JP2018038995A - Sterilized sea water, sterilized fresh water generation method and device - Google Patents
Sterilized sea water, sterilized fresh water generation method and device Download PDFInfo
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Abstract
【課題】海洋生物又は淡水生物の飼育用水や養殖用水、生鮮魚介類の殺菌洗浄用水、生鮮魚介類の運搬時の鮮度保持用水、生鮮魚介類を扱う場所に設置されている設備や機械器具の洗浄用水等、種々の用途に使用される無菌海水及び無菌淡水の生成方法、及び前記水を生成する装置の提供。【解決手段】海水又は淡水の入った水槽3に、電解原液2を内蔵した電解槽1を投入し、容器内の海水又は淡水からの電解により電解水及び電解ガス(塩素)を得、水槽11内で次亜塩素酸により除菌を行い、除菌能力を持つ海水又は淡水を得た後、チオ硫酸ナトリウム9等の中和剤を添加し次亜塩素酸を中和後、無菌海水及び淡水12を得る。電解槽3の容器上部4には、微細電解ガス放出用の細孔を設け、容器下部にはバルブ8を設置し、電解終了時の電解物の排出を容易にした装置。【選択図】図1PROBLEM TO BE SOLVED: To provide water for breeding and aquaculture of marine organisms or freshwater organisms, water for sterilizing and washing fresh seafood, water for maintaining freshness when transporting fresh seafood, equipment and machinery installed in a place where fresh seafood is handled Providing a method for producing aseptic seawater and aseptic fresh water used for various purposes such as washing water, and an apparatus for producing the water. An electrolytic tank 1 containing an electrolytic stock solution 2 is placed in a tank 3 containing seawater or fresh water, and electrolyzed water and electrolytic gas (chlorine) are obtained by electrolysis from seawater or fresh water in the container. After sterilizing with hypochlorous acid to obtain seawater or fresh water having sterilizing ability, neutralizing hypochlorous acid by adding a neutralizing agent such as sodium thiosulfate 9 and then aseptic seawater and fresh water Get 12. An apparatus in which a fine electrolytic gas discharge pore is provided in the upper part 4 of the electrolytic cell 3 and a valve 8 is provided in the lower part of the container to facilitate the discharge of the electrolyte at the end of electrolysis. [Selection] Figure 1
Description
本発明は、除菌海水または除菌淡水を製造する生成法及び製造装置に関する。 The present invention relates to a production method and a production apparatus for producing sterilized seawater or sterilized fresh water.
本発明における除菌海水または除菌淡水とは、塩素塩溶液もしくは塩酸もしくは希塩酸を被電解水とする無隔膜電解にて生成された除菌能力を有する電解生成水を海水または淡水である原水(以下同じ)に添加し無菌原水とした上で、電解生成水が含有する有効塩素成分を中和(殺菌能の中和)して、無菌状態または無菌に近い状態に調製された水をいう。 The sterilized seawater or sterilized fresh water in the present invention refers to electrolyzed water having a sterilizing ability generated by non-diaphragm electrolysis using a chlorine salt solution or hydrochloric acid or dilute hydrochloric acid as the electrolyzed water. The same shall apply hereinafter) to make sterile raw water, and then neutralize the effective chlorine component contained in the electrolyzed water (neutralizing sterilizing ability) to prepare water that is prepared in a sterile or nearly aseptic condition.
当該除菌海水または除菌淡水を構成する電解生成水は、被電解水の電解時に生成される有効塩素成分の除菌作用を有するもので、当該電解生成水を添加した原水は雑菌等が殺菌されて無菌状態となる。
さらに有効塩素成分が飼育や養殖の対象とする生物に影響を及ぼさない程度の濃度になるように、有効塩素成分を中和して無菌状態または無菌に近い状態に調製される。
これにより、当該除菌海水または除菌淡水の生物や生鮮魚介類に対する悪影響は解消され、当該除菌海水または除菌淡水は、生物の飼育用水や養殖用水、生鮮魚介類の殺菌洗浄用水、生鮮魚介類の運搬時の鮮度保持用水、生鮮魚介類を扱う場所に設置されている設備や機械器具の洗浄用水等、種々の用途に使用される。The electrolyzed water that constitutes the sterilized seawater or sterilized fresh water has the effect of sterilizing the effective chlorine component produced during electrolysis of the electrolyzed water. To be aseptic.
