JP2017205310A - Generation method and generation device for hypochlorous acid water - Google Patents

Generation method and generation device for hypochlorous acid water Download PDF

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JP2017205310A
JP2017205310A JP2016099981A JP2016099981A JP2017205310A JP 2017205310 A JP2017205310 A JP 2017205310A JP 2016099981 A JP2016099981 A JP 2016099981A JP 2016099981 A JP2016099981 A JP 2016099981A JP 2017205310 A JP2017205310 A JP 2017205310A
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hydrochloric acid
sodium hypochlorite
raw water
water
hypochlorous acid
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JP6667845B2 (en
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強 倉本
Tsutomu Kuramoto
強 倉本
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KOMORO NUNOBIKI STRAWBERRY FARM CO Ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40Mixing liquids with liquids; Emulsifying
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
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    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/50Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2/00Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
    • A61L2/16Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using chemical substances
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Abstract

PROBLEM TO BE SOLVED: To provide a generation device of hypochlorous acid water capable of generating hypochlorous acid water with predetermined pH and concentration by a simple structure without generating noxious gas.SOLUTION: In a generation device 1 of hypochlorous acid water, raw water is branched into first and second branch pipe paths 3 and 4. A sodium hypochlorite solution of predetermined concentration is intermittently supplied by a fixed quantity to raw water flowing in the first branch pipe path 3 by using a first metering pump 31, stirred and mixed through a first disc filter 41 and uniform diluted aqueous solution of sodium hypochlorite is obtained. Hydrochloric acid is intermittently supplied by a fixed quantity to raw water flowing in the second branch pipe path 3 by using a second metering pump 32, stirred and mixed through a second disc filter 42 and uniform diluted hydrochloric acid is obtained. By stirring and mixing the diluted solution of sodium hypochlorite and the diluted hydrochloric acid through a third disc filter 43, hypochlorous acid water with predetermined concentration and pH is generated.SELECTED DRAWING: Figure 1

Description

本発明は、水道水などの原水に、次亜塩素酸ナトリウム水溶液および塩酸を混合して所定濃度、pHの次亜塩素酸水を生成する次亜塩素酸水の生成方法および生成器に関する。   The present invention relates to a hypochlorous acid water generation method and a generator for mixing hypochlorous acid water having a predetermined concentration and pH by mixing sodium hypochlorite aqueous solution and hydrochloric acid with raw water such as tap water.

植物などの殺菌水として次亜塩素酸水を用いることが知られている。本発明者は、特許文献1において、次亜塩素酸水を用いた植物の洗浄農法を提案している。例えば、次亜塩素酸水を用いた洗浄農法をイチゴ苗の栽培に適用することにより、イチゴの炭そ病感染などを確実に防止できる。   It is known to use hypochlorous acid water as sterilizing water for plants and the like. The present inventor has proposed a plant cleaning farming method using hypochlorous acid water in Patent Document 1. For example, by applying a cleaning farming method using hypochlorous acid water to cultivation of strawberry seedlings, strawberry anthracnose infection can be reliably prevented.

次亜塩素酸水の生成方法としては、電解法および二液法が知られている。農業などにおいて殺菌水として次亜塩素酸水を用いる場合には電解法では生成量が不足するので、二液法が採用される。   As a method for producing hypochlorous acid water, an electrolytic method and a two-component method are known. When hypochlorous acid water is used as sterilizing water in agriculture or the like, the amount produced is insufficient in the electrolytic method, so the two-component method is adopted.

特許文献2には、二液法により次亜塩素酸水を生成する殺菌水製造装置が提案されている。この殺菌水製造装置では、原水に次亜塩素酸ナトリウム水溶液と塩酸を添加して、所定のpH値、所定の残留塩素濃度の次亜塩素酸水を生成している。   Patent Document 2 proposes a sterilizing water production apparatus that generates hypochlorous acid water by a two-component method. In this sterilizing water manufacturing apparatus, sodium hypochlorite aqueous solution and hydrochloric acid are added to raw water to generate hypochlorous acid water having a predetermined pH value and a predetermined residual chlorine concentration.

