量計などの接水部材を洗浄する洗浄液、洗浄剤及び洗浄方法に関する。 The present invention relates to a cleaning liquid, a cleaning agent, and a cleaning method for cleaning a wetted member such as a UF membrane (ultrafiltration membrane), an MF membrane (microfiltration membrane), a filter, a pipe, a pressure gauge, and a flow meter.
 UF膜やMF膜を用いる膜分離装置(除濁膜装置)においては、分離膜に汚れが付着するため、通常30秒~60分ごとに間欠的に洗浄流体(水及び/又は気体)を供給して膜の物理洗浄を行う。 In membrane separation devices (turbidity membrane devices) that use UF membranes or MF membranes, dirt is attached to the separation membrane, so cleaning fluid (water and / or gas) is usually supplied intermittently every 30 seconds to 60 minutes. Then, the membrane is physically cleaned.
 この物理洗浄においても除去できない汚れが膜に堆積するため、次第に膜の濾過能力が低下する。 Since dirt that cannot be removed even by this physical cleaning is deposited on the film, the filtration capacity of the film gradually decreases.
 そのため、除濁膜装置においては定期的あるいは非定期的に薬品を用いた薬品洗浄が必要となる。 Therefore, chemical cleaning using chemicals is required regularly or irregularly in the turbidity removal membrane device.
 特許文献1には、酸化劣化しやすい膜を、結合塩素剤によって洗浄することが記載されている。特許文献1には、洗浄剤の配合について、クロラミン化合物濃度0.005~0.5M、有効塩素(Cl)とクロラミン化合物に由来する窒素原子Nのモル比(Cl/N)が0.1~1との記載がある。従って、特許文献1の洗浄方法では、膜は、遊離塩素がほとんど存在しない条件で洗浄される。 Patent Document 1 describes that a film that is susceptible to oxidative degradation is washed with a combined chlorine agent. In Patent Document 1, the concentration of the chloramine compound is 0.005 to 0.5 M, and the molar ratio (Cl 2 / N) of effective chlorine (Cl 2 ) to nitrogen atom N derived from the chloramine compound is 0.00. There is a description of 1-1. Therefore, in the cleaning method of Patent Document 1, the membrane is cleaned under conditions where almost no free chlorine exists.
 特許文献2には、Cl/Nが1より大きい結合塩素剤を用いて、冷却水系、排水処理水系、紙パルプ水系の殺菌を行うことが記載されている。特許文献2には、殺菌処理時の遊離塩素濃度は0.05mg/L以上と記載されている。特許文献2には、選択性透過膜の洗浄剤の用途についての記載はない。 Patent Document 2 describes that a cooling water system, a wastewater treatment water system, and a paper pulp water system are sterilized by using a combined chlorine agent having Cl 2 / N larger than 1. Patent Document 2 describes that the free chlorine concentration during the sterilization treatment is 0.05 mg / L or more. Patent Document 2 does not describe the use of the cleaning agent for the selective permeable membrane.
特開2015-97991号公報Japanese Patent Laid-Open No. 2015-97991 特開2009-195823号公報JP 2009-195823 A
 本発明は、洗浄効果の高い洗浄液、洗浄剤及び洗浄方法を提供することを目的とする。 An object of the present invention is to provide a cleaning liquid, a cleaning agent, and a cleaning method having a high cleaning effect.
 本発明は、次を要旨とする。 The gist of the present invention is as follows.
 本発明の接水部材の洗浄液は、遊離塩素とクロラミン化合物とを含む洗浄液であって、全塩素とクロラミン化合物に由来する窒素原子Nのモル比(Cl/N)が1以上であり、pH9以上である。 The cleaning solution for a water contact member of the present invention is a cleaning solution containing free chlorine and a chloramine compound, and the molar ratio (Cl 2 / N) of nitrogen atoms N derived from total chlorine and the chloramine compound is 1 or more, and the pH is 9 That's it.
 本発明の洗浄液の一態様では、前記クロラミン化合物として結合塩素型スルファミン酸およびその塩から選ばれる少なくとも1種のスルファミン酸系化合物を含む。 In one aspect of the cleaning liquid of the present invention, the chloramine compound includes at least one sulfamic acid compound selected from bound chlorine type sulfamic acid and a salt thereof.
 本発明の洗浄液の一態様では、前記接水部材がMF膜、UF膜、濾過器、配管、圧力計及び流量計の少なくとも一つである。 In one aspect of the cleaning liquid of the present invention, the water contact member is at least one of an MF membrane, a UF membrane, a filter, a pipe, a pressure gauge, and a flow meter.
 本発明の洗浄液の一態様では、洗浄液のpHは11以上である。 In one aspect of the cleaning liquid of the present invention, the pH of the cleaning liquid is 11 or more.
 本発明の洗浄液の一態様では、クロラミン化合物と塩素の結合型塩素濃度が100mg/L以上、遊離塩素濃度が20mg/L以上である。 In one embodiment of the cleaning liquid of the present invention, the combined 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.
 本発明の接水部材の洗浄剤は、遊離塩素とクロラミン化合物とを含む洗浄剤であって、全塩素とクロラミン化合物に由来する窒素原子Nのモル比(Cl/N)が1以上であり、pH12以上である。 The cleaning agent for a water contact member of the present invention is a cleaning agent containing free chlorine and a chloramine compound, and the molar ratio (Cl 2 / N) of nitrogen atoms N derived from total chlorine and the chloramine compound is 1 or more. , PH 12 or more.
