WO2023120350A1 - 水系の微生物汚染抑制方法 - Google Patents
水系の微生物汚染抑制方法 Download PDFInfo
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- WO2023120350A1 WO2023120350A1 PCT/JP2022/046153 JP2022046153W WO2023120350A1 WO 2023120350 A1 WO2023120350 A1 WO 2023120350A1 JP 2022046153 W JP2022046153 W JP 2022046153W WO 2023120350 A1 WO2023120350 A1 WO 2023120350A1
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- oxidizing agent
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- based oxidizing
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/76—Treatment of water, waste water, or sewage by oxidation with halogens or compounds of halogens
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/04—Feed pretreatment
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/06—Energy recovery
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/10—Accessories; Auxiliary operations
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/08—Prevention of membrane fouling or of concentration polarisation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2311/00—Details relating to membrane separation process operations and control
- B01D2311/04—Specific process operations in the feed stream; Feed pretreatment
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2311/00—Details relating to membrane separation process operations and control
- B01D2311/26—Further operations combined with membrane separation processes
- B01D2311/263—Chemical reaction
- B01D2311/2634—Oxidation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/76—Treatment of water, waste water, or sewage by oxidation with halogens or compounds of halogens
- C02F1/766—Treatment of water, waste water, or sewage by oxidation with halogens or compounds of halogens by means of halogens other than chlorine or of halogenated compounds containing halogen other than chlorine
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/18—Removal of treatment agents after treatment
- C02F2303/185—The treatment agent being halogen or a halogenated compound
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/20—Prevention of biofouling
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
Definitions
- the present invention relates to a method for suppressing microbial contamination of water systems.
- INDUSTRIAL APPLICABILITY The method for suppressing microbial contamination of a water system of the present invention is useful, for example, as a method for suppressing slime in a reverse osmosis (RO) membrane water supply system and preventing fouling of the reverse osmosis membrane.
- RO reverse osmosis
- RO membrane devices that can efficiently remove electrolytes and medium- and low-molecular-weight organic components are widely used.
- pretreatment such as pressure filtration equipment, gravity filtration equipment, coagulation sedimentation treatment equipment, pressure flotation filtration equipment, immersion membrane equipment, membrane pretreatment equipment, etc. is usually performed before the RO membrane equipment.
- a device is provided. After being pretreated by these pretreatment devices, the water to be treated is supplied to the RO membrane device and subjected to RO membrane separation treatment.
- microorganisms contained in the water to be treated proliferate in the pipes of the equipment and on the membrane surface to form slime. can cause
- a disinfectant In order to prevent contamination by microorganisms, it is common to add a disinfectant to the water to be treated constantly or intermittently to sterilize the water to be treated or the inside of the device while treating.
- a disinfectant a chlorine-based oxidizing agent such as sodium hypochlorite is used because it is inexpensive and relatively easy to handle.
- RO membranes generally do not have chlorine resistance like polyamide polymer membranes, when a chlorine-based oxidizing agent is added, free chlorine derived from the chlorine-based oxidizing agent causes oxidative deterioration and removal. rate will decline.
- a chlorine-based oxidizing agent is added on the upstream side of the water treatment device, and a reducing agent such as sodium bisulfite (SBS) is added on the inlet side of the RO membrane device to reduce and remove the remaining free chlorine.
- a reducing agent such as sodium bisulfite (SBS)
- SBS sodium bisulfite
- stabilized chlorine-based oxidizing agents such as chloramine and sodium chlorosulfamate, and stabilized bromine are added to suppress microbial contamination of the piping from the point of addition of the reducing agent to the inlet of the RO membrane device and the surface of the RO membrane.
- a slime control agent that suppresses the growth of microorganisms such as an oxidizing agent or an isothiazolone compound.
- stabilized chlorine-based oxidants and stabilized bromine-based oxidants have been widely used because they can suppress microbial contamination.
- Stabilized chlorine-based oxidizing agents and stabilized bromine-based oxidizing agents were found to exhibit the inhibitory effect more easily in some water systems and less so in some systems.
- SBS Sodium bisulfite
- Non-Patent Document 1 Sodium bisulfite (SBS), a reducing agent that is generally added to reduce free chlorine in the preceding stage of the RO membrane, is usually added in an excessive amount to reliably prevent membrane deterioration. SBS is known to damage films by reacting with heavy metals (Non-Patent Document 1).