Further, the effective chlorine component is neutralized and prepared in a sterilized state or a state close to sterilization so that the effective chlorine component has a concentration that does not affect the organisms to be reared and cultured.
As a result, adverse effects on the organism and fresh fish and shellfish of the sterilized seawater or sterilized freshwater are eliminated. It is used for various purposes such as water for maintaining freshness when transporting seafood, and water for cleaning equipment and machinery installed in a place where fresh seafood is handled.
殺菌能を有する電解生成水を水または海水で希釈して調製された希釈電解生成水を、活魚介類の洗浄殺菌に使用することはすでに提案されている(特許文献1を参照)。また、殺菌能を有する電解生成水を清澄な水で希釈することにより、所定のpHに調整した殺菌用水を生成する方法についてもすでに提案されている。
ところで、殺菌能を有する電解生成水を希釈用水で希釈する手段としては、電解生成水を一旦貯留タンク内に導入して収容し、電解生成水が収容されている貯留タンク内に希釈用水を導入して混合する手段が採られるのが一般であり、また、電解生成水の導出管路に希釈用水を導入して、導出管路内で希釈用水を電解生成水に混合する手段が採られるのが一般である。 By the way, as means for diluting the electrolyzed water having sterilizing ability with the diluting water, the electrolyzed water is once introduced and stored in the storage tank, and the diluting water is introduced into the storage tank in which the electrolyzed water is stored. In general, a means for mixing is adopted, and a means for introducing the dilution water into the lead-out line for the electrolyzed water and mixing the dilution water with the electrolyzed water in the lead-out pipe is adopted. Is common.
しかしながら、前者の手段を採る場合には、貯留タンク内で希釈電解生成水を調製している場合には、当該貯留タンクからは希釈電解生成水を採取することはできず、貯留タンク内の希釈電解生成水を消費した後には、希釈電解生成水の採取を一旦中断しなければならないとう問題がある。また、後者の手段を採る場合には、電解生成水が流動する導出管路内で、電解生成水と希釈用水とを混合することから、調製される希釈電解生成水には濃度斑が生じ易いと問題があり、かつ、電解生成水および希釈用水の導出管路内への導入量は大きく規制されることから、希釈電解生成水を短時間に大量に消費する場合には、支障が生じるという問題がある。 However, in the case where the former method is adopted, when diluted electrolytic product water is prepared in the storage tank, diluted electrolytic product water cannot be collected from the storage tank, and dilution in the storage tank is not possible. There is a problem that after the electrolyzed water is consumed, the collection of the diluted electrolyzed water must be interrupted. Further, when the latter method is adopted, since the electrolytically generated water and the dilution water are mixed in the outlet pipe through which the electrolytically generated water flows, concentration spots are easily generated in the prepared diluted electrolytically generated water. In addition, the amount of electrolytically generated water and dilution water introduced into the outlet conduit is greatly regulated, and there is a problem when a large amount of diluted electrolytically generated water is consumed in a short time. There's a problem.
さらに海水を電気分解した際に二酸化鉄が発生し電解海水が茶色く変色し、当該除菌海水の使用目的である生鮮魚介類の殺菌洗浄用水、生鮮魚介類の運搬時の鮮度保持用水、生鮮魚介類を扱う場所に設置されている設備や機械器具の洗浄用水には使用できなくなるのが現状である。
しかも装置は大きくならざるを得ず、携帯や搬送には不向きで、1個所に固定設置して使用することしかできなかった。また、原水が連続的に一定の圧力で供給されることが必要で、そのような給水設備の整った場所でしか使用できなかった。また、装置は高価であり、広く利用するには向いていなかった。従って、本発明の目的は、これらの問題を解消することにある。Furthermore, when the seawater is electrolyzed, iron dioxide is generated and the electrolyzed seawater turns brown, and the water for sterilization and washing of fresh seafood, which is the purpose of use of the sterilized seawater, water for maintaining freshness when transporting fresh seafood, and fresh seafood At present, it cannot be used as cleaning water for equipment and machinery installed in places where food is handled.