特許第5866147号公報Japanese Patent No. 5866147 特許第3719589号公報Japanese Patent No. 3719589

ここで、次亜塩素酸ナトリウムは塩酸と反応して有毒な塩素ガスが発生する。このため、特許文献2に開示の殺菌水製造装置では、次亜塩素酸ナトリウムおよび塩酸を、それぞれ別個に原水によって希釈し、希釈後の次亜塩素酸ナトリウム水溶液と希釈塩酸を混合することにより、有毒ガスの発生を抑制している。また、配管経路を上流側から下流側に向けて垂直方向の下方に向かうように配置して、運転中断状態、停止状態などにおいて次亜塩素酸ナトリウム水溶液と塩酸とが接触して有毒ガスが発生することを回避すると共に配管経路からのガス抜きを容易にしている。   Here, sodium hypochlorite reacts with hydrochloric acid to generate toxic chlorine gas. For this reason, in the sterilizing water production apparatus disclosed in Patent Document 2, sodium hypochlorite and hydrochloric acid are separately diluted with raw water, and the diluted sodium hypochlorite aqueous solution and diluted hydrochloric acid are mixed, Controls the generation of toxic gases. In addition, the piping route is arranged so as to be directed downward in the vertical direction from the upstream side to the downstream side, and toxic gas is generated when sodium hypochlorite aqueous solution and hydrochloric acid come into contact with each other when the operation is interrupted or stopped. This makes it easy to vent the gas from the piping path.

特許文献2に開示の殺菌水製造装置などの従来の二液法による次亜塩素酸水の生成器は、次亜塩素酸ナトリウム、塩酸を原水に供給(添加)するために一般的なターボ型ポンプ(非容積型ポンプ)を用いている。ポンプを駆動して、タンクに貯留されている次亜塩素酸ナトリウム、塩酸を、ポンプを経由する配管経路を通して原水に供給している。運転停止時には、配管経路内に残留する次亜塩素酸ナトリウム、塩酸を、配管経路を含む循環経路を介してタンクに戻すようにしている。   A conventional hypochlorite water generator by a two-component method such as a sterilizing water production apparatus disclosed in Patent Document 2 is a general turbo type for supplying (adding) sodium hypochlorite and hydrochloric acid to raw water. A pump (non-volumetric pump) is used. The pump is driven, and sodium hypochlorite and hydrochloric acid stored in the tank are supplied to the raw water through a piping path passing through the pump. When the operation is stopped, sodium hypochlorite and hydrochloric acid remaining in the piping path are returned to the tank via the circulation path including the piping path.

従来における次亜塩素酸水の生成器では、原水によって希釈される前の次亜塩素酸ナトリウム、塩酸を、ポンプおよび配管経路に沿って流している。これらの薬液によってポンプ内部、配管などの劣化が早く、寿命が短いという問題がある。また、従来の二液法による生成器では、必要されるpH値あるいは残留塩素濃度の次亜塩素酸水を精度良く生成することが困難である。さらには、特許文献2に記載されているように、配管経路を垂直に配置しなければならない等の機器レイアウト上の制約もある。このような理由により、今まで、二液法による次亜塩素酸水の生成器は殆ど実用化されていないのが現状である。   In a conventional hypochlorous acid water generator, sodium hypochlorite and hydrochloric acid before being diluted with raw water flow along a pump and a piping path. There is a problem that the inside of the pump, piping, and the like are rapidly deteriorated by these chemical solutions, and the life is short. In addition, it is difficult to accurately generate hypochlorous acid water having a required pH value or residual chlorine concentration with a conventional two-component generator. Furthermore, as described in Patent Document 2, there is a restriction on the equipment layout such that the piping route must be arranged vertically. For these reasons, the generator of hypochlorous acid water by the two-component method has not been put to practical use until now.

本発明の課題は、簡単な構成により、所定のpH値、濃度の次亜塩素酸水を有毒ガスを発生させることなく生成可能な次亜塩素酸水の生成方法および生成器を提供することにある。   An object of the present invention is to provide a hypochlorous acid water generating method and generator capable of generating hypochlorous acid water having a predetermined pH value and concentration without generating a toxic gas with a simple configuration. is there.

