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JP3291619B2 - Sodium hypochlorite solution generator - Google Patents
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JP3291619B2 - Sodium hypochlorite solution generator - Google Patents

Sodium hypochlorite solution generator

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Publication number
JP3291619B2
JP3291619B2 JP23374398A JP23374398A JP3291619B2 JP 3291619 B2 JP3291619 B2 JP 3291619B2 JP 23374398 A JP23374398 A JP 23374398A JP 23374398 A JP23374398 A JP 23374398A JP 3291619 B2 JP3291619 B2 JP 3291619B2
Authority
JP
Japan
Prior art keywords
salt
water
tank
sodium hypochlorite
storage tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP23374398A
Other languages
Japanese (ja)
Other versions
JP2000064076A (en
Inventor
久宗 栗原
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Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP23374398A priority Critical patent/JP3291619B2/en
Publication of JP2000064076A publication Critical patent/JP2000064076A/en
Application granted granted Critical
Publication of JP3291619B2 publication Critical patent/JP3291619B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】この発明は、塩化ナトリウム
溶液を電気分解して次亜塩素酸ナトリウム溶液を得る装
置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for obtaining a sodium hypochlorite solution by electrolyzing a sodium chloride solution.

【0002】[0002]

【従来の技術】次亜塩素酸ナトリウムを生成する装置と
して、特公昭63−28997号(特許第148330
4号)を挙げることができる。この公知例は、電解電流
に比例して発生する水素ガスで次亜塩素酸ナトリウムを
移送するものであり、原料の塩は別のタンク3に貯留
し、飽和塩水に溶解させ、この飽和塩水を貯留槽1内に
入れて水を加えて3〜5%の希釈塩水にしてこの希釈塩
水を電解槽7内に送り込んで次亜塩素酸ナトリウム溶液
(効力塩素8,000mg/l)を生成していた。
2. Description of the Related Art An apparatus for producing sodium hypochlorite is disclosed in JP-B-63-28997 (Japanese Patent No. 148330).
No. 4). In this known example, sodium hypochlorite is transferred by hydrogen gas generated in proportion to the electrolytic current. The salt of the raw material is stored in another tank 3 and dissolved in saturated saline, and the saturated saline is dissolved. Water is added to the storage tank 1 to make a 3-5% diluted saline solution, and the diluted saline solution is sent into the electrolytic cell 7 to produce a sodium hypochlorite solution (effective chlorine 8,000 mg / l). Was.

【0003】[0003]

【発明が解決しようとする課題】この従来の装置は、塩
の貯留タンク3と、飽和塩水の貯留槽1を持たなければ
ならず、装置の大型化となる欠点を有しているし、ま
た、希釈塩素の電気分解から、次亜塩素酸ナトリウム溶
液の生成の濃度が低く、高濃度の生成装置が要求されて
いた。
This conventional apparatus must have a salt storage tank 3 and a saturated salt water storage tank 1, which has the disadvantage of increasing the size of the apparatus. The concentration of sodium hypochlorite solution produced from the electrolysis of diluted chlorine is low, and a high-concentration generator has been required.

【0004】そこで、この発明は、装置の小型化と共
に、高濃度な次亜塩素酸ナトリウム溶液を生成する装置
を提供するものである。
Accordingly, the present invention provides an apparatus for producing a high-concentration sodium hypochlorite solution while reducing the size of the apparatus.