- a reducing agent such as sodium bisulfite is added and a stabilized chlorine-based oxidizing agent and/or a bromine-based oxidizing agent comprising a chlorine-based oxidizing agent and a sulfamic acid compound are used in an aqueous system containing a residual reducing agent.
- An object of the present invention is to provide a method for suppressing microbial contamination of water systems, which can stably and effectively obtain the effect of suppressing microbial contamination by adding a stabilized brominated oxidizing agent comprising a sulfamic acid compound.
- the present inventors have proposed a stabilized chlorine-based oxidizing agent and/or stabilized bromine having a low sulfamic acid ratio (the ratio of the sulfamic acid compound to the effective chlorine amount of the chlorine-based oxidizing agent and/or the effective chlorine equivalent amount of the bromine-based oxidizing agent).
- a stabilized chlorine-based oxidizing agent and/or stabilized bromine having a low sulfamic acid ratio (the ratio of the sulfamic acid compound to the effective chlorine amount of the chlorine-based oxidizing agent and/or the effective chlorine equivalent amount of the bromine-based oxidizing agent).
- the gist of the present invention is as follows.
- a method for suppressing microbial contamination in a water system containing a reducing agent comprising a chlorine-based oxidizing agent and a sulfamic acid compound, wherein the ratio of the sulfamic acid compound to 1 mol of available chlorine of the chlorine-based oxidizing agent is 1 to 1.5 mol of a stabilized chlorine-based oxidizing agent and/or composed of a bromine-based oxidizing agent and a sulfamic acid compound, wherein the ratio of the sulfamic acid compound to 1 mol of the effective chlorine equivalent of the bromine-based oxidizing agent is 1
- the addition concentration of the stabilized chlorine-based oxidizing agent and/or the stabilized bromine-based oxidizing agent to the concentration of the reducing agent in the aqueous system is 2.5 times in molar ratio.
- a reducing agent such as sodium bisulfite is added to an aqueous system containing a residual reducing agent, and the addition of a stabilized chlorine-based oxidant and/or a stabilized bromine-based oxidant stably and effectively causes microbial contamination. can be suppressed.
- a reducing agent such as sodium bisulfite and heavy metals
- FIG. 1 is a graph showing the results of Example 1 and Comparative Example 1.
- FIG. 2 is a graph showing the results of Test Example 2.
- a method for suppressing microbial contamination of an aqueous system is a method for suppressing microbial contamination in an aqueous system containing a reducing agent, which comprises a chlorine-based oxidizing agent and a sulfamic acid compound, and the effective chlorine of the chlorine-based oxidizing agent is A stabilized chlorine-based oxidizing agent and/or a bromine-based oxidizing agent and sulfaamine, in which the ratio of the sulfamic acid compound to 1 mol (hereinafter sometimes referred to as "sulfamic acid ratio”) is 1 to 1.5 mol.
- a stabilized bromine-based oxidizing agent having a ratio of 1 to 1.5 mol of the sulfamic acid compound per 1 mol of effective chlorine equivalent of the bromine-based oxidizing agent with respect to the concentration of the reducing agent in the aqueous system.
- the stabilized chlorine-based oxidizing agent and/or the stabilized bromine-based oxidizing agent are added to the aqueous system in such a manner that the added concentration is 2.5 times or more in terms of molar ratio.
- a reducing agent such as sodium bisulfite (SBS) in water also reduces the stabilized chlorine-based oxidant and the stabilized bromine-based oxidant added later.
- SBS sodium bisulfite
- the stabilized chlorine-based oxidant consisting of the chlorine-based oxidant and the sulfamic acid compound and/or the stabilized bromine-based oxidant consisting of the bromine-based oxidant and the sulfamic acid compound release sulfamic acid.
- the higher the residual reducing agent concentration the higher the ratio of sulfamic acid to available chlorine in the system. As the ratio of sulfamic acid increases, the reactivity as a component decreases due to the equilibrium relationship.
- the effect of suppressing microbial contamination can be maintained even after reduction with a reducing agent such as sodium bisulfite. .
- a reducing agent such as sodium bisulfite.
- the water system to be treated in the present invention is not particularly limited as long as it contains a reducing agent.
- the present invention uses a reducing agent such as sodium bisulfite (SBS) in order to prevent oxidation deterioration of the RO membrane after a chlorine-based oxidant is added in the previous stage in a water treatment apparatus including an RO membrane apparatus.