 本発明の洗浄剤の一態様では、前記クロラミン化合物として結合塩素型スルファミン酸およびその塩から選ばれる少なくとも1種のスルファミン酸系化合物を含む。 In one aspect of the cleaning agent of the present invention, the chloramine compound includes at least one sulfamic acid compound selected from bound chlorine type sulfamic acid and a salt thereof.
 本発明の洗浄剤の一態様では、スルファミン酸とアルカリ剤を混合した後、塩素剤を添加して結合塩素化合物を生成させることによって得られる。 In one embodiment of the cleaning agent of the present invention, it is obtained by mixing sulfamic acid and an alkali agent and then adding a chlorine agent to form a combined chlorine compound.
 本発明の洗浄剤の一態様では、最終的な洗浄剤の重量に対するスルファミン酸の濃度が5質量%以下である。 In one embodiment of the cleaning agent of the present invention, the concentration of sulfamic acid relative to the final cleaning agent weight is 5% by mass or less.
 本発明の洗浄剤の一態様では、前記接水部材がMF膜、UF膜、濾過器、配管、圧力計及び流量計の少なくとも一つである。 In one aspect of the cleaning agent of the present invention, the water contact member is at least one of an MF membrane, a UF membrane, a filter, a pipe, a pressure gauge, and a flow meter.
 本発明の接水部材の洗浄液は、上記本発明の洗浄剤を水で希釈してなる。 The cleaning solution for the water contact member of the present invention is obtained by diluting the above-described cleaning agent of the present invention with water.
 本発明の接水部材の洗浄方法は、本発明の洗浄液を用いて接水部材を洗浄する。 The water contact member cleaning method of the present invention cleans the water contact member using the cleaning liquid of the present invention.
 本発明の接水部材の洗浄液、洗浄剤及び洗浄方法は、遊離塩素剤の酸化力の強さと、結合塩素剤(クロラミン化合物)の接水部材内部への浸透力の強さを併せ持つ。そのため、結合塩素剤よりも即効性があり、遊離塩素剤よりも洗浄効果が高い。また、本発明の洗浄液及び洗浄剤は優れた殺菌効果も有する。 The cleaning solution, cleaning agent, and cleaning method for the water contact member of the present invention have both the oxidizing power of the free chlorine agent and the strength of penetration of the bound chlorine agent (chloramine compound) into the water contact member. Therefore, it is more effective than the combined chlorine agent and has a higher cleaning effect than the free chlorine agent. Moreover, the cleaning liquid and the cleaning agent of the present invention also have an excellent sterilizing effect.
実施例で用いた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 test apparatus used in the Example. 実施例及び比較例の結果を示すグラフである。It is a graph which shows the result of an Example and a comparative example. 実施例及び比較例の結果を示すグラフである。It is a graph which shows the result of an Example and a comparative example. 実施例及び比較例の結果を示すグラフである。It is a graph which shows the result of an Example and a comparative example. 実施例及び比較例の結果を示すグラフである。It is a graph which shows the result of an Example and a comparative example. 実験結果を示すグラフである。It is a graph which shows an experimental result. 実験結果を示すグラフである。It is a graph which shows an experimental result.
 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.
 本発明は、洗浄液、洗浄剤および洗浄方法に関する発明であるが、本発明において「洗浄液」と「洗浄剤」とは以下の通り区別されるものである。
 本発明において洗浄液とは、洗浄時に使用される液体である。一方、本発明において洗浄剤とは流通の際に使用される製品である。洗浄剤をそのまま洗浄液として洗浄に供する場合もあるが、通常は、洗浄剤は水などで希釈して洗浄液として洗浄に使用される。
The present invention relates to a cleaning liquid, a cleaning agent, and a cleaning method. In the present invention, “cleaning liquid” and “cleaning agent” are distinguished as follows.
In the present invention, the cleaning liquid is a liquid used during cleaning. On the other hand, the cleaning agent in the present invention is a product used for distribution. In some cases, the cleaning agent may be used as it is as a cleaning solution, but usually the cleaning agent is diluted with water or the like and used as a cleaning solution for cleaning.
 本発明の洗浄液は、遊離塩素と結合塩素化合物とを含む。本発明の洗浄液は、全塩素(Cl)と結合塩素化合物に由来する窒素原子Nのモル比(Cl/N)が1以上であり、pH9以上である。 The cleaning liquid of the present invention contains free chlorine and a combined chlorine compound. The cleaning liquid of the present invention has a molar ratio (Cl 2 / N) of nitrogen atoms N derived from total chlorine (Cl 2 ) and combined chlorine compounds of 1 or more and a pH of 9 or more.
 本発明の洗浄液は、好ましくは、全塩素濃度5,000mg-Cl/L以下、より好ましくは200~5,000mg-Cl/L、特に好ましくは1,000~2,000mg-Cl/L、結合塩素濃度100mg-Cl/L以上、より好ましくは100~4,980mg-Cl/L、特に好ましくは300~1,980mg-Cl/L、遊離塩素濃度が20mg-Cl/L以上、より好ましくは20~4,900mg-Cl/L、特に好ましくは20~1,700mg-Cl/Lである。 Cleaning solution of the present invention, preferably, the total chlorine concentration 5,000mg-Cl 2 / L or less, more preferably 200 ~ 5,000mg-Cl 2 / L , particularly preferably 1,000 ~ 2,000mg-Cl 2 / L, bound chlorine concentration of 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, free chlorine concentration of 20 mg-Cl 2 / L L or more, more preferably 20 to 4,900 mg-Cl 2 / L, particularly preferably 20 to 1,700 mg-Cl 2 / L.