上記の課題を解決するために、本発明の次亜塩素酸水の生成方法は、
所定の圧力で供給される原水流を形成し、
前記原水流を第1、第2分岐流に分岐させ、
第1分岐流に、第1定量ポンプを用いて、第1薬液タンクに貯留されている予め設定された濃度の次亜塩素酸ナトリウム水溶液を、所定量ずつ断続的に供給し、
次亜塩素酸ナトリウム水溶液が供給された後の前記第1分岐流を攪拌混合して、次亜塩素酸ナトリウムの均一な希釈水溶液流を生成し、
第2分岐流に、第2定量ポンプを用いて、第2薬液タンクに貯留されている予め設定された濃度の塩酸を所定量ずつ断続的に供給し、
塩酸が供給された後の前記第2分岐流を攪拌混合して均一な希釈塩酸流を生成し、
次亜塩素酸ナトリウムの希釈水溶液流と希釈塩酸流とを合流させた後に、攪拌混合して、所定濃度およびpHの次亜塩素酸水を生成し、
生成される次亜塩素酸水の濃度およびpHの制御を、供給される原水流量を計測し、計測結果に基き、前記第1、第2定量ポンプによる次亜塩素酸ナトリウム水溶液および塩酸の供給量を増減することにより行うことを特徴としている。
In order to solve the above problems, the method for producing hypochlorous acid water of the present invention is as follows.
Forming a raw water stream supplied at a given pressure,
Branching the raw water stream into first and second branch streams;
Using a first metering pump, a predetermined concentration of sodium hypochlorite aqueous solution stored in the first chemical liquid tank is intermittently supplied to the first branch flow by a predetermined amount,
Stirring and mixing the first branched stream after the aqueous sodium hypochlorite solution is supplied to produce a uniform diluted aqueous stream of sodium hypochlorite;
The second branch flow is intermittently supplied with a predetermined amount of hydrochloric acid stored in the second chemical tank by a predetermined amount using a second metering pump,
Stirring and mixing the second branched stream after the hydrochloric acid is fed to produce a uniform diluted hydrochloric acid stream;
A dilute aqueous sodium hypochlorite stream and a dilute hydrochloric acid stream are combined and mixed by stirring to produce hypochlorous acid water having a predetermined concentration and pH,
Control the concentration and pH of the generated hypochlorous acid water, measure the flow rate of the supplied raw water, and supply the sodium hypochlorite aqueous solution and hydrochloric acid by the first and second metering pumps based on the measurement results It is characterized by being performed by increasing / decreasing the value.

また、本発明の次亜塩素酸水の生成器は、
上流側管路と、
前記上流側管路の下流端から分岐して再び合流する第1分岐管路および第2分岐管路と、
前記第1、第2分岐管路の下流端の合流点から延びている下流側管路と、
原水を、前記上流側管路から前記第1、第2分岐管路のそれぞれを経由して前記下流側管路に圧送する原水供給ポンプと、
予め設定した濃度の次亜塩素酸ナトリウム水溶液を貯留する第1薬液タンクと、
予め設定した濃度の塩酸を貯留する第2薬液タンクと、
前記第1分岐管路を流れる原水に、前記第1薬液タンクから次亜塩素酸ナトリウム水溶液を所定量ずつ断続的に供給する第1定量ポンプと、
前記第2分岐管路を流れる原水に、前記第2薬液タンクから塩酸を所定量ずつ断続的に供給する第2定量ポンプと、
前記第1分岐管路の途中において、次亜塩素酸ナトリウム水溶液が供給された後の原水を攪拌混合する第1攪拌混合器と、
前記第2分岐管路の途中において、塩酸が供給された後の原水を攪拌混合する第2攪拌混合器と、
前記下流側管路を流れる次亜塩素酸ナトリウムの希釈水溶液および希釈塩酸を攪拌混合する第3攪拌混合器と、
を有していることを特徴としている。
The generator of hypochlorous acid water of the present invention is
An upstream pipeline,
A first branch pipe and a second branch pipe branching from the downstream end of the upstream pipe and joining again;
A downstream pipe line extending from a confluence of the downstream ends of the first and second branch pipe lines;
A raw water supply pump for pumping raw water from the upstream pipeline to the downstream pipeline via each of the first and second branch pipelines;
A first chemical tank for storing a sodium hypochlorite aqueous solution having a preset concentration;
A second chemical tank for storing hydrochloric acid having a preset concentration;
A first metering pump that intermittently supplies a predetermined amount of sodium hypochlorite aqueous solution from the first chemical solution tank to the raw water flowing through the first branch pipe;
A second metering pump that intermittently supplies hydrochloric acid from the second chemical tank to the raw water flowing through the second branch pipe by a predetermined amount;
In the middle of the first branch pipe, a first stirring mixer that stirs and mixes raw water after the sodium hypochlorite aqueous solution is supplied;
In the middle of the second branch pipe, a second stirring mixer that stirs and mixes raw water after hydrochloric acid is supplied;
A third stirring mixer for stirring and mixing a diluted aqueous solution of sodium hypochlorite and diluted hydrochloric acid flowing through the downstream side pipe;
It is characterized by having.

本発明において、溝の入ったディスクの積層体をろ過部分として備えたディスクフィルタを攪拌混合器として用いることが望ましい。   In the present invention, it is desirable to use as a stirring mixer a disc filter provided with a laminated body of discs having grooves as a filtration part.