Moreover, the apparatus has to be large, and is unsuitable for carrying or transporting, and can only be used by being fixedly installed in one place. In addition, the raw water must be continuously supplied at a constant pressure, and can only be used in a place where such water supply facilities are provided. Moreover, the apparatus is expensive and not suitable for wide use. Therefore, the object of the present invention is to eliminate these problems.
本発明は、除菌海水または除菌淡水を製造する製造装置に関する。本発明に係る生成法は除菌海水または除菌淡水を製造する製造装置である。 The present invention relates to a production apparatus for producing sterilized seawater or sterilized fresh water. The production method according to the present invention is a production apparatus for producing sterilized seawater or sterilized fresh water.
本発明者は課題を解決するために、電極と該電極を収容する容器から構成された、コンパクトな電解槽を発明した。また、塩素塩溶液もしくは塩酸もしくは希塩酸の電解用の原液は電解槽の容器中に、上部に設けた蓋付きの注入部から注入するようにした。また、該容器の上部には電解ガスを細かな気泡として電解槽外部に出すような細孔を設けた。また、該細孔は蓋付きの注入部に設けることや、蓋付き注入部と電解槽容器の接合部に設けることも可能であることを確認し、何れかの構造とした。細孔を設けたことにより、電解ガスが細かな気泡となり、電解槽が浸漬されている原水に容易に溶解できるようになった。さらに、電解槽容器の下部にバルブを設けることにより、電解終了時に電解物の排出が容易であることを知り電解槽容器の形状を決定した。電解原液を注入した該電解槽を、予め原水を貯留した容器に浸漬し電解することにより、水道等の加圧給水設備を必要とせず、電解水を調製することを可能にした。さらに、そのようにして電解中に電解ガスが原水を貯留した容器から外部に漏れることを防ぐために、原水を貯留した容器に密栓ができる構造とすることによって課題を解決した。In order to solve the problem, the inventor has invented a compact electrolytic cell composed of an electrode and a container for housing the electrode. In addition, a chlorine salt solution or a stock solution for electrolysis of hydrochloric acid or dilute hydrochloric acid was poured into a container of an electrolytic tank from an injection portion with a lid provided on the top. Moreover, the upper part of the container was provided with pores that let the electrolytic gas come out of the electrolytic cell as fine bubbles. In addition, it was confirmed that the pores could be provided in the injection part with a lid or in the joint part between the injection part with the lid and the electrolytic cell container, and any structure was adopted. By providing the pores, the electrolytic gas became fine bubbles, which can be easily dissolved in the raw water in which the electrolytic cell is immersed. Furthermore, by providing a valve in the lower part of the electrolytic cell container, the shape of the electrolytic cell container was determined by knowing that the electrolyte could be easily discharged at the end of electrolysis. The electrolytic cell into which the electrolytic stock solution was injected was immersed in a container in which raw water was previously stored for electrolysis, so that it was possible to prepare electrolytic water without the need for pressurized water supply equipment such as tap water. Furthermore, in order to prevent the electrolytic gas from leaking outside from the container storing the raw water during electrolysis, the problem has been solved by adopting a structure in which the container storing the raw water can be sealed.