 本発明の洗浄剤は、遊離塩素とクロラミン化合物とを含む洗浄剤であって、全塩素(Cl)とクロラミン化合物に由来する窒素原子Nのモル比(Cl/N)が1以上であり、pH12以上である。 The cleaning agent of the present invention is a cleaning agent containing free chlorine and a chloramine compound, and the molar ratio (Cl 2 / N) of total chlorine (Cl 2 ) to nitrogen atom N derived from the chloramine compound is 1 or more. , PH 12 or more.
 本発明の洗浄剤は、好ましくは、全塩素濃度(Cl換算濃度)は10質量%以下、より好ましくは1~8質量%、特に好ましくは3~8質量%である。結合塩素濃度(Cl換算濃度)は0.1質量%以上、より好ましくは0.5~3質量%、特に好ましくは1~2.8質量%、遊離塩素濃度(Cl換算濃度)は0.02質量%以上、より好ましくは0.1~10質量%、特に好ましくは1~5質量%である。 The cleaning agent of the present invention preferably has a total chlorine concentration (Cl 2 equivalent concentration) of 10% by mass or less, more preferably 1 to 8% by mass, particularly preferably 3 to 8% by mass. The combined chlorine concentration (Cl 2 equivalent concentration) 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 (Cl 2 equivalent concentration) is 0. 0.02% by mass or more, more preferably 0.1 to 10% by mass, particularly preferably 1 to 5% by mass.
 本発明において、全塩素濃度および遊離塩素濃度はJIS K 0400-33-10:1999で規定されるDPD法により測定する。また、結合塩素濃度は前記で求めた全塩素濃度から遊離塩素濃度を差し引くことで求める。 In the present invention, the total chlorine concentration and the free chlorine concentration are measured by the DPD method defined in JIS K 0400-33-10: 1999. The bound chlorine concentration is determined by subtracting the free chlorine concentration from the total chlorine concentration determined above.
 本発明は、アルカリ条件下における塩素系洗浄液及び洗浄剤の接水部材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、結合塩素化合物による有機物分解作用と、遊離塩素による即効的殺菌洗浄効果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、汚染した選択性透過膜や濾過器等の性能を十分に回復させることができる。 The present invention makes it possible to apply a chlorine-based cleaning liquid and a cleaning agent to a water contact member under alkaline conditions. In the present invention, the organic substance decomposing action by the combined chlorine compound and the immediate sterilizing and washing effect by free chlorine 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 washing | cleaning can be improved and performances, such as a contaminated permselective membrane and a filter, can fully be recovered | restored.
<接水部材>
 接水部材としては、UF膜、MF膜、濾過器、配管、圧力計、流量計などが例示されるが、これらに限定されない。濾過器としては、砂、アンスラサイト等の粒状濾材を用いたものが例示される。
 本発明は、MF膜及びUF膜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、選択性透過膜は何らこれらに限定されず、本発明は、その他の選択性透過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選択性透過膜の洗浄に有効に適用される。
<Wetted parts>
Examples of the water contact member include, but are not limited to, a UF membrane, an MF membrane, a filter, a pipe, a pressure gauge, and a flow meter. Examples of the filter include those using granular filter media such as sand and anthracite.
In the present invention, when the MF film and the UF film are to be cleaned, the cleaning effect is effectively exhibited. However, the selective permeable membrane is not limited to these, and the present invention can be applied to other selective permeable membranes, and the membrane material is not limited. Moreover, there is no restriction | limiting also in the form of a membrane etc., This invention is applied effectively to the washing | cleaning of the selective permeable membrane for water treatment in a wide field | area.
<遊離塩素>
 遊離塩素としては、次亜塩素酸及び/又は次亜塩素酸塩が用いられる。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。
<Free chlorine>
As free chlorine, hypochlorous acid and / or hypochlorite is used. As hypochlorite, alkali metal salts of hypochlorous acid such as sodium hypochlorite, alkaline earth metal salts of hypochlorous acid such as calcium hypochlorite, and the like can be used. These may be used alone or in combination of two or more.
<結合塩素化合物>
 結合塩素化合物としては、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、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膜であっても洗浄液及び洗浄剤として用いることが可能となり、また、多糖類のような粘度の高い汚染物に対しても、浸透して、内部で分解作用を発揮する。
  XNH+HOCl⇔XNHCl+HO   (1)
  XNH+OCl⇔XNHCl+OH   (2)
<Combined chlorine compounds>
The bound chlorine compound is 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 a hydrogen atom of an amino group is substituted with a chlorine atom is preferred. Since this compound has a weak oxidizing action, it can be used as a cleaning liquid and a cleaning agent even for aromatic polyamide RO membranes with low chlorine resistance. Also penetrates and exerts a decomposing action inside.
XNH 2 + HOCl⇔XNHCl + H 2 O (1)
XNH 2 + OCl ⇔XNHCl + OH (2)
 本発明において、結合塩素化合物は、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結合塩素化合物となる。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、非常に有効な洗浄液及び洗浄剤となる。 In the present invention, the bonded chlorine compound is any one of a compound having a primary amino group, ammonia, and an ammonium salt (hereinafter referred to as “NH 2 -based compound”), hypochlorous acid and / or the following. It is preferable to produce by mixing with chlorite. 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, a stable bound chlorine compound is obtained. 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 solution and cleaning agent are obtained.
 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。
 結合塩素を形成させる窒素原子を有する化合物としてスルファミン酸を用いる場合、最終的な洗浄剤の重量に対して、使用するスルファミン酸の重量濃度を5質量%以下とすることが好ましい。スルファミン酸の濃度が5質量%よりも大きくなると塩素が分解しやすくなることがある。
Hypochlorite to be reacted with NH 2 compounds includes alkali metal salts of hypochlorous acid such as sodium hypochlorite, 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.