- SBS sodium bisulfite
- sodium bisulfite As a reducing agent contained in the water system, sodium bisulfite (SBS) is typical, but sodium thiosulfate and the like may also be used.
- the reducing agent concentration in the aqueous system containing this residual reducing agent is preferably 0.01 mg/L-Cl 2 or more in order to effectively obtain the effects of the present invention, and this concentration is more preferably 0.1 mg. /L-Cl 2 or more.
- the concentration of the reducing agent is excessively high, the stabilized chlorine-based oxidizing agent and/or the stabilized bromine-based oxidizing agent that are added later are reduced accordingly, resulting in a higher required addition amount and an increase in treatment cost. Therefore, the reducing agent concentration in the water system to be treated is preferably 5 mg/L-Cl 2 or less, particularly 2 mg/L-Cl 2 or less.
- the concentration of the reducing agent is expressed in terms of free chlorine, that is, the concentration of free chlorine (mg/L-Cl 2 ) that can be reduced by the reducing agent at that concentration.
- the stabilized chlorine-based oxidant used in the present invention comprises a chlorine-based oxidant and a sulfamic acid compound.
- the stabilized brominated oxidant used in the present invention comprises a brominated oxidant and a sulfamic acid compound.
- chlorine-based oxidizing agent used in the stabilized chlorine-based oxidizing agent, and examples include chlorine gas, chlorine dioxide, hypochlorous acid or its salts, chlorous acid or its salts, chloric acid or its salts, and perchloric acid. or a salt thereof, chlorinated isocyanuric acid or a salt thereof.
- salt forms include alkali metal hypochlorites such as sodium hypochlorite and potassium hypochlorite; hypochlorites such as calcium hypochlorite and barium hypochlorite; acid alkaline earth metal salts; alkali metal chlorite salts such as sodium chlorite, potassium chlorite; alkaline earth metal chlorite salts such as barium chlorite; other chlorite salts such as nickel chlorite. acid metal salts; ammonium chlorate; alkali metal chlorates such as sodium chlorate and potassium chlorate; alkaline earth metal chlorates such as calcium chlorate and barium chlorate.
- hypochlorite can be preferably used because it is easy to handle.
- the brominated oxidizing agent used in the present invention is not particularly limited, and examples include liquid bromine, bromine chloride, bromic acid or salts thereof, hypobromous acid or salts thereof. These brominated oxidizing agents may be used alone or in combination of two or more.
- sulfamic acid compounds include compounds represented by the following general formula [1] or salts thereof.
- R 1 and R 2 are each independently a hydrogen atom or a hydrocarbon group having 1 to 8 carbon atoms.
- sulfamic acid compounds include sulfamic acid in which both R 1 and R 2 are hydrogen atoms, as well as N-methylsulfamic acid, N,N-dimethylsulfamic acid, and N-phenylsulfamic acid. be able to.
- the salts of the compounds include, for example, alkali metal salts such as sodium salts and potassium salts; alkaline earth metal salts such as calcium salts, strontium salts and barium salts; manganese salts and copper salts; salts, zinc salts, iron salts, cobalt salts, nickel salts and other metal salts; ammonium salts; and guanidine salts, specifically sodium sulfamate, potassium sulfamate, calcium sulfamate, Strontium sulfamate, barium sulfamate, iron sulfamate, zinc sulfamate and the like can be mentioned. Sulfamic acid and these sulfamates can be used singly or in combination of two or more.
- a chlorine-based oxidizing agent such as hypochlorite and/or a bromine-based oxidizing agent
- a sulfamic acid compound such as sulfamate
- these compounds combine to form chlorosulfamate and stabilize it. It is possible to maintain a stable concentration of free chlorine and/or free bromine in water without causing a difference in dissociation due to pH as with chloramine and resulting fluctuations in the concentration of free chlorine and/or free bromine.
- the ratio of the chlorine-based oxidizing agent and/or the bromine-based oxidizing agent to the sulfamic acid compound is sulfamine per 1 mol of the effective chlorine amount in terms of available chlorine of the chlorine-based oxidizing agent and/or the bromine-based oxidizing agent.
- the acid compound is preferably 1.0 to 5.0 mol, more preferably 1.0 to 2.5 mol.