【0005】[0005]

【課題を解決するための手段】この発明に係る次亜塩素
酸ナトリウム溶液生成装置は、塩が貯留される塩貯留槽
と、給水口を持ち塩の溶解水が溜められる水槽が仕切壁
を介して併設され、前記仕切壁には塩の溶解水を前記水
槽より前記塩貯留槽に供給する塩溶解水供給口が形成さ
れ、前記塩潮流槽内に開口する開口部より飽和塩水を取
り入れ、この取り入れた飽和塩水を電気分解する電極が
配された電解槽が設けられ、この電解槽に次亜塩素酸ナ
トリウム溶液を発生する水素ガスの浮力を利用して前
記水槽内に送り出す移送管が設けられると共に、前記水
槽内に生成される希釈された希釈次亜塩素酸ナトリウム
溶液をオーバーフローにて外部へ送り出す流口を設け
たものである(請求項1)。
In the sodium hypochlorite solution producing apparatus according to the present invention, a salt storage tank for storing salt and a water tank having a water supply port for storing dissolved water of salt are provided through a partition wall. A salt-dissolved water supply port for supplying salt-dissolved water from the water tank to the salt storage tank is formed on the partition wall, and takes in saturated salt water from an opening that opens into the salt tide tank. An electrolytic cell provided with an electrode for electrolyzing the saturated brine taken in is provided, and a transfer pipe for sending the sodium hypochlorite solution into the water tank by utilizing the buoyancy of the generated hydrogen gas is provided in the electrolytic cell. together it is, is provided with a flow exit for feeding to the outside by the overflow of diluted diluted sodium hypochlorite solution produced in said water tank (claim 1).

【0006】したがって、電解槽内には、塩貯留槽から
飽和塩水が供給され、該電解槽内で次亜塩素酸ナトリウ
ム溶液が生成される。そして共に発生する水素ガスにて
移送管を介して水槽内へ送り出される。水槽内では、希
釈化され、流出口より外部機器へ送り出される。そして
送り出された液量分自動的に塩溶解水が塩溶解水供給口
より補充され、該溶解水は塩の結晶を通過しながら塩を
溶解して飽和塩水により電解槽内に補給され、前述した
ごとく電気分解され高濃度の次亜塩素酸ナトリウム溶液
(有効塩素30,000mg/l)が生成される。
Therefore, saturated salt water is supplied from the salt storage tank into the electrolytic cell, and a sodium hypochlorite solution is generated in the electrolytic cell. Then, the hydrogen gas generated together is sent into the water tank through the transfer pipe. In the water tank, it is diluted and sent out from the outlet to external equipment. Then, the salt-dissolved water is automatically replenished from the salt-dissolved water supply port by the amount of the sent liquid, and the dissolved water dissolves the salt while passing through the salt crystals and is replenished into the electrolytic cell with saturated salt water. Electrolysis is performed as described above, and a high-concentration sodium hypochlorite solution (effective chlorine 30,000 mg / l) is produced.

【0007】[0007]

【発明の実施の形態】以下、この発明の実施の形態を図
面にもとづいて説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0008】図1にあって、この発明の第1の実施例が
示され、槽1は、塩貯留槽2と水槽3とに仕切壁4にて
分けられている。塩貯留槽2には、塩(NaC1)の結
晶が下記する水より成る希釈水にて溶解されながら、該
結晶と飽和溶液とが共存して貯留されている。また、こ
の塩貯留槽2内には、下記する塩を電気分解する電解槽
7が配されている。なお、5は塩の投入用の投入口であ
る。
FIG. 1 shows a first embodiment of the present invention. The tank 1 is divided into a salt storage tank 2 and a water tank 3 by a partition wall 4. In the salt storage tank 2, while crystals of salt (NaC1) are dissolved in diluting water composed of water described below, the crystals and a saturated solution are stored together. Further, in the salt storage tank 2, an electrolytic tank 7 for electrolyzing a salt described below is arranged. Reference numeral 5 denotes an inlet for charging the salt.