図1および図2に基づいて本発明の実施の1形態を説明する。図1は使用状態を説明する全体図である。▲1▼電解槽本体は▲6▼電力供給電線で▲5▼コントロール部と電気的に結合されている。▲6▼電気コードの途中には▲3▼原水容器用の▲4▼中蓋が取り付けられており、▲1▼電解槽を▲3▼原水容器に投入した状態で▲4▼中蓋を施し、▲3▼原水容器を密閉できる構造になっている。図2は電解槽の構造を説明する外観図と断面図である。本体は▲20▼上部と21下部から成っており、▲20▼上部は空洞で▲19▼電極板が陰極、陽極それぞれ1枚ずつ保持、内蔵している。▲19▼電極板には、それぞれ▲6▼電気コードによって、▲5▼コントロール部に内蔵されている直流電源の陰極、陽極に接続されている。また上部▲20▼の上端には、▲14▼電解原液注入部が設置されており、▲17▼蓋を開けることによって、▲1▼電解槽に電解原液を注入できる構造になっている。また、▲14▼電解原液注入口と上部▲20▼の接合部には23細孔(図示していない)が設けられ、電解ガスを微細な気泡にする役目をする。
21下部は▲1▼電解槽の底を構成すると同時に電解物の排出を行う▲18▼排出口と排出口を開閉できる▲16▼バルブを内蔵している。▲16▼バルブの開閉は21下部の側面に設置された▲16▼バルブの一部に設けられた22取手を利用し、▲16▼バルブ本体を回転させて行う。
この装置を使って電解水を調製する手順は次のようになる。まず、▲3▼原水容器に▲2▼原水を注入する。
次に▲1▼電解槽の▲16▼バルブを閉じて、▲14▼電解原液注入部から電解液を注入し、▲17▼蓋を閉じる。▲1▼電解槽を▲3▼原水容器に投入する。▲6▼電気コードに取り付けられた▲4▼内蓋を、▲3▼原水容器の口に嵌合し、▲3▼原水容器を密閉する。続いて、▲5▼コントロール部に設置してある始動スイッチを入れて電解を始める。
電解が終了したら、▲1▼電解槽を▲2▼原水から引き上げ、▲16▼バルブを開け▲14▼電解原液注入部の▲17▼蓋を開き、内部の電解物を▲2▼原水に加えて混合し、再度▲1▼電解槽を▲2▼原液に浸して、▲1▼電解槽を洗浄する。▲1▼電解槽を引き上げて、▲3▼原水容器の内容物を攪拌して電解水が調製される。▲8▼原水移液バルブを開き、▲11▼無菌水槽に移液し、▲13▼チオ硫酸ナトリウム槽から▲9▼チオ硫酸ナトリウムを▲10▼チオ硫酸ナトリウム添加バルブを開き添加し有効塩素濃度を中和せしめ無菌海水または無菌淡水が調製される。An embodiment of the present invention will be described based on FIG. 1 and FIG. FIG. 1 is an overall view illustrating a use state. (1) The electrolytic cell main body is electrically coupled with (5) the control unit by (6) power supply wire. (6) In the middle of the electrical cord, (3) (4) inner lid for raw water container is attached, (1) The electrolytic cell is put in (3) raw water container, and (4) inner lid is applied. , (3) The raw water container can be sealed. FIG. 2 is an external view and a sectional view for explaining the structure of the electrolytic cell. The main body is composed of (20) upper part and 21 lower part, (20) upper part is hollow, and (19) electrode plate holds and incorporates one cathode and one anode. (19) Each electrode plate is connected to a cathode and an anode of a DC power source incorporated in a control unit by (6) an electric cord, respectively. Further, at the upper end of the upper part (20), (14) an electrolytic stock solution injection part is installed, and (17) by opening the lid, (1) the electrolytic stock solution can be injected into the electrolytic cell. Further, 23 pores (not shown) are provided at the junction of the electrolytic solution inlet and the
The
The procedure for preparing electrolyzed water using this apparatus is as follows. First, (2) raw water is poured into (3) raw water container.