本発明では、定量ポンプ、例えば、ダイヤフラム型定量ポンプを用いて、次亜塩素酸ナトリウム水溶液および塩酸を原水に供給している。定量ポンプによって原水に供給される次亜塩素酸水溶液、塩酸の量を正確に制御することができる。これにより、予め設定したpH値あるいは残留塩素濃度の次亜塩素酸水を確実に得ることができる。   In the present invention, a sodium hypochlorite aqueous solution and hydrochloric acid are supplied to raw water using a metering pump, for example, a diaphragm metering pump. The amount of hypochlorous acid aqueous solution and hydrochloric acid supplied to the raw water by the metering pump can be accurately controlled. Thereby, hypochlorous acid water having a preset pH value or residual chlorine concentration can be obtained with certainty.

また、次亜塩素酸ナトリウム水溶液、塩酸が流れる定量ポンプのポンプ室内には、ターボ型ポンプのようなロータ、その軸受などの駆動部分が無いので、これらの水溶液によってポンプが劣化して寿命が短くなる可能性もない。さらに、運転停止後などにおいて、配管内に濃度の高い次亜塩素酸ナトリウム、塩酸が残留することがなく、希釈されたものが僅かの量で混合攪拌器内に残るだけである。よって、有毒ガスが発生せず、また、基本的にガス抜き機構も不要である。   In addition, there are no drive parts such as a turbo type pump rotor and its bearings in the pump chamber of a metering pump through which sodium hypochlorite aqueous solution and hydrochloric acid flow. Therefore, these aqueous solutions deteriorate the pump and shorten its life. There is no possibility of becoming. Further, after the operation is stopped, high concentration sodium hypochlorite and hydrochloric acid do not remain in the pipe, and only a small amount of the diluted one remains in the mixing stirrer. Therefore, no toxic gas is generated and a gas venting mechanism is basically unnecessary.

さらには、配管経路のレイアウトの自由度が高く、従来のように、上流から下流に向かって垂直方向に配管しなければならないなどの制約も少ない。箱型などの定まった形状の筐体内に、配管などの構成部品を簡単に組み込むことができる。よって、本発明によれば、実用的な二液法による次亜塩素酸水の生成器を実現できる。   Furthermore, there is a high degree of freedom in the layout of the piping path, and there are few restrictions such as having to pipe in the vertical direction from upstream to downstream as in the prior art. Components such as piping can be easily incorporated into a box having a fixed shape such as a box shape. Therefore, according to this invention, the generator of hypochlorous acid water by a practical two-component method is realizable.

本発明を適用した次亜塩素酸水の生成器の概略構成を示す説明図である。It is explanatory drawing which shows schematic structure of the generator of hypochlorous acid water to which this invention is applied.

以下に、図面を参照して本発明を適用した次亜塩素酸水の生成器の実施の形態を説明する。図1は、次亜塩素酸水の生成器の概略構成を示す説明図である。次亜塩素酸水の生成器1は、水道水などの原水の配管経路として、上流側管路2と、この上流側管路2の下流端から二股に分岐して延びる第1分岐管路3および第2分岐管路4と、これら第1、第2分岐管路3、4の下流端の合流点5から延びている下流側管路6とを備えている。例えば、40mm径の硬質塩化ビニル管が用いられる。この構成の配管経路が、図1において二点鎖線で示す生成器筐体7の内部に組み込まれている。   Hereinafter, embodiments of a hypochlorous acid water generator to which the present invention is applied will be described with reference to the drawings. FIG. 1 is an explanatory diagram showing a schematic configuration of a hypochlorous acid water generator. The hypochlorous acid water generator 1 includes an upstream pipe 2 and a first branch pipe 3 that branches from the downstream end of the upstream pipe 2 and branches as raw water pipes such as tap water. And a second branch pipe 4 and a downstream pipe 6 extending from the junction 5 at the downstream end of the first and second branch pipes 3 and 4. For example, a hard vinyl chloride pipe having a diameter of 40 mm is used. The piping path having this configuration is incorporated in the generator housing 7 indicated by a two-dot chain line in FIG.