【0009】電解槽7は例えば円筒形で、横方向にして
前記塩貯留槽内の塩化ナトリウム溶液の液面下方に配さ
れている。この電解槽7は先方に開口部8を有してお
り、ここに設けられたフィルタ9を介して飽和塩水が内
部に流入される。また、電解槽7には、陽極と陰極とよ
り成る一対の電極10a,10bが挿入され、該電極1
0a,10bの基端は、フランジ12に絶縁物13を介
して絶縁固定されている。この電極10a,10bは、
白金族から成る一つ又は複数の細長い線材の電極線と、
この電極線を結束するチタンより成る基体から成ってい
る。
The electrolytic cell 7 has, for example, a cylindrical shape and is disposed horizontally below the liquid level of the sodium chloride solution in the salt storage tank. The electrolytic cell 7 has an opening 8 at the front side, and saturated salt water flows into the inside through a filter 9 provided therein. A pair of electrodes 10a and 10b composed of an anode and a cathode are inserted into the electrolytic cell 7,
The base ends of Oa and 10b are insulated and fixed to the flange 12 via an insulator 13. These electrodes 10a, 10b
An electrode wire of one or more elongated wires of the platinum group;
It consists of a substrate made of titanium which binds the electrode wires.

【0010】移送管15は、前記電解槽7の上部に形成
された出口16に接続されていると共に、該移送管15
の他端が塩化ナトリウム溶液の液面より出て、前記水槽
3内、具体的には、仕切壁4に開口17している。した
がって、電解槽7内で生成の次亜塩素酸ナトリウム(N
aClO)と水素(H2 )が移送管15を介して水槽3
内に送り出される。
The transfer pipe 15 is connected to an outlet 16 formed at the upper part of the electrolytic cell 7 and is connected to the transfer pipe 15.
Has an opening 17 in the water tank 3, specifically, in the partition wall 4. Therefore, the sodium hypochlorite (N
aCLO) and hydrogen (H 2 ) are transferred through the transfer pipe 15 to the water tank 3
Sent out within.

【0011】水槽3は、水が供給される給水口19と、
希釈化された次亜塩素酸ナトリウム溶液を送り出す流出
口20を備えて、該流出口20の先端20aにて液面レ
ベルが規制されている。この水槽3と前記塩貯留槽2と
を仕切る仕切壁4には、溶解水が塩貯留槽2に流れ込む
塩溶解水給水口21が形成されている。なお、22は水
槽3の上方に設けられ、水素を外部に排出する孔であ
る。
The water tank 3 has a water supply port 19 to which water is supplied,
An outlet 20 for sending out the diluted sodium hypochlorite solution is provided, and a liquid level is regulated at a tip 20a of the outlet 20. A salt water supply port 21 through which dissolved water flows into the salt storage tank 2 is formed in a partition wall 4 that separates the water tank 3 from the salt storage tank 2. A hole 22 is provided above the water tank 3 and discharges hydrogen to the outside.

【0012】上述の構成において、貯留槽1内には塩の
結晶が投入されると共に、溶解水が塩溶解水給水口21
から供給され、該貯留槽1内は塩の結晶と飽和塩水が共
に溶存している。ここで、電極(10a,10b)に通
電すると、電解槽7の塩化ナトリウム溶液が電解し、そ
の通電量に応じた次亜塩素酸ナトリウムが生成されると
共に、陰極側の電極10bの周囲に水素ガスが発生す
る。
In the above configuration, salt crystals are charged into the storage tank 1 and the dissolved water is supplied to the salt-dissolved water supply port 21.
And the storage tank 1 has both salt crystals and saturated brine dissolved therein. Here, when electricity is supplied to the electrodes (10a, 10b), the sodium chloride solution in the electrolytic cell 7 is electrolyzed, and sodium hypochlorite is generated in accordance with the amount of electricity supplied, and hydrogen is generated around the electrode 10b on the cathode side. Gas is generated.

【0013】その反応式は、陽極においては、化1のよ
うになり、
The reaction formula at the anode is as follows:

【化1】2Cl- →Cl2 +2e 2H2 O+2e→H2 +2OH- 陽極においては、化2のようになり、At the anode, 2Cl → Cl 2 + 2e 2H 2 O + 2e → H 2 + 2OH

【化2】2Na+ +2OH- →2NaOH+H2 ↑ 電解槽内液中では、化3のようになる。Embedded image 2Na + + 2OH → 2NaOH + H 2は In the liquid in the electrolytic cell, the chemical reaction is as shown in Chemical formula 3.