When sulfamic acid is used as the compound having a nitrogen atom that forms bonded chlorine, the weight concentration of sulfamic acid used is preferably 5% by mass or less based on the weight of the final cleaning agent. If the concentration of sulfamic acid is higher than 5% by mass, chlorine may be easily decomposed.
<遊離塩素と結合塩素化合物との比率>
 本発明では、遊離塩素由来の有効塩素(Cl)と結合塩素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1以上、好ましくは1~10、特に好ましくは1~5である。この範囲とすることにより、遊離塩素の即効的洗浄作用と結合塩素化合物の浸透的洗浄作用とがバランスよく得られる。
<Ratio of free chlorine and combined chlorine compounds>
In the present invention, the Cl 2 / N molar ratio, which is the molar ratio of available chlorine derived from free chlorine (Cl 2 ) and nitrogen atom N derived from the combined chlorine compound, is 1 or more, preferably 1 to 10, particularly preferably 1 to 5. By setting it within this range, an immediate cleaning action of free chlorine and an osmotic cleaning action of the combined chlorine compound can be obtained in a balanced manner.
<pH>
 本発明の洗浄液は、遊離塩素及び結合塩素化合物含有アルカリ水溶液よりなり、pHが9以上である。洗浄液のpHが9未満であると、十分な洗浄性が得られない。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、洗浄される膜が劣化したり、金属が腐食する危険性が高くなる。洗浄液のpHは好ましくは11以上13以下である。
<PH>
The cleaning liquid of the present invention comprises an aqueous alkaline solution containing free chlorine and a combined chlorine compound, and has a pH of 9 or more. If the pH of the cleaning liquid is less than 9, sufficient cleaning properties cannot be obtained. The higher the pH of the cleaning solution is, the better the cleaning effect is. However, when the cleaning solution is too high, the handling property as the cleaning solution is deteriorated, and the film to be cleaned is deteriorated or the risk of corrosion of the metal is increased. The pH of the cleaning liquid is preferably 11 or more and 13 or less.
 本発明の洗浄液をpH9以上特に12以上とするのに用いるアルカリ剤は、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が好ましい。 The alkali agent used to adjust the cleaning liquid of the present invention to pH 9 or more, particularly 12 or more, is preferably an alkali metal hydroxide such as sodium hydroxide or potassium hydroxide.
 本発明の洗浄剤は、遊離塩素及び結合塩素含有アルカリ水溶液よりなり、pH12以上である。洗浄剤のpHが12未満であると、保存安定性が悪くなり、希釈使用した時の洗浄効果が不足する可能性がある。洗浄剤のpHは好ましくは13以上である。洗浄剤のpHが高すぎると全塩素濃度が低くなり、希釈した時のpHとのバランスが悪くなる。本発明の洗浄剤のpHの上限は14である。 The cleaning agent of the present invention comprises an aqueous alkaline solution containing free chlorine and bound chlorine, and has a pH of 12 or more. When the pH of the cleaning agent is less than 12, the storage stability is deteriorated, and the cleaning effect may be insufficient when diluted. The pH of the cleaning agent is preferably 13 or more. If the pH of the cleaning agent is too high, the total chlorine concentration becomes low, and the balance with the pH when diluted is poor. The upper limit of the pH of the cleaning agent of the present invention is 14.
<洗浄液及び洗浄剤の製造方法>
 本発明の洗浄液及び洗浄剤は、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結合塩素化合物水溶液を調製し、この結合塩素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。
<Manufacturing method of cleaning liquid and cleaning agent>
The cleaning liquid and cleaning agent of the present invention are 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. A combined chlorine compound aqueous solution can be prepared by adding and mixing chlorate, and hypochlorous acid and / or hypochlorite can be added to and mixed with this combined chlorine compound aqueous solution. .
 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、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。 A compound having a primary amino group such as sulfamic acid may be added in the form of a salt. As this salt, sodium sulfamate, potassium sulfamate, ammonium sulfamate, etc. can be used.
 本発明の洗浄液は、上述の通りに製造された洗浄剤を、必要に応じ水、好ましくは純水で希釈して得てもよい。 The cleaning liquid of the present invention may be obtained by diluting the cleaning agent produced as described above with water, preferably with pure water as necessary.
<その他の成分>
 本発明で用いる洗浄液及び洗浄剤には、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。
<Other ingredients>
To the cleaning liquid and the cleaning agent used in the present invention, other cleaning component may be added as long as the cleaning effect is not impaired.
 例えば、膜汚染物質の剥離効果を高めるために、界面活性剤や、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。 For example, surfactants and chelating agents such as EDTA (ethylenediaminetetraacetic acid), EGTA (ethyleneglycolbis (aminoethylether) tetraacetic acid), IDA (iminodiacetic acid), etc. to enhance the peeling effect of membrane contaminants You may add 1 type, or 2 or more types of the other washing | cleaning-agent component.