上流側管路2には、給水ポンプ8、開閉弁9、減圧弁10および流量計11が、上流側からこの順序で配置されている。給水ポンプ8によって、水道水などの原水が、上流側管路2から第1、第2分岐管路3、4のそれぞれを経由して下流側管路6に圧送される。流量計11によって、圧送される原水の流量が計測される。   A water supply pump 8, an on-off valve 9, a pressure reducing valve 10, and a flow meter 11 are arranged in this order from the upstream side in the upstream side pipeline 2. Raw water such as tap water is pumped from the upstream pipeline 2 to the downstream pipeline 6 via the first and second branch pipelines 3 and 4 by the water supply pump 8. The flow meter 11 measures the flow rate of the raw water being pumped.

また、次亜塩素酸水の生成器1は、第1薬液タンク21、第2薬液タンク22および第3薬液タンク23を備えている。これらのタンク容量は例えば200リットルである。第1薬液タンク21には、予め設定した濃度、例えば、濃度4%の次亜塩素酸ナトリウム水溶液が貯留され、第2薬液タンク22には、予め設定した濃度、例えば濃度4%の塩酸が貯留される。また、第3薬液タンク23には、生成された次亜塩素酸水が貯留され、ここから、殺菌あるいは消毒対象の植物などに次亜塩素酸水を供給可能である。これら第1〜第3薬液タンク21〜23は、外付けのタンクであってもよいし、内蔵のタンクであってもよい。   The hypochlorous acid water generator 1 includes a first chemical liquid tank 21, a second chemical liquid tank 22, and a third chemical liquid tank 23. These tank capacities are, for example, 200 liters. The first chemical tank 21 stores a preset concentration, for example, 4% sodium hypochlorite aqueous solution, and the second chemical tank 22 stores a preset concentration, for example, 4% hydrochloric acid. Is done. Moreover, the produced | generated hypochlorous acid water is stored in the 3rd chemical | medical solution tank 23, and it can supply hypochlorous acid water to the plant etc. which are sterilization or disinfection from here. These first to third chemical liquid tanks 21 to 23 may be external tanks or built-in tanks.

さらに、次亜塩素酸水の生成器1は、第1定量ポンプ31および第2定量ポンプ32を備えている。これらの第1、第2定量ポンプ31、32は例えば電磁駆動式のダイヤフラム型定量ポンプであり、ダイヤフラムを所定ストロークで変位させることにより、ポンプ室容積を増減させ、所定量の液体を断続的に繰り返し吐出可能である。   Further, the hypochlorous acid water generator 1 includes a first metering pump 31 and a second metering pump 32. These first and second metering pumps 31 and 32 are, for example, electromagnetically driven diaphragm metering pumps, and by displacing the diaphragm with a predetermined stroke, the pump chamber volume is increased or decreased, and a predetermined amount of liquid is intermittently supplied. Repeated discharge is possible.

第1定量ポンプ31は、その吸入口31aが第1薬液タンク21に連通し、その吐出口31bが第1分岐管路3の途中位置に連通している。第1定量ポンプ31を駆動することによって、第1分岐管路3を流れる原水に、第1薬液タンク21から次亜塩素酸ナトリウム水溶液を所定量ずつ断続的に供給(添加)することができる。   The first metering pump 31 has a suction port 31 a communicating with the first chemical liquid tank 21, and a discharge port 31 b communicating with a middle position of the first branch pipe 3. By driving the first metering pump 31, the sodium hypochlorite aqueous solution can be intermittently supplied (added) from the first chemical liquid tank 21 to the raw water flowing through the first branch pipe 3 by a predetermined amount.

第2定量ポンプ32は、その吸入口32aが第2薬液タンク22に連通し、その吐出口
32bが第2分岐管路4の途中位置に連通している。第2定量ポンプ32を駆動することによって、第2分岐管路4を流れる原水に、第2薬液タンク22から塩酸を所定量ずつ断続的に供給(添加)することができる。
The second metering pump 32 has a suction port 32 a communicating with the second chemical liquid tank 22, and a discharge port 32 b communicating with a middle position of the second branch pipe 4. By driving the second metering pump 32, hydrochloric acid can be intermittently supplied (added) from the second chemical liquid tank 22 to the raw water flowing through the second branch pipe 4 by a predetermined amount.

第1分岐管路3において、第1定量ポンプ31の吐出口31bに連通している部位と、その下流端の合流点5との間には、第1ディスクフィルタ41が配置されている。次亜塩素酸ナトリウム水溶液が供給された後の原水は、第1ディスクフィルタ41を通って流れる間に攪拌混合されて、均一な希釈水溶液となって下流側に流れる。希釈倍率は、例えば、400倍(100ppm)〜4000倍(10ppm)である。   In the first branch pipe 3, a first disk filter 41 is disposed between a portion communicating with the discharge port 31 b of the first metering pump 31 and the junction 5 at the downstream end thereof. The raw water after the sodium hypochlorite aqueous solution is supplied is stirred and mixed while flowing through the first disk filter 41, and becomes a uniform diluted aqueous solution and flows downstream. The dilution factor is, for example, 400 times (100 ppm) to 4000 times (10 ppm).