【化3】 Cl2 +2NaOH→NaClO+NaCl+H2 Embedded image Cl 2 + 2NaOH → NaClO + NaCl + H 2 O

【0014】水素ガスは、発生初期には、その気泡が小
さいために次亜塩素酸ナトリウム溶液を電解槽7の外部
へ送り出すことができず、電解槽7の上部に集まり、徐
々にその気泡を大きくし、気泡が移送管15をふさぐ程
度の大きさとなると、移送管15内に溜められた次亜塩
素酸ナトリウム溶液を押し出しながら水槽3内へ排出さ
れる。この排出された量と等しい新たなる塩化ナトリウ
ム溶液が貯留槽2から電解槽7に送られ、前述した工程
が繰り返し行われる。
In the early stage of the generation of hydrogen gas, the sodium hypochlorite solution cannot be sent out of the electrolytic cell 7 due to its small bubbles, and collects at the upper part of the electrolytic cell 7 and gradually removes the bubbles. When the size is increased and the bubbles become large enough to block the transfer tube 15, the sodium hypochlorite solution stored in the transfer tube 15 is discharged into the water tank 3 while being pushed out. A new sodium chloride solution equal to the discharged amount is sent from the storage tank 2 to the electrolytic tank 7, and the above-described steps are repeatedly performed.

【0015】この場合、電極10a,10bへの通電量
の増に比して次亜塩素酸ナトリウム溶液の量も増大す
る。実施の形態では、飽和塩水を電気分解するので有効
塩素30,000mg/lの高濃度の次亜塩素酸ナトリ
ウム溶液が生成される。なお、飽和塩水を電解液として
いるので、液抵抗の変動がなく低電圧で電解電流に変動
がない。
In this case, the amount of the sodium hypochlorite solution also increases as the amount of electricity supplied to the electrodes 10a and 10b increases. In the embodiment, since the saturated salt water is electrolyzed, a high concentration sodium hypochlorite solution having an available chlorine of 30,000 mg / l is produced. Since the saturated salt water is used as the electrolytic solution, there is no change in the liquid resistance and there is no change in the electrolytic current at a low voltage.

【0016】水槽3内に送られた次亜塩素酸ナトリウム
は、水にて希釈され、希釈された溶液は、流出口20を
通して所望する機器へ送られ、主に殺菌消毒剤として利
用される。
The sodium hypochlorite sent into the water tank 3 is diluted with water, and the diluted solution is sent to a desired device through the outlet 20 and is mainly used as a disinfectant.

【0017】図2にあって、この発明の第2の実施の形
態が示されている。この実施の形態にあっては、前記第
1の実施の形態と異なり、電解槽7を水槽3内に配した
例であり、その先端の開口部8は、前記塩貯留槽2内に
配され開口している。したがって、開口部8を介して飽
和塩水を電解槽7に取り入れることができる。その他前
記実施の形態と同一のため同一の符号を付して説明を省
略するが、第1の実施の形態と同一の作用効果を奏する
ものである。
FIG. 2 shows a second embodiment of the present invention. This embodiment is different from the first embodiment in that the electrolytic cell 7 is disposed in the water tank 3 and the opening 8 at the tip thereof is disposed in the salt storage tank 2. It is open. Therefore, the saturated salt water can be introduced into the electrolytic cell 7 through the opening 8. Other components are the same as those of the above-described embodiment, and therefore, the same reference numerals are given and the description is omitted.

【0018】[0018]

【発明の効果】以上のように、この発明によれば、飽和
塩水を電解するため、高濃度の次亜塩素酸ナトリウム溶
液を得ることが出来るものである。そして、塩貯留槽と
別に希釈塩水槽が不要となることから、従来例に比べて
装置を小型化できる利点を有している。
As described above, according to the present invention, a high-concentration sodium hypochlorite solution can be obtained for electrolyzing saturated saline. In addition, since a dilute salt water tank is not required separately from the salt storage tank, there is an advantage that the apparatus can be downsized as compared with the conventional example.