Next, (1) the electrolytic cell's (16) valve is closed, (14) the electrolytic solution is injected from the electrolytic solution injection part, and (17) the lid is closed. (1) The electrolytic cell is put into the (3) raw water container. (6) (4) The inner lid attached to the electric cord is fitted into the mouth of (3) raw water container, and (3) the raw water container is sealed. Next, (5) start the electrolysis by turning on the start switch installed in the control unit.
When the electrolysis is completed, (1) the electrolytic cell is lifted from (2) raw water, (16) the valve is opened, (14) the electrolytic solution injection part is opened, (17) the lid is opened, and the internal electrolyte is added to the raw water. Then, (1) electrolytic cell is immersed again in (2) stock solution, and (1) electrolytic cell is washed. (1) The electrolytic cell is pulled up, and (3) the contents of the raw water container are stirred to prepare electrolytic water. (8) Open the raw water transfer valve, (11) Transfer to a sterile water tank, (13) Add sodium thiosulfate from the sodium thiosulfate tank, (10) Open the sodium thiosulfate addition valve, and add effective chlorine concentration Aseptic seawater or aseptic fresh water is prepared.
本発明に係る海水の殺菌処理方法は無隔膜の電解槽で塩水を電解し、得られた次亜塩素酸を海水貯槽に添加し、除菌された海水とした後、チオ硫酸ナトリウムを添加し次亜塩素酸を中和後、原水貯槽から、除菌海水槽に生成海水を移し完了する。
実際に海水を原水とし、それに各濃度の希塩酸を入れた投入型電解槽を浸漬し、電気分解し、所定時間後原水である海水と混合した後のpH、ORP、有効塩素濃度は以下の通りである。
上記表を説明すると原水である海水は富山県で採取された海洋深層水10Lとし、原液は21%食品添加物塩酸を飲用可能な水で希釈し3%、6%、9%の希塩酸とした。
投入型電解槽は株式会社ホクエツ製の「アピアミニ」を使用し、電解毎に10mLを電解槽に注入し原水10Lに浸漬後、DC5V、を印加し電気分解したその時の電流値は1.0A〜1.6Aであった。
結果どの電解でも有効塩素濃度が10mg/L以上の除菌海水の生成が確認できた。
また、除菌海水を無菌海水とする為、0.01mol/Lのチオ硫酸ナトリウムを添加し次亜塩素酸を中和した結果は以下の通りである。
結果、海水でも次亜塩素の中和は有効塩素濃度から1.77を商した0.01mol/Lのチオ硫酸ナトリウムを添加すれば中和することが確認できた。
これはチオ硫酸ナトリウムを0.1mol/Lとすれば各1/10で中和可能となる。
(化学式)
Na2S2O3+4Cl2+5H2O→2NaCl+2H2SO4+6HClとか L−アスコルビン酸+HClO→酸化型アスコルビン酸+HCl+H2O等In the seawater sterilization method according to the present invention, salt water is electrolyzed in an electrolyzed electrolysis tank, and the obtained hypochlorous acid is added to a seawater storage tank to obtain sterilized seawater, and then sodium thiosulfate is added. After neutralizing hypochlorous acid, the generated seawater is transferred from the raw water storage tank to the sterilized seawater tank and completed.
The pH, ORP, and effective chlorine concentration after actually charging seawater as raw water and immersing it in an electrolytic cell containing dilute hydrochloric acid of each concentration, electrolyzing, and mixing with seawater as raw water after a predetermined time are as follows It is.
Explaining the above table, the raw sea water is 10 L of deep sea water collected in Toyama Prefecture, and the stock solution is diluted with 21% food additive hydrochloric acid with drinkable water to make 3%, 6% and 9% dilute hydrochloric acid. .
The input type electrolytic cell uses “Apiamini” manufactured by Hokuetsu Co., Ltd. 10 mL is poured into the electrolytic cell for each electrolysis and immersed in 10 L of raw water, and then DC5 V is applied and electrolysis is performed. 1.6 A.
Results The generation of sterilized seawater having an effective chlorine concentration of 10 mg / L or more was confirmed in any electrolysis.