第2分岐管路4の途中において、第2定量ポンプ32の吐出口32bに連通している部位と、その下流端の合流点5との間には、第2ディスクフィルタ42が配置されている。塩酸が供給された後の原水は、第2ディスクフィルタ42を通って流れる間に攪拌混合されて、均一な希釈塩酸となって下流側に流れる。希釈倍率は、例えば、400倍(100ppm)〜4000倍(10ppm)である。   In the middle of the second branch pipe 4, a second disk filter 42 is disposed between a portion communicating with the discharge port 32 b of the second metering pump 32 and the junction 5 at the downstream end thereof. . The raw water after the hydrochloric acid is supplied is stirred and mixed while flowing through the second disk filter 42, and becomes uniform diluted hydrochloric acid and flows downstream. The dilution factor is, for example, 400 times (100 ppm) to 4000 times (10 ppm).

下流側管路6には、第1分岐管路3から次亜塩素酸ナトリウムの希釈水溶液が供給され、第2分岐管路4から希釈塩酸が供給される。また、下流側管路6には第3ディスクフィルタ43が配置されている。次亜塩素酸ナトリウムの希釈水溶液および希釈塩酸は、第3ディスクフィルタ43を通って流れる間に攪拌混合される。これにより、所定のpH値あるいは所定の残留塩素濃度の次亜塩素酸水が生成される。生成された次亜塩素酸水は、開閉弁12を介して、第3薬液タンク23に一時的に貯留され、ここから、散布対象の植物などへ供給される。例えば、第1〜第3ディスクフィルタの容量は5リットル以上とされる。   A diluted aqueous solution of sodium hypochlorite is supplied from the first branch pipe 3 to the downstream side pipe 6, and diluted hydrochloric acid is supplied from the second branch pipe 4. A third disk filter 43 is disposed in the downstream pipe line 6. The dilute aqueous solution of sodium hypochlorite and dilute hydrochloric acid are stirred and mixed while flowing through the third disk filter 43. Thereby, hypochlorous acid water having a predetermined pH value or a predetermined residual chlorine concentration is generated. The produced hypochlorous acid water is temporarily stored in the third chemical liquid tank 23 via the on-off valve 12, and is supplied from here to a plant to be spread. For example, the capacity of the first to third disk filters is 5 liters or more.

次亜塩素酸水の生成器1には制御盤50が配置されている。制御盤50は各部の駆動制御を司る。例えば、生成される次亜塩素酸水のpH値、残留塩素濃度が設定値となるように制御するために、流量計11による計測結果に基き、第1定量ポンプ31による次亜塩素酸ナトリウム水溶液の供給量および第2定量ポンプ32による塩酸の供給量を増減する。   A control panel 50 is disposed in the hypochlorous acid water generator 1. The control panel 50 controls the drive of each part. For example, in order to control the pH value and residual chlorine concentration of the generated hypochlorous acid water to be set values, the sodium hypochlorite aqueous solution by the first metering pump 31 is based on the measurement result by the flow meter 11. The supply amount of hydrochloric acid and the supply amount of hydrochloric acid by the second metering pump 32 are increased or decreased.

本例では、制御盤50はパルス変換器51を備えており、流量計11によって計測された原水流量を表す流量パルスに基き、必要とされる次亜塩素酸ナトリウム水溶液の量に対応するパルス信号、および、必要とされる塩酸の量に対応するパルス信号を生成する。これらのパルス信号に基き、第1、第2定量ポンプ31、32をパルス駆動する。具体的には、パルス数に対応する回数だけダイヤフラムを駆動して、必要量の薬液を第1、第2分岐管路3、4に供給する。   In this example, the control panel 50 includes a pulse converter 51, and a pulse signal corresponding to the required amount of aqueous sodium hypochlorite solution based on the flow rate pulse representing the raw water flow rate measured by the flow meter 11. And a pulse signal corresponding to the amount of hydrochloric acid required. Based on these pulse signals, the first and second metering pumps 31 and 32 are pulse-driven. Specifically, the diaphragm is driven a number of times corresponding to the number of pulses, and a necessary amount of chemical solution is supplied to the first and second branch pipes 3 and 4.