- the stabilized sulfamic acid ratio is 1 to 1.5 mol, preferably 1 to 1.4 mol.
- a chlorine-based oxidant and/or a stabilized bromine-based oxidant is used.
- the sulfamic acid ratio exceeds 1.5 mol, the microbial contamination inhibiting effect of the present invention cannot be sufficiently obtained. If the sulfamic acid ratio is less than 1 mol, decomposition of sulfamic acid will occur during production.
- the chlorine-based oxidizing agent and/or the bromine-based oxidizing agent and the sulfamic acid compound may be added as a mixed aqueous solution or may be added separately.
- the stabilized chlorine-based oxidizing agent and/or the stabilized bromine-based oxidizing agent according to the present invention can be used in addition to the chlorine-based oxidizing agent and/or the bromine-based oxidizing agent and the sulfamic acid compound within a range that does not impair the effects thereof. It may contain ingredients. Other components include alkaline agents, azoles, anionic polymers, phosphonic acids and the like.
- the alkaline agent is used to stabilize the chlorine-based oxidizing agent and/or the bromine-based oxidizing agent in the stabilized chlorine-based oxidizing agent and/or the stabilized bromine-based oxidizing agent.
- Sodium hydroxide, potassium hydroxide and the like are usually used as the alkaline agent.
- the stabilized chlorine-based oxidizing agent and/or the stabilized bromine-based oxidizing agent are added.
- the addition concentration of the stabilized chlorine-based oxidizing agent and/or the stabilized bromine-based oxidizing agent is 2.5 times or more in molar ratio.
- the amount of the stabilized chlorine-based oxidant and/or the stabilized bromine-based oxidant to be added is at least the above lower limit, a good effect of suppressing microbial contamination can be obtained.
- the larger the amount of the stabilized chlorine-based oxidizing agent and/or the stabilized bromine-based oxidizing agent to be added the better in terms of the effect of suppressing microbial contamination, but on the other hand, the chemical cost increases. Therefore, the amount of the stabilized chlorine-based oxidizing agent and/or the stabilized bromine-based oxidizing agent to be added should be 2.5 to 10 times, particularly 2.5 to 5 times, the molar ratio of the concentration of the reducing agent in the aqueous system. It is preferable to add to
- Example 1 Comparative Example 1
- An experiment was conducted to examine the difference in the effect of suppressing microbial contamination depending on the sulfamic acid ratio (H 3 NSO 3 /Cl 2 molar ratio) of the stabilized chlorine-based oxidizing agent.
- the effect of suppressing microbial contamination was evaluated using the membrane fouling simulator described in Non-Patent Document 1, based on the degree of increase in differential pressure (pressure loss in the flow path).
- a substrate was added to raw water (water to be treated) to promote the biofouling effect of microorganisms.
- the raw water contains citric acid: 1.2 mg/L as C, ammonium chloride: 0.6 mg/L as N, and sodium dihydrogen phosphate: 0.2 mg/L as P as substrates.
- the added water was used as the water to be treated.
- the pH of raw water was 7-8.5.
- Test Example 1 Chemical 1 mixed with various concentrations of sodium bisulfite (SBS) in sample water was exposed for 2 hours to observe changes in ATP (adenosine triphosphate) in water. ATP is also called an organism's energy currency, and is used as an indicator of the amount of microorganisms.
- SBS sodium bisulfite
- the chemical treatment conditions are as shown in Table 2, and all were adjusted so that the residual chlorine concentration after reaction with sodium bisulfite was 1 mg/L-Cl 2 (Condition 1 was SBS-free).
- the sample water used was MF and UF treated water from a wastewater recovery system plant in the Kurita Development Center of Kurita Water Industries Ltd.
- ATP ATP measurement kit EnSure manufactured by Hygiena, and Aquasnap Free and Aquasnap Total were used.
- ATP a number obtained by subtracting the Free value from the Total value was used in order to capture the activity of microorganisms. Table 3 shows the results.
- the ATP concentration was effectively lowered, while in conditions 3 and 4, the extent of ATP decrease was smaller.
- the effect of suppressing microbial contamination is low with respect to the amount of SBS in condition 3, the effect of suppressing microbial contamination is sufficient under condition 2 even if SBS is added. From this, it can be seen that the addition concentration of the stabilized chlorine-based oxidizing agent to the reducing agent is preferably 2.5 times or more in molar ratio for the effect of suppressing microbial contamination.