Moreover, in order to use the sterilized seawater as sterile seawater, the result of neutralizing hypochlorous acid by adding 0.01 mol / L sodium thiosulfate is as follows.
As a result, it was confirmed that even in seawater, hypochlorous acid was neutralized by adding 0.01 mol / L sodium thiosulfate obtained by dividing 1.77 from the effective chlorine concentration.
If sodium thiosulfate is 0.1 mol / L, neutralization is possible at 1/10 each.
(Chemical formula)
Na 2 S 2 O 3 + 4Cl 2 + 5H 2 O → 2N a Cl + 2H 2 SO 4 + 6HCl or L-ascorbic acid + HClO → oxidized ascorbic acid + HCl + H 2 O, etc.
図1、図2に示した装置を使った実施例を示すが、これは本発明の理解を助けるのが目的であり、本発明の範囲をこの例に限定する趣旨ではない。Although the Example using the apparatus shown in FIG. 1 and FIG. 2 is shown, this is for the purpose of assisting the understanding of the present invention, and is not intended to limit the scope of the present invention to this example.
▲1▼電解槽は全出のホクエツ製「アピアミニ」を10倍の電解面積にスケールアップし、内部にためることの出来る電解液量も10mLから100mLに増量した。
▲3▼原水容器は容量100Lのダイライト社製樹脂製容器を使用し、当該槽には▲7▼(株)佐竹製ポータブルミキサーA720型攪拌機を配置する。
▲13▼中和液用容器は樹脂製の20L容器を使用して0.01mol/Lのチオ硫酸ナトリウムを貯液し、▲11▼無菌海水槽は容量500Lの樹脂製容器を使用し、25(株)佐竹製ポータブルミキサーA720型攪拌機、および24サニートレーディング(株)製AT−0923残留塩素濃度計を配置する。
▲13▼0.01mol/Lのチオ硫酸ナトリウム容器から▲11▼無菌水槽への中和液の添加は▲10▼積水化学(株)製樹脂製電磁弁Tipe131型15Aを介して添加する、この▲13▼0.01mol/Lのチオ硫酸ナトリウム容器は▲11▼無菌水槽より上部に配置され、当該電磁弁を開くのみで中和液は添加可能となる。処理を終了した海水は26手動弁で使用場所に取り出される。(1) The electrolytic cell was scaled up to 10 times the electrolytic area of Hokuetsu's “Apiamini”, and the amount of electrolyte that could be accumulated inside was increased from 10 mL to 100 mL.
{Circle around (3)} The raw water container is a resin container made by Dailite Co., Ltd. with a capacity of 100 L, and a portable mixer A720 type agitator made by Satake Corp. is placed in the tank.
(13) The neutralization solution container uses a resin 20 L container to store 0.01 mol / L sodium thiosulfate. (11) The sterile seawater tank uses a 500 L resin container. A portable mixer A720 type agitator manufactured by Satake Corp. and an AT-0923 residual chlorine concentration meter manufactured by 24 Sunny Trading Corp. are arranged.
(13) Addition of neutralization solution from 0.01 mol / L sodium thiosulfate container to (11) sterile water tank is added via (10) resin solenoid valve Type 131 type 15A manufactured by Sekisui Chemical Co., Ltd. (13) A 0.01 mol / L sodium thiosulfate container is placed above the (11) sterile water tank, and the neutralizing solution can be added only by opening the solenoid valve. The seawater that has been processed is taken out to the place of use by 26 manual valves.