<洗浄方法>
 本発明の洗浄液を用いて接水部材を洗浄する方法では、この洗浄液に接水部材を接触させる。接水部材がMF膜又はUF膜である場合、膜装置への通水を停止した後に、洗浄液を膜装置に導入する。洗浄液は膜装置の原水入り口から導入されてもよく、処理水出口側から導入され原水側に押し出されても良い。洗浄液を装置に導入した後は、膜を洗浄液に浸漬させるか、又は洗浄液を循環させる。洗浄液を循環させる場合、洗浄液に空気を吹き込んでも良い。浸漬と循環を含めて、洗浄液と選択性透過膜の接触時間は1~24時間特に1~18時間程度が好ましい。膜以外の接水部材の場合も、洗浄液と接水部材の接触時間は1~24時間特に1~18時間程度が好ましい。
<Washing method>
In the method of cleaning the water contact member using the cleaning liquid of the present invention, the water contact member is brought into contact with the cleaning liquid. In the case where the water contact member is an MF membrane or a UF membrane, after stopping water flow to the membrane device, the cleaning liquid is introduced into the membrane device. The cleaning liquid may be introduced from the raw water inlet of the membrane device, or may be introduced from the treated water outlet and pushed out to the raw water side. After the cleaning liquid is introduced into the apparatus, the membrane is immersed in the cleaning liquid or the cleaning liquid is circulated. When the cleaning liquid is circulated, air may be blown into the cleaning liquid. Including immersion and circulation, the contact time between the cleaning solution and the selective permeable membrane is preferably about 1 to 24 hours, particularly about 1 to 18 hours. Also in the case of a water contact member other than a membrane, the contact time between the cleaning liquid and the water contact member is preferably about 1 to 24 hours, particularly about 1 to 18 hours.
[比較例1~4、実施例1]
 東レ株式会社製UF中空糸膜モジュール(HFU-2008、膜素材PVDF、孔径0.01μm)から得た膜(有効膜長さ100mm)を用いて、膜1本モジュール(単糸モジュール)を作成した。その後、図1に示す単糸モジュール用通水装置で千葉県五井市原地区の工業用水(以下、山倉工水)を通水して膜を汚染させた。
[Comparative Examples 1 to 4, Example 1]
Using a membrane (effective membrane length 100 mm) obtained from a UF hollow fiber membrane module (HFU-2008, membrane material PVDF, pore diameter 0.01 μm) manufactured by Toray Industries, Inc., a single membrane module (single yarn module) was created. . Thereafter, the membrane was contaminated by passing water for industrial use (hereinafter referred to as “Yamakura Kosui”) in the Hara area of Goi City, Chiba Prefecture with the single-thread module water flow device shown in FIG.
 膜1は、上下両端をポッティング材よりなる保持部材3a,3bで保持されてカラム2内に配置されている。膜1の上端は保持部材3aに埋設されている。膜1の下端は保持部材3bを貫通してカラム2下部の室4に連通している。カラム2の下部(保持部材3bよりも上側)に配管5、ポンプ6及び弁7を介して山倉工水が供給され、透過水は、カラム2の下端の室4から弁8、配管9を介して流出する。濃縮水は、カラム2の上部(保持部材3a直下)から配管10、弁11を介して流出する。逆洗水は、配管12、ポンプ13及び弁14を介してカラム2の下端の室4内に導入され、膜2内に流入する。逆洗排水は、配管10から分岐した配管15、弁16を介して流出する。 The membrane 1 is arranged in the column 2 with its upper and lower ends held by holding members 3a and 3b made of a potting material. The upper end of the film 1 is embedded in the holding member 3a. The lower end of the membrane 1 passes through the holding member 3b and communicates with the chamber 4 below the column 2. Yamakura industrial water is supplied to the lower part of the column 2 (above the holding member 3b) via the pipe 5, the pump 6 and the valve 7, and the permeated water passes through the valve 8 and the pipe 9 from the chamber 4 at the lower end of the column 2. Leaked. The concentrated water flows out from the upper part of the column 2 (just 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 membrane 2. The backwash drainage flows out through the pipe 15 and the valve 16 branched from the pipe 10.
 膜汚染のための通水は、次の4工程を1サイクルとし、200サイクル繰り返すことにより行った。
 工程1:水張り(30秒)
 工程2:濾過(透過流束2~4m/m/d、28分)
 工程3:逆洗(水量0.6~1.4mL/min、30秒)
 工程4:排水(30秒)
Water flow for membrane contamination was performed by repeating the following four steps as one cycle and repeating 200 cycles.
Process 1: Water filling (30 seconds)
Step 2: Filtration (permeation flux 2-4 m 3 / m 2 / d, 28 minutes)
Step 3: Backwash (water volume 0.6-1.4 mL / min, 30 seconds)
Process 4: Drainage (30 seconds)
 汚染後の膜に純水を通水して透過流束4m/m/dにおける膜間差圧を測定し、洗浄前の膜間差圧値とした。その後、カラム2内に表1に示す洗浄液を導入して浸漬させた。所定時間浸漬させた後、薬液を排水し、純水でフラッシングした後に純水を通水して透過流束4m/m/dにおける膜間差圧を測定し、当該所定時間における膜間差圧値とした。膜間差圧測定後は、再度薬液を導入して、通算浸漬時間6~8時間まで操作を繰り返した。なお、薬液は導入の都度新しく調製した。膜間差圧値の測定結果(浸漬時間と膜間差圧値との関係)を図2に示す。なお、いずれの洗浄液もpH12、全塩素濃度約1200mgである。遊離塩素濃度はDPD法により測定した。 Pure water was passed through the contaminated membrane and the transmembrane differential pressure at a permeation flux of 4 m 3 / m 2 / d was measured to obtain the transmembrane differential pressure value before cleaning. Thereafter, the cleaning liquid shown in Table 1 was introduced into the column 2 and immersed therein. After soaking for a predetermined time, the chemical solution is drained, flushed with pure water, and then passed with pure water to measure a transmembrane differential pressure at a permeation flux of 4 m 3 / m 2 / d. The differential pressure value was used. After measuring the transmembrane pressure difference, the chemical solution was introduced again, and the operation was repeated until the total immersion time was 6 to 8 hours. The chemical solution was newly prepared for each introduction. The measurement result of the transmembrane pressure value (relation between the immersion time and the transmembrane pressure value) is shown in FIG. Each cleaning solution has a pH of 12 and a total chlorine concentration of about 1200 mg. Free chlorine concentration was measured by the DPD method.
Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001
[考察]
 比較例1の次亜塩素酸ナトリウムによる洗浄では、洗浄直後の差圧の低下が著しい(即効性が高い)が、最終到達差圧は比較例2~4の結合塩素剤よりも高く、洗浄効果は結合塩素剤に劣る。比較例2~4の結合塩素剤による洗浄では、洗浄の最終到達差圧が低く洗浄効果は高いが、洗浄の即効性において比較例1の次亜塩素酸ナトリウムに劣る。実施例1の洗浄液(結合塩素+遊離塩素剤)による洗浄では、次亜塩素酸ナトリウムと同等の即効性を示し、さらに結合塩素剤と同等の洗浄効果を兼ね備えている。
[Discussion]
In the cleaning with sodium hypochlorite in Comparative Example 1, the pressure difference immediately after cleaning is remarkably reduced (high immediate effect), but the final pressure difference is higher than the combined chlorine agent of Comparative Examples 2 to 4, and the cleaning effect Is inferior to bound chlorine. In the cleaning with the combined chlorine agent in Comparative Examples 2 to 4, the final ultimate differential pressure of the cleaning is low and the cleaning effect is high, but the cleaning immediate effect is inferior to that of the sodium hypochlorite of Comparative Example 1. The cleaning with the cleaning liquid of Example 1 (bonded chlorine + free chlorine agent) exhibits an immediate effect equivalent to that of sodium hypochlorite and also has the same cleaning effect as that of the combined chlorine agent.
[比較例5、実施例2~4]
 洗浄液を表2に示すものとしたこと以外は比較例1~4及び実施例1と同一条件にて膜の洗浄を行った。(ただし、実験日が比較例1~4及び実施例1とは異なるので、原水の水質が若干異なり、膜の汚染状況も若干異なる。)なお、いずれの洗浄液もpH12、全塩素濃度約1200mg-Cl/Lである。結果を図3に示す。
[Comparative Example 5, Examples 2 to 4]
The membrane was cleaned under the same conditions as in Comparative Examples 1 to 4 and Example 1 except that the cleaning solution was as shown in Table 2. (However, since the experimental date is different from Comparative Examples 1 to 4 and Example 1, the quality of the raw water is slightly different, and the state of contamination of the membrane is also slightly different.) All the cleaning solutions have a pH of 12 and a total chlorine concentration of about 1200 mg- Cl 2 / L. The results are shown in FIG.
Figure JPOXMLDOC01-appb-T000002
Figure JPOXMLDOC01-appb-T000002
[考察]
 実施例2~4は、比較例5の次亜塩素酸ナトリウムと同等の即効性を示し、かつ最終到達差圧において次亜塩素酸ナトリウムよりも低い膜間差圧(高い洗浄効果)を示した。
[Discussion]
Examples 2 to 4 showed an immediate effect equivalent to that of sodium hypochlorite of Comparative Example 5 and a lower transmembrane pressure difference (high cleaning effect) than sodium hypochlorite in the final ultimate pressure difference. .
[比較例6~8、実施例5]
 表3に示す洗浄剤を総塩素濃度1000mg-Cl/Lとなるように希釈し、pHをNaOHにより12に調整した洗浄液を調製した。
 また、薬液洗浄工程における通算浸漬時間を400minとした。これら以外は前記比較例及び実施例と同様の実験を行った。ただし、実験日が前記比較例及び実施例と異なるので、原水の水質が若干異なり、膜の汚染状況も若干異なる。
[Comparative Examples 6 to 8, Example 5]
The cleaning agent shown in Table 3 was diluted to a total chlorine concentration of 1000 mg-Cl 2 / L, and a cleaning solution was prepared in which the pH was adjusted to 12 with NaOH.
Further, the total immersion time in the chemical solution cleaning step was set to 400 min. Except these, the same experiment as the comparative example and the example was performed. However, since the experiment date is different from the comparative examples and examples, the quality of the raw water is slightly different, and the contamination of the membrane is also slightly different.
Figure JPOXMLDOC01-appb-T000003
Figure JPOXMLDOC01-appb-T000003
 図4に洗浄時間と差圧の関係を示す。実施例5の洗浄剤を希釈して調製した洗浄液が、最も差圧の下がり方が速く、到達差圧が低いことが分かる。比較例6は、到達差圧が高いままであり、比較例7、比較例8は、到達差圧は実施例5に近いが、差圧の下がり方が遅い。 Fig. 4 shows the relationship between cleaning time and differential pressure. It can be seen that the cleaning liquid prepared by diluting the cleaning agent of Example 5 has the fastest difference pressure drop and the lowest ultimate pressure difference. In Comparative Example 6, the ultimate differential pressure remains high. In Comparative Examples 7 and 8, the ultimate differential pressure is close to that of Example 5, but the method of decreasing the differential pressure is slow.
<実験例1~3>
 下記水溶液の殺菌効果の評価を行った。以下に示す剤を有効塩素が所定濃度になるように希釈して、評価菌と15min又は1h接触させ、生菌数を測定した。評価菌として、Aspergillus nigerを用いた。
実験例1:次亜塩素酸ナトリウム水溶液(有効塩素12%)
実験例2:スルファミン酸系結合塩素剤 Cl/N比=0.56 pH14.0の水溶液
実験例3:スルファミン酸系遊離塩素、結合塩素剤 Cl/N比=2.08 pH14.1の水溶液
<Experimental Examples 1-3>
The sterilizing effect of the following aqueous solutions was evaluated. The agent shown below was diluted so that effective chlorine might become a predetermined density | concentration, it was made to contact for 15 minutes or 1 h with evaluation microbe, and the number of viable bacteria was measured. Aspergillus niger was used as an evaluation bacterium.