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Abstract
Description
また、重亜硫酸ナトリウム等の還元剤と重金属との反応による膜劣化も防止することができ、円滑かつ良好な水処理を行える。
本発明者は、従来技術の課題を解決すべく検討した結果、以下の通り、水系に含まれる還元剤が安定化塩素系酸化剤や安定化臭素系酸化剤の微生物汚染抑制効果に影響を与えていることを知見した。
本発明における処理対象水系は、還元剤を含む水系であればよく特に制限はない。本発明は、前述の通り、RO膜装置を含む水処理装置において、前段で塩素系酸化剤が添加された後、RO膜の酸化劣化防止のために、重亜硫酸ナトリウム(SBS)等の還元剤が塩素系酸化剤に対して過剰に添加されることで還元剤が残留する(還元剤を含む)水系であって、その後の配管とRO膜の微生物汚染の抑制のために安定化塩素系酸化剤及び/又は安定化臭素系酸化剤が添加される水系、即ち、RO膜給水系に有効に適用される。
本発明で用いる安定化塩素系酸化剤は、塩素系酸化剤とスルファミン酸化合物とからなるものである。
本発明で用いる安定化臭素系酸化剤は、臭素系酸化剤とスルファミン酸化合物とからなるものである。
しかし、スルファミン酸比率の低い安定化塩素系酸化剤及び/又は安定化臭素系酸化剤を用いる本発明では、スルファミン酸比率が1~1.5モル、好ましくは1~1.4モルの安定化塩素系酸化剤及び/又は安定化臭素系酸化剤を用いる。この場合、スルファミン酸比率が1.5モルを超えると本発明による微生物汚染抑制効果を十分に得ることができない。スルファミン酸比率が1モル未満であると製造時にスルファミン酸の分解を招く。
アルカリ剤は、安定化塩素系酸化剤及び/又は安定化臭素系酸化剤中の塩素系酸化剤及び/又は臭素系酸化剤を安定化させるために用いられる。アルカリ剤としては、通常、水酸化ナトリウム、水酸化カリウム等が用いられる。
スルファミン酸比率の低い安定化塩素系酸化剤及び/又は安定化臭素系酸化剤を添加する本発明では、安定化塩素系酸化剤及び/又は安定化臭素系酸化剤は、水系の還元剤濃度に対する安定化塩素系酸化剤及び/又は安定化臭素系酸化剤の添加濃度がモル比で2.5倍以上となるように添加する。
安定化塩素系酸化剤及び/又は安定化臭素系酸化剤の添加量が上記下限以上であれば良好な微生物汚染抑制効果を得ることができる。安定化塩素系酸化剤及び/又は安定化臭素系酸化剤の添加量は多い程微生物汚染抑制効果の面では好ましいが、一方で薬品コストが嵩む。このため、安定化塩素系酸化剤及び/又は安定化臭素系酸化剤の添加量は水系の還元剤濃度に対してモル比で2.5~10倍、特に2.5~5倍となるように添加することが好ましい。
安定化塩素系酸化剤のスルファミン酸比率(H3NSO3/Cl2モル比)による微生物汚染の抑制効果の差異を調べる実験を行った。
微生物汚染抑制効果は、非特許文献1にある膜ファウリングシミュレータを用い、差圧(流路における圧力損失)上昇の程度に基づいて評価した。
原水のpHは7~8.5であった。
安定化塩素系酸化剤としては、実施例1では薬品1を、比較例1では薬品2を用いた。
結果を図1に示す。
両条件とも重亜硫酸ナトリウムが添加されるまでは差圧上昇を抑制できていたが、重亜硫酸ナトリウムを添加した後の挙動として、比較例1では差圧上昇を抑えられていないのに対して、実施例1では効果的に差圧を抑制できた。
スルファミン酸比率が高い薬品2は、重亜硫酸ナトリウムの添加により微生物汚染の抑制効果を失いやすい。これに対して、スルファミン酸比率が低い薬品1は、重亜硫酸ナトリウムの添加があっても微生物汚染の抑制効果を維持しやすいことが示された。
サンプル水中で種々濃度の重亜硫酸ナトリウム(SBS)と混合した薬品1を2時間曝露して水中のATP(アデノシン三リン酸)の変化を観察した。ATPは生物のエネルギー通貨とも呼ばれ、微生物量を示す指標として用いられる。薬品の処理条件は表2の通りであり、いずれも重亜硫酸ナトリウムとの反応後の残留塩素濃度が1mg/L-Cl2になるように調整した(ただし、条件1はSBS無添加)。
サンプル水は栗田工業社 クリタ開発センター内の排水回収系プラントのMF,UF処理水を用いた。
ATPはHygiena社製ATP測定キットEnSure及び、Aquasnap FreeとAquasnap Totalを用いた。なお、ATPは微生物の活性をとらえるために、Totalの値からFreeの値を引いた数字を用いた。