▲3▼原水槽に▲2▼海水100Lを貯液し、▲1▼電解槽に100mLの6.0%希塩酸を入れ、▲2▼海水に浸漬後、電解電圧5V、同電流1.0Aを電解槽に印加し、電解する。電解槽上部の232.0mm細孔より電気分解による塩素ガスが排出され海水中に溶解される。10分後、残留塩素濃度計で16mg/Lの有効塩素が検出され、電圧、電流の印加を停止し▲1▼投入型次亜塩素酸生成電解槽を、▲2▼海水から取り出す、その際電解槽内部に残った電解質は▲16▼電解槽下部バルブを開き、▲3▼原水槽に排出する。▲7▼攪拌機で1分攪拌し濃度斑を無くする、この時点で海水の有効塩素濃度は19mg/Lで、次亜塩素酸を含んだ殺菌能力を持つ海水となり、当然無菌状態となる。次に▲8▼手動弁を開き、▲11▼無菌海水槽へ▲2▼有効塩素を含んだ海水を移し、24残留塩素濃度計で監視し▲13▼中和液槽に貯められた▲9▼チオ硫酸ナトリウム0.01mol/Lを▲7▼電磁弁を経て▲4▼攪拌機で攪拌しつつ0mg/Lまで中和液を添加する。▲5▼残留塩素濃度計の信号で▲10▼電磁弁を自動閉、添加終了となる。さらに1分間攪拌して完全に濃度斑を解消した後攪拌が自動停止される。この時点で海水は次亜塩素酸を含まない除菌海水となる。最後に手動弁を介して取り出される。
この手法を何度か繰り返し、▲11▼殺菌海水槽の液レベルを監視しつつ貯液する
▲11▼無菌海水槽の海水のサンプル水を培養し菌を確認した所、菌は全く存在せず無菌状態が確認できた。
これにより有効塩素濃度が中和され海洋生物の飼育用水や養殖用水が可能な無菌海水が調製された(3) Store 100 L of seawater in the raw water tank, (1) Add 100 mL of 6.0% dilute hydrochloric acid to the electrolytic tank, and (2) soak in seawater, then apply an electrolysis voltage of 5 V and the same current of 1.0 A. Apply to the electrolytic cell and electrolyze. Chlorine gas by electrolysis is discharged from the 232.0 mm pores at the top of the electrolytic cell and dissolved in seawater. After 10 minutes, 16 mg / L of effective chlorine was detected by the residual chlorine concentration meter, the application of voltage and current was stopped, and (1) the charging-type hypochlorous acid producing electrolytic cell was removed from (2) seawater. The electrolyte remaining inside the electrolytic cell is opened (16) by opening the lower valve of the electrolytic cell, and (3) discharged into the raw water tank. (7) Stir with a stirrer for 1 minute to eliminate concentration spots. At this point, the effective chlorine concentration of seawater is 19 mg / L, and it becomes seawater with sterilizing ability containing hypochlorous acid, and naturally becomes sterile. Next, (8) Open the manual valve, (11) Transfer the seawater containing effective chlorine to (11) Aseptic seawater tank, monitor with 24 residual chlorine concentration meter, (13) Stored in the neutralization tank (9) (2) Add neutralizing solution to 0 mg / L while stirring 0.01 mol / L of sodium thiosulfate through (7) solenoid valve and (4) stirring with a stirrer. (5) Residual chlorine concentration meter signal (10) The solenoid valve is automatically closed and the addition is completed. Further, stirring is automatically stopped after stirring for 1 minute to completely eliminate the density unevenness. At this point, the seawater becomes sanitized seawater that does not contain hypochlorous acid. Finally, it is taken out via a manual valve.
This technique is repeated several times, and {11} the liquid is stored while monitoring the liquid level in the sterilized seawater tank. {11} The bacteria are confirmed by culturing the sample water of the seawater in the sterile seawater tank. Aseptic conditions were confirmed.
As a result, the effective chlorine concentration was neutralized, and aseptic seawater that can be used for marine life and aquaculture was prepared.
本発明に依る除菌海水または除菌淡水生成法は生物の飼育用水や養殖用水として、生鮮魚介類の殺菌洗浄用水、生鮮魚介類の運搬時の鮮度保持用水、生鮮魚介類を扱う場所に設置されている設備や機械器具の洗浄用として魚介類関連の食品製造や物流、環境において衛生状態の向上に寄与する。また装置、ランニングコスト共極めて安価であるため、幅広く利用できる。The method for producing sterilized seawater or sterilized fresh water according to the present invention is installed in a place for handling fresh fish and shellfish sterilization and washing water, freshness-maintaining water during transport of fresh fish and shellfish, and fresh fish and shellfish It contributes to the improvement of hygiene in the production and distribution of seafood-related foods and the environment for the cleaning of existing facilities and machinery. In addition, since the apparatus and running cost are extremely low, it can be used widely.