以上説明したように、本例の次亜塩素酸水の生成器1では、原水を第1、第2分岐管路3、4に分岐させている。第1分岐管路3を流れる原水に、第1定量ポンプ31を用いて、所定濃度の次亜塩素酸ナトリウム水溶液を定量ずつ断続的に供給し、第1ディスクフィルタ41を通して攪拌混合して、次亜塩素酸ナトリウムの均一な希釈水溶液を得ている。これと並行して、第2分岐管路を流れる原水に、第2定量ポンプ32を用いて所定濃度の塩酸を定量ずつ断続的に供給し、第2ディスクフィルタ42に通して攪拌混合して均一な希釈塩酸を得ている。得られた次亜塩素酸ナトリウムの希釈水溶液と希釈塩酸とを混合して、第3ディスクフィルタ43に通して攪拌混合している。これにより、所定濃度およびpHの次亜塩素酸水が生成される。   As described above, in the hypochlorous water generator 1 of this example, the raw water is branched into the first and second branch pipes 3 and 4. A predetermined amount of sodium hypochlorite aqueous solution is intermittently supplied to the raw water flowing through the first branch pipe 3 by a first metering pump 31, stirred and mixed through the first disk filter 41, and then A homogeneous diluted aqueous solution of sodium chlorite is obtained. In parallel with this, a predetermined amount of hydrochloric acid is intermittently supplied to the raw water flowing through the second branch pipe using the second metering pump 32, and the mixture is stirred and mixed uniformly through the second disk filter 42. Diluted hydrochloric acid is obtained. The obtained dilute aqueous solution of sodium hypochlorite and dilute hydrochloric acid are mixed and passed through the third disk filter 43 and stirred and mixed. Thereby, hypochlorous acid water having a predetermined concentration and pH is generated.

1 次亜塩素酸水の生成器
2 上流側管路
3 第1分岐管路
4 第2分岐管路
5 合流点
6 下流側管路
7 生成器筐体
8 給水ポンプ
9 開閉弁
10 減圧弁
11 流量計
12 開閉弁
21 第1薬液タンク
22 第2薬液タンク
23 第3薬液タンク
31 第1定量ポンプ
31a 吸入口
31b 吐出口
32 第2定量ポンプ
32a 吸入口
32b 吐出口
41 第1ディスクフィルタ
42 第2ディスクフィルタ
43 第3ディスクフィルタ
50 制御盤
51 パルス変換器
Primary chlorite water generator 2 Upstream line 3 First branch line 4 Second branch line 5 Junction point 6 Downstream line 7 Generator housing 8 Water supply pump 9 On-off valve 10 Pressure reducing valve 11 Flow rate Total 12 On-off valve 21 First chemical tank 22 Second chemical tank 23 Third chemical tank 31 First metering pump 31a Suction port 31b Discharge port 32 Second metering pump 32a Suction port 32b Discharge port 41 First disk filter 42 Second disk Filter 43 Third disk filter 50 Control panel 51 Pulse converter

Claims (4)