Experimental example 1: Sodium hypochlorite aqueous solution (effective chlorine 12%)
Experimental example 2: Aqueous solution of sulfamic acid-based bound chlorine agent Cl 2 / N ratio = 0.56 pH 14.0 Experimental example 3: Sulfamic acid-based free chlorine, bound chlorine agent Cl 2 / N ratio = 2.08 of pH 14.1 Aqueous solution
 15minにおける結果を図5に示す。1hにおける結果を図6に示す。実験例1,3の場合は、有効塩素濃度10m/L、15minで、殺菌が完了するのに対して、実験例2の場合は、有効塩素200mg/L、1hでもほとんどの菌が生存していることが認められた。実験例1にも高い殺菌効果があるが、上記の比較例6と同じ薬剤であり、洗浄効果が劣っている。
 以上より、本発明の洗浄殺菌剤が、高い洗浄効果と殺菌効果を有していることが示された。
The result at 15 min is shown in FIG. The result in 1 h is shown in FIG. In Experimental Examples 1 and 3, sterilization is completed at an effective chlorine concentration of 10 m / L and 15 min, whereas in Experimental Example 2, most bacteria survive even at effective chlorine of 200 mg / L and 1 h. It was recognized that Although Experimental Example 1 also has a high bactericidal effect, it is the same agent as Comparative Example 6 described above and has a poor cleaning effect.
From the above, it was shown that the cleaning disinfectant of the present invention has a high cleaning effect and a disinfecting effect.
[塩素分解率の測定実験]
 スルファミン酸、次亜塩素酸ナトリウム水溶液(有効塩素12質量%)、48%水酸化ナトリウム、および純水を用いて表4に示す配合の洗浄剤を製造した。スルファミン酸の重量濃度は、2.5~5.0質量%である。配合(i)~(iv)で得られる洗浄剤のスルファミン酸モル濃度と残存する有効塩素モル濃度の関係、および塩素の分解率を図7に示す。図7の通り、スルファミン酸の重量濃度が高くなるほど、塩素の分解率が大きくなる。スルファミン酸の重量濃度が5.0質量%では、(有効塩素モル濃度)/(スルファミン酸モル濃度)の比は1.01と僅かに1を超える程度になる。従って、スルファミン酸の重量濃度は5.0質量%以下にすることが好ましい。塩素の分解率が大きくなる理由としては、不安定なジクロロスルファミン酸が出来易くなるためと推定される。
[Measurement experiment of chlorine decomposition rate]
A cleaning agent having the composition shown in Table 4 was produced using sulfamic acid, an aqueous sodium hypochlorite solution (effective chlorine 12% by mass), 48% sodium hydroxide, and pure water. The weight concentration of sulfamic acid is 2.5 to 5.0% by mass. FIG. 7 shows the relationship between the molar concentration of sulfamic acid and the residual effective molar concentration of chlorine in the detergents obtained by the formulations (i) to (iv), and the decomposition rate of chlorine. 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 mass%, the ratio of (effective chlorine molar concentration) / (sulfamic acid molar concentration) is 1.01, which is slightly over 1. Accordingly, the weight concentration of sulfamic acid is preferably 5.0% by mass or less. The reason why the decomposition rate of chlorine increases is presumably because unstable dichlorosulfamic acid is easily formed.
Figure JPOXMLDOC01-appb-T000004
Figure JPOXMLDOC01-appb-T000004
 本発明を特定の態様を用いて詳細に説明したが、本発明の意図と範囲を離れることなく様々な変更が可能であることは当業者に明らかである。
 本出願は、2017年3月15日付で出願された日本特許出願2017-050165に基づいており、その全体が引用により援用される。
Although the present invention has been described in detail using specific embodiments, it will be apparent to those skilled in the art that various modifications can be made without departing from the spirit and scope of the invention.
This application is based on Japanese Patent Application No. 2017-050165 filed on Mar. 15, 2017, which is incorporated by reference in its entirety.
 1 選択性透過膜
 2 カラム
1 Selective membrane 2 Column

Claims (12)

  1.  遊離塩素とクロラミン化合物とを含む洗浄液であって、全塩素とクロラミン化合物に由来する窒素原子Nのモル比(Cl/N)が1以上であり、pH9以上である接水部材の洗浄液。 A cleaning liquid containing a free chlorine and a chloramine compound, wherein the molar ratio (Cl 2 / N) of nitrogen atoms N derived from total chlorine and the chloramine compound is 1 or more and the pH is 9 or more.
  2.  前記クロラミン化合物として結合塩素型スルファミン酸およびその塩から選ばれる少なくとも1種のスルファミン酸系化合物を含む請求項1の洗浄液。 The cleaning liquid according to claim 1, comprising at least one sulfamic acid compound selected from bound chlorine type sulfamic acid and a salt thereof as the chloramine compound.
  3.  前記接水部材がMF膜、UF膜、濾過器、配管、圧力計及び流量計の少なくとも一つである請求項1又は2に記載の洗浄液。 The cleaning liquid according to claim 1 or 2, wherein the water contact member is at least one of an MF membrane, a UF membrane, a filter, a pipe, a pressure gauge, and a flow meter.
  4.  pH11以上である請求項1~3のいずれかに記載の洗浄液。 The cleaning liquid according to any one of claims 1 to 3, wherein the pH is 11 or more.
  5.  請求項1~4のいずれか1項において、クロラミン化合物と塩素の結合型塩素濃度が100mg/L以上、遊離塩素濃度が20mg/L以上であることを特徴とする洗浄液。 The cleaning liquid according to any one of claims 1 to 4, wherein the combined 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.