【図面の簡単な説明】[Brief description of the drawings]

【図1】この発明の第1の実施の形態を示す構成図であ
る。
FIG. 1 is a configuration diagram showing a first embodiment of the present invention.

【図2】この発明の第2の実施の形態を示す構成図であ
る。
FIG. 2 is a configuration diagram showing a second embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 槽 2 塩貯留槽 3 水槽 4 仕切壁 7 電解槽 10a,10b 電極 15 移送管 19 給水口 20 流出口 21 塩溶解水給水口 Reference Signs List 1 tank 2 salt storage tank 3 water tank 4 partition wall 7 electrolytic tank 10a, 10b electrode 15 transfer pipe 19 water supply port 20 outlet 21 salt water supply port for dissolved salt water

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C25B 1/00 - 15/08 ──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int. Cl. 7 , DB name) C25B 1/00-15/08

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 塩が貯留される塩貯留槽と、給水口を持
ち塩の溶解水が溜められる水槽が仕切壁を介して併設さ
れ、前記仕切壁には塩の溶解水を前記水槽より前記塩貯
留槽に供給する塩溶解水供給口が形成され、前記塩貯留
槽内に開口する開口部より飽和塩水を取り入れ、この取
り入れた飽和塩水を電気分解する電極が配された電解槽
が設けられ、この電解槽に次亜塩素酸ナトリウム溶液
発生する水素ガスの浮力を利用して前記水槽内に送
り出す移送管が設けられると共に、前記水槽内に生成さ
れる希釈された希釈次亜塩素酸ナトリウム溶液をオーバ
ーフローにて外部へ送り出す流口を設けたことを特徴
とする次亜塩素酸ナトリウム溶液生成装置。
1. A salt storage tank in which salt is stored and a water tank having a water supply port and in which salt water is stored through a partition wall, wherein the salt water is supplied from the water tank to the partition wall. A salt solution supply port for supplying to the salt storage tank is formed, and an electrolytic tank provided with an electrode for taking in saturated salt water from an opening opening in the salt storage tank and electrolyzing the taken saturated salt water is provided. A transfer pipe for feeding the sodium hypochlorite solution into the water tank by utilizing the buoyancy of the generated hydrogen gas in the electrolytic tank, and a diluted diluted hypochlorous acid generated in the water tank. Over sodium solution
Sodium hypochlorite solution generating apparatus characterized in that a flow exit for feeding to the outside at Furo.
JP23374398A 1998-08-20 1998-08-20 Sodium hypochlorite solution generator Expired - Fee Related JP3291619B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23374398A JP3291619B2 (en) 1998-08-20 1998-08-20 Sodium hypochlorite solution generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23374398A JP3291619B2 (en) 1998-08-20 1998-08-20 Sodium hypochlorite solution generator

Publications (2)

Publication Number Publication Date
JP2000064076A JP2000064076A (en) 2000-02-29
JP3291619B2 true JP3291619B2 (en) 2002-06-10

Family

ID=16959890

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23374398A Expired - Fee Related JP3291619B2 (en) 1998-08-20 1998-08-20 Sodium hypochlorite solution generator

Country Status (1)

Country Link
JP (1) JP3291619B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106148994A (en) * 2016-08-29 2016-11-23 潍坊和创环保设备有限公司 Sodium hypochlorite produces and uses generator main frame

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107261877A (en) * 2017-07-12 2017-10-20 深圳市瑞恩医疗器械有限公司 Hypochlorite disinfectant's machine

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106148994A (en) * 2016-08-29 2016-11-23 潍坊和创环保设备有限公司 Sodium hypochlorite produces and uses generator main frame

Also Published As

Publication number Publication date
JP2000064076A (en) 2000-02-29

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