1.電解槽本体
2.原水
3.原水貯槽
4.中蓋
5.コントロール部
6.電力供給電線
7.原水槽攪拌機
8.原水移液バルブ
9.チオ硫酸ナトリウム
10.チオ硫酸ナトリウム添加バルブ
11.除菌海水槽または除菌淡水槽
12.除菌海水または除菌淡水
13.チオ硫酸ナトリウム容器
14.電解原液注入部
15.電解槽の電解質貯液部
16.電解物排出口開閉バルブ
17.電解原液注入部蓋
18.電解物排出口
19.電極板
20.電解槽本体上部
21.電解槽本体下部
22.電解物排出口開閉バルブバルブ回転用取手
23.細孔
24.有効塩素濃度計
25.無菌水槽攪拌機
26.取り出し手動弁1. Electrolyzer body 1. Raw water 3. Raw water storage tank 4. Inner lid 5. Control unit 6. Electric power supply wire 7. Raw
Claims (7)
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Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4992156A (en) * | 1989-03-06 | 1991-02-12 | Silveri Michael A | Electrolytic pool purifier |
| JPH07163982A (en) * | 1994-10-31 | 1995-06-27 | Yoshitane Tamura | Electrolytic sterilization device for stored water |
| JP2003275764A (en) * | 2002-03-25 | 2003-09-30 | Sanyo Electric Co Ltd | Sterilization apparatus |
| JP2004181441A (en) * | 2002-12-02 | 2004-07-02 | Hokuetsu:Kk | Container-type electrolyzed water generator |
| JP2011177321A (en) * | 2010-03-01 | 2011-09-15 | Sanyo Electric Co Ltd | Finger sterilizing apparatus |
| JP2013017936A (en) * | 2011-07-08 | 2013-01-31 | Gaia:Kk | Apparatus for producing electrolyzed water |
| WO2014064942A1 (en) * | 2012-10-25 | 2014-05-01 | パナソニック株式会社 | Method for treating ballast water and device for treating ballast water used therefor |
| US20150211133A1 (en) * | 2012-08-01 | 2015-07-30 | Cosmic Round Korea Co., Ltd. | Apparatus for Producing Slightly Weak Acidic Hypochlorous Acid Water |
-
2016
- 2016-09-06 JP JP2016190314A patent/JP6536907B2/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4992156A (en) * | 1989-03-06 | 1991-02-12 | Silveri Michael A | Electrolytic pool purifier |
| JPH07163982A (en) * | 1994-10-31 | 1995-06-27 | Yoshitane Tamura | Electrolytic sterilization device for stored water |
| JP2003275764A (en) * | 2002-03-25 | 2003-09-30 | Sanyo Electric Co Ltd | Sterilization apparatus |
| JP2004181441A (en) * | 2002-12-02 | 2004-07-02 | Hokuetsu:Kk | Container-type electrolyzed water generator |
| JP2011177321A (en) * | 2010-03-01 | 2011-09-15 | Sanyo Electric Co Ltd | Finger sterilizing apparatus |
| JP2013017936A (en) * | 2011-07-08 | 2013-01-31 | Gaia:Kk | Apparatus for producing electrolyzed water |
| US20150211133A1 (en) * | 2012-08-01 | 2015-07-30 | Cosmic Round Korea Co., Ltd. | Apparatus for Producing Slightly Weak Acidic Hypochlorous Acid Water |
| WO2014064942A1 (en) * | 2012-10-25 | 2014-05-01 | パナソニック株式会社 | Method for treating ballast water and device for treating ballast water used therefor |
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