結果を表3に示す。
脱塩素野木町水水中で種々濃度の重亜硫酸ナトリウム(SBS)と混合した薬品1の酸化還元電位(ORP)を観察した。試験例1と同様にすべて重亜硫酸ナトリウムとの反応後の残留塩素濃度が1mg/L-Cl2になるように調整した。重亜硫酸ナトリウムに対する薬品1の塩素換算の添加量比で整理した結果を下記表4及び図2に示す。
本出願は、2021年12月20日付で出願された日本特許出願2021-205981に基づいており、その全体が引用により援用される。
Claims (5)
- 還元剤を含有する水系における微生物汚染を抑制する方法において、
塩素系酸化剤とスルファミン酸化合物とからなり、該塩素系酸化剤の有効塩素1モルに対する該スルファミン酸化合物の割合が1~1.5モルである安定化塩素系酸化剤、及び/又は、臭素系酸化剤とスルファミン酸化合物とからなり、該臭素系酸化剤の有効塩素換算量1モルに対する該スルファミン酸化合物の割合が1~1.5モルである安定化臭素系酸化剤を、
該水系の該還元剤濃度に対する該安定化塩素系酸化剤及び/又は安定化臭素系酸化剤の添加濃度がモル比で2.5倍以上となるように該水系に添加することを特徴とする水系の微生物汚染抑制方法。 - 前記水系が逆浸透膜給水系であることを特徴とする請求項1に記載の水系の微生物汚染抑制方法。
- 前記水系の還元剤濃度が0.01mg/L-Cl2以上であることを特徴とする請求項1又は2に記載の水系の微生物汚染抑制方法。
- 前記還元剤が重亜硫酸ナトリウムであることを特徴とする請求項1ないし3のいずれか1項に記載の水系の微生物汚染抑制方法。
- 前記水系の前記還元剤濃度に対する前記安定化塩素系酸化剤及び/又は安定化臭素系酸化剤の添加濃度がモル比で2.5~10倍となるように前記水系に添加することを特徴とする請求項1ないし4のいずれか1項に記載の水系の微生物汚染抑制方法。
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| EP22911058.0A EP4455097A4 (en) | 2021-12-20 | 2022-12-15 | METHOD FOR PREVENTING CONTAMINATION BY MICROORGANISMS IN A WATER SUPPLY SYSTEM |
| JP2023569360A JP7495017B2 (ja) | 2021-12-20 | 2022-12-15 | 水系の微生物汚染抑制方法 |
| KR1020247019248A KR20240125568A (ko) | 2021-12-20 | 2022-12-15 | 수계의 미생물 오염 억제 방법 |
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| KR20160143768A (ko) * | 2014-05-08 | 2016-12-14 | 오르가노 코포레이션 | 여과 처리 시스템 및 여과 처리 방법 |
| JP5967337B1 (ja) * | 2015-03-31 | 2016-08-10 | 栗田工業株式会社 | 逆浸透膜処理システムの運転方法及び逆浸透膜処理システム |
| JP7013141B2 (ja) | 2017-04-27 | 2022-02-15 | オルガノ株式会社 | 逆浸透膜を用いる水処理方法 |
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| JP7250612B2 (ja) * | 2018-12-27 | 2023-04-03 | オルガノ株式会社 | 水系の殺菌方法、および水系のニトロソアミン化合物の除去方法 |
| JP2020131134A (ja) | 2019-02-21 | 2020-08-31 | オルガノ株式会社 | 分離膜用スライム抑制剤、分離膜用スライム抑制剤の製造方法、および分離膜のスライム抑制方法 |
| JP7552938B2 (ja) * | 2021-12-20 | 2024-09-18 | 栗田工業株式会社 | 水系の微生物汚染抑制方法 |
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