所定の圧力で供給される原水流を形成し、
前記原水流を第1、第2分岐流に分岐させ、
第1分岐流に、第1定量ポンプを用いて、第1薬液タンクに貯留されている予め設定された濃度の次亜塩素酸ナトリウム水溶液を、所定量ずつ断続的に供給し、
次亜塩素酸ナトリウム水溶液が供給された後の前記第1分岐流を攪拌混合して、次亜塩素酸ナトリウムの均一な希釈水溶液流を生成し、
第2分岐流に、第2定量ポンプを用いて、第2薬液タンクに貯留されている予め設定された濃度の塩酸を所定量ずつ断続的に供給し、
塩酸が供給された後の前記第2分岐流を攪拌混合して均一な希釈塩酸流を生成し、
次亜塩素酸ナトリウムの希釈水溶液流と希釈塩酸流とを合流させた後に、攪拌混合して、所定濃度およびpHの次亜塩素酸水を生成し、
生成される次亜塩素酸水の濃度およびpHの制御を、供給される原水流量を計測し、計測結果に基き、前記第1、第2定量ポンプによる次亜塩素酸ナトリウム水溶液および塩酸の供給量を増減することにより行うことを特徴とする次亜塩素酸水の生成方法。
Forming a raw water stream supplied at a given pressure,
Branching the raw water stream into first and second branch streams;
Using a first metering pump, a predetermined concentration of sodium hypochlorite aqueous solution stored in the first chemical liquid tank is intermittently supplied to the first branch flow by a predetermined amount,
Stirring and mixing the first branched stream after the aqueous sodium hypochlorite solution is supplied to produce a uniform diluted aqueous stream of sodium hypochlorite;
The second branch flow is intermittently supplied with a predetermined amount of hydrochloric acid stored in the second chemical tank by a predetermined amount using a second metering pump,
Stirring and mixing the second branched stream after the hydrochloric acid is fed to produce a uniform diluted hydrochloric acid stream;
A dilute aqueous sodium hypochlorite stream and a dilute hydrochloric acid stream are combined and mixed by stirring to produce hypochlorous acid water having a predetermined concentration and pH,
Control the concentration and pH of the generated hypochlorous acid water, measure the flow rate of the supplied raw water, and supply the sodium hypochlorite aqueous solution and hydrochloric acid by the first and second metering pumps based on the measurement results A method for producing hypochlorous acid water, which is carried out by increasing or decreasing the amount of water.
上流側管路と、
前記上流側管路の下流端から分岐して再び合流する第1分岐管路および第2分岐管路と、
前記第1、第2分岐管路の下流端の合流点から延びている下流側管路と、
原水を、前記上流側管路から前記第1、第2分岐管路のそれぞれを経由して前記下流側管路に圧送する原水供給ポンプと、
予め設定した濃度の次亜塩素酸ナトリウム水溶液を貯留する第1薬液タンクと、
予め設定した濃度の塩酸を貯留する第2薬液タンクと、
前記第1分岐管路を流れる原水に、前記第1薬液タンクから次亜塩素酸ナトリウム水溶液を所定量ずつ断続的に供給する第1定量ポンプと、
前記第2分岐管路を流れる原水に、前記第2薬液タンクから塩酸を所定量ずつ断続的に供給する第2定量ポンプと、
前記第1分岐管路の途中において、次亜塩素酸ナトリウム水溶液が供給された後の原水を攪拌混合する第1攪拌混合器と、
前記第2分岐管路の途中において、塩酸が供給された後の原水を攪拌混合する第2攪拌混合器と、
前記下流側管路を流れる次亜塩素酸ナトリウムの希釈水溶液および希釈塩酸を攪拌混合する第3攪拌混合器と、
を有していることを特徴とする次亜塩素酸水の生成器。
An upstream pipeline,
A first branch pipe and a second branch pipe branching from the downstream end of the upstream pipe and joining again;
A downstream pipe line extending from a confluence of the downstream ends of the first and second branch pipe lines;
A raw water supply pump for pumping raw water from the upstream pipeline to the downstream pipeline via each of the first and second branch pipelines;
A first chemical tank for storing a sodium hypochlorite aqueous solution having a preset concentration;
A second chemical tank for storing hydrochloric acid having a preset concentration;
A first metering pump that intermittently supplies a predetermined amount of sodium hypochlorite aqueous solution from the first chemical solution tank to the raw water flowing through the first branch pipe;
A second metering pump that intermittently supplies hydrochloric acid from the second chemical tank to the raw water flowing through the second branch pipe by a predetermined amount;
In the middle of the first branch pipe, a first stirring mixer that stirs and mixes raw water after the sodium hypochlorite aqueous solution is supplied;
In the middle of the second branch pipe, a second stirring mixer that stirs and mixes raw water after hydrochloric acid is supplied;
A third stirring mixer for stirring and mixing a diluted aqueous solution of sodium hypochlorite and diluted hydrochloric acid flowing through the downstream side pipe;
A hypochlorous acid water generator characterized by comprising:
請求項2において、
前記第1〜第3攪拌混合器はディスクフィルタである次亜塩素酸水の生成器。
In claim 2,
The said 1st-3rd stirring mixer is a generator of hypochlorous acid water which is a disk filter.
請求項2または3において、
前記上流側管路を流れる原水流量を計測する流量計と、
前記流量計による計測結果に基き、前記第1定量ポンプによる次亜塩素酸ナトリウム水溶液の供給量および前記第2定量ポンプによる塩酸の供給量を増減して、前記第3攪拌混合器を介して得られる次亜塩素酸水の濃度およびpHを制御する制御盤と、
を有している次亜塩素酸水の生成器。
In claim 2 or 3,
A flow meter for measuring the flow rate of raw water flowing through the upstream pipeline,
Based on the measurement result by the flow meter, the amount of sodium hypochlorite aqueous solution supplied by the first metering pump and the amount of hydrochloric acid supplied by the second metering pump are increased or decreased, and obtained through the third stirring mixer. A control panel for controlling the concentration and pH of hypochlorous acid water,
A hypochlorous acid water generator.
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