  6.  遊離塩素とクロラミン化合物とを含む洗浄剤であって、全塩素とクロラミン化合物に由来する窒素原子Nのモル比(Cl/N)が1以上であり、pH12以上である接水部材の洗浄剤。 A cleaning agent containing free chlorine and a chloramine compound, the cleaning agent for a water contact member having a molar ratio (Cl 2 / N) of nitrogen atoms N derived from total chlorine and a chloramine compound of 1 or more and a pH of 12 or more .
  7.  前記クロラミン化合物として結合塩素型スルファミン酸およびその塩から選ばれる少なくとも1種のスルファミン酸系化合物を含む請求項6の洗浄剤。 The cleaning agent according to claim 6, comprising at least one sulfamic acid compound selected from bound chlorine type sulfamic acid and a salt thereof as the chloramine compound.
  8.  スルファミン酸とアルカリ剤を混合した後、塩素剤を添加して結合塩素化合物を生成させることによって得られる請求項6又は7に記載の洗浄剤。 The cleaning agent according to claim 6 or 7, which is obtained by mixing a sulfamic acid and an alkali agent and then adding a chlorine agent to produce a combined chlorine compound.
  9.  最終的な洗浄剤の重量に対するスルファミン酸の濃度が5質量%以下である請求項7又は8に記載の洗浄剤。 The cleaning agent according to claim 7 or 8, wherein the concentration of sulfamic acid relative to the weight of the final cleaning agent is 5% by mass or less.
  10.  前記接水部材がMF膜、UF膜、濾過器、配管、圧力計及び流量計の少なくとも一つである請求項6~9のいずれかである洗浄剤。 The cleaning agent according to any one of claims 6 to 9, wherein the water contact member is at least one of an MF membrane, a UF membrane, a filter, a pipe, a pressure gauge, and a flow meter.
  11.  請求項6~9のいずれかの洗浄剤を水で希釈してなる、接水部材の洗浄液。 A cleaning solution for a water contact member, wherein the cleaning agent according to any one of claims 6 to 9 is diluted with water.
  12.  請求項1~5および請求項11のいずれかに記載の洗浄液を用いて接水部材を洗浄する接水部材の洗浄方法。 A method for cleaning a water contact member, wherein the water contact member is cleaned using the cleaning liquid according to any one of claims 1 to 5 and claim 11.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110449033A (en) * 2019-08-27 2019-11-15 湖北中泉环保技术有限公司 The cleaning method of ultrafiltration membrane surface organic sediment
CN114940906A (en) * 2022-05-13 2022-08-26 武汉汉烯科技有限公司 High-efficiency corrosive agent suitable for multiphase metal minerals and preparation method thereof

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07124559A (en) * 1993-11-08 1995-05-16 Toyobo Co Ltd Sterilization of water to be treated in seawater desalting process
JP2009195823A (en) * 2008-02-21 2009-09-03 Kurita Water Ind Ltd Method of controlling concentration of aqueous treating agent
JP2013010718A (en) * 2011-06-29 2013-01-17 Hakuto Co Ltd Slime release agent and method for releasing slime
WO2013179775A1 (en) * 2012-05-30 2013-12-05 栗田工業株式会社 Agent for cleaning permeation film, and cleaning method
JP2015097991A (en) * 2013-11-19 2015-05-28 栗田工業株式会社 Cleaning agent and cleaning method of permeable membrane
JP2016215125A (en) * 2015-05-20 2016-12-22 栗田工業株式会社 Cleaning liquid and cleaning method of polyamide type reverse osmotic membrane

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3832399B2 (en) * 2001-08-28 2006-10-11 栗田工業株式会社 Bactericidal algicide composition and water-based bactericidal algae method
WO2011125762A1 (en) * 2010-03-31 2011-10-13 栗田工業株式会社 Combined chlorine agent, and manufacturing method and method of use for same
TWI537046B (en) * 2011-07-06 2016-06-11 栗田工業股份有限公司 Method of membrane separation
WO2014208599A1 (en) * 2013-06-28 2014-12-31 三菱レイヨン株式会社 Method for cleaning filtration membrane
JP5892136B2 (en) * 2013-09-24 2016-03-23 栗田工業株式会社 Cooling water system algae killing method

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07124559A (en) * 1993-11-08 1995-05-16 Toyobo Co Ltd Sterilization of water to be treated in seawater desalting process
JP2009195823A (en) * 2008-02-21 2009-09-03 Kurita Water Ind Ltd Method of controlling concentration of aqueous treating agent
JP2013010718A (en) * 2011-06-29 2013-01-17 Hakuto Co Ltd Slime release agent and method for releasing slime
WO2013179775A1 (en) * 2012-05-30 2013-12-05 栗田工業株式会社 Agent for cleaning permeation film, and cleaning method
JP2015097991A (en) * 2013-11-19 2015-05-28 栗田工業株式会社 Cleaning agent and cleaning method of permeable membrane
JP2016215125A (en) * 2015-05-20 2016-12-22 栗田工業株式会社 Cleaning liquid and cleaning method of polyamide type reverse osmotic membrane

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110449033A (en) * 2019-08-27 2019-11-15 湖北中泉环保技术有限公司 The cleaning method of ultrafiltration membrane surface organic sediment
CN114940906A (en) * 2022-05-13 2022-08-26 武汉汉烯科技有限公司 High-efficiency corrosive agent suitable for multiphase metal minerals and preparation method thereof
CN114940906B (en) * 2022-05-13 2023-10-10 武汉汉烯科技有限公司 Efficient corrosive agent suitable for multiphase metal minerals and preparation method thereof

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