JP3509915B2 - Method and apparatus for removing carbon dioxide component dissolved in water, and electrolyzed water generator equipped with the same - Google Patents

Method and apparatus for removing carbon dioxide component dissolved in water, and electrolyzed water generator equipped with the same

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Publication number
JP3509915B2
JP3509915B2 JP01548094A JP1548094A JP3509915B2 JP 3509915 B2 JP3509915 B2 JP 3509915B2 JP 01548094 A JP01548094 A JP 01548094A JP 1548094 A JP1548094 A JP 1548094A JP 3509915 B2 JP3509915 B2 JP 3509915B2
Authority
JP
Japan
Prior art keywords
water
carbon dioxide
chamber
anode chamber
generated
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
JP01548094A
Other languages
Japanese (ja)
Other versions
JPH07214066A (en
Inventor
陽一郎 清水
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hoshizaki Electric Co Ltd
Original Assignee
Hoshizaki Electric Co Ltd
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Filing date
Publication date
Application filed by Hoshizaki Electric Co Ltd filed Critical Hoshizaki Electric Co Ltd
Priority to JP01548094A priority Critical patent/JP3509915B2/en
Publication of JPH07214066A publication Critical patent/JPH07214066A/en
Application granted granted Critical
Publication of JP3509915B2 publication Critical patent/JP3509915B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/20Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/46Apparatus for electrochemical processes
    • C02F2201/461Electrolysis apparatus
    • C02F2201/46105Details relating to the electrolytic devices
    • C02F2201/46115Electrolytic cell with membranes or diaphragms

Landscapes

  • Degasification And Air Bubble Elimination (AREA)
  • Physical Water Treatments (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、水中に溶存する炭酸ガ
ス成分の除去方法及び除去装置、並びに同除去装置を備
えた電解水生成装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and apparatus for removing carbon dioxide gas components dissolved in water, and an electrolyzed water producing apparatus equipped with the removal apparatus.

【0002】[0002]

【従来の技術】水中には相当量の炭酸ガス成分がC
2,H2CO3,HCO3 -,CO3 2-等の状態で溶存して
おり、用途によってはこれらの炭酸ガス成分を除去する
必要がある。例えば、食塩水を電気分解して酸性水及び
アルカリ性水を生成する場合に使用する原水に上記した
炭酸ガス成分が溶存していると、CO2の生成過電圧が
低いためにCO2ガスの生成に電力が消費されて酸性水
のpHが下がらず、また有効塩素の生成が少なくなると
いう支障が生じる。また、通常の水を電気分解して酸性
水およびアルカリ性水を生成する場合にも、同様のこと
が言える。
2. Description of the Related Art A considerable amount of carbon dioxide gas component in water is C
It is dissolved in the state of O 2 , H 2 CO 3 , HCO 3 , CO 3 2−, etc., and it is necessary to remove these carbon dioxide gas components depending on the application. For example, if the carbon dioxide gas component described above is dissolved in the raw water used in the case of electrolyzing salt water to generate acidic water and alkaline water, the CO 2 generation overvoltage is low, and therefore CO 2 gas is not generated. Electricity is consumed, the pH of the acidic water is not lowered, and the production of available chlorine is reduced, which causes problems. The same can be said when ordinary water is electrolyzed to generate acidic water and alkaline water.

【0003】水中に溶存している炭酸ガス成分の除去方
法としては、膜脱気装置を使用する方法が知られてい
る。膜脱気装置は、刊行物「JETI Vol.40,
NO.4(1992)」に示されているようにガス透過
膜を備え、炭酸ガス成分を溶存する水を同透過膜の一側
に沿って流動させて、同透過膜に付与した内外の差圧に
より水中に溶存する炭酸ガス成分を同透過膜を透過して
除去するものである。
As a method for removing the carbon dioxide gas component dissolved in water, a method using a membrane deaerator is known. The membrane degassing device is described in the publication “JETI Vol.40,
NO. 4 (1992) ”, the water having carbon dioxide gas component dissolved therein is caused to flow along one side of the permeable membrane, and the internal and external differential pressures applied to the permeable membrane are applied. The carbon dioxide component dissolved in water is removed through the permeable membrane.

【0004】[0004]

【発明が解決しようとする課題】ところで、当該ガス透
過膜を使用して炭酸ガス成分を除去する場合、溶存する
炭酸ガス成分中のCO2及びH2CO3成分は除去される
が、HCO3 -及びCO3 2-成分は除去し難く、目的によ
つては十分な除去方法とはいえない。特に、上記した通
常水または塩水の電解により酸性水とアルカリ性水を得
る工程においては、なお上記した問題を解消し得ない。
従って、本発明の目的は、水中に溶存する炭酸ガス成分
を十分に除去し得る除去方法及び除去装置を提供して、
上記した問題を解消することにある。
By the way, when carbon dioxide gas components are removed using the gas permeable membrane, CO 2 and H 2 CO 3 components in the dissolved carbon dioxide gas components are removed, but HCO 3 It is difficult to remove the - and CO 3 2- components, and it cannot be said to be a sufficient removal method depending on the purpose. In particular, in the step of obtaining acidic water and alkaline water by electrolysis of the above-mentioned normal water or salt water, the above-mentioned problems cannot be solved.
Therefore, an object of the present invention is to provide a removal method and a removal device capable of sufficiently removing carbon dioxide gas components dissolved in water,
There is a solution to the above problems.

【0005】[0005]

【課題を解決するための手段】本発明は炭酸ガス成分の
除去方法、除去装置、及び同除去装置を備えた電解水生
成装置に関するもので、第1の発明である炭酸ガス成分
の除去方法は、水に溶存する炭酸ガス成分を除去して中
性水を生成するための炭酸ガス成分の除去方法であっ
て、炭酸ガス成分を溶存する原水を、隔膜にて区画され
た区画室に電極を配置して形成したアノード室及びカソ
ード室に供給して電気分解し、前記アノード室にて生成
した生成水をガス透過膜の一側に沿って流動させて同
透過膜に付与した内外の差圧により生成水中に溶存す
る炭酸ガス成分を前記透過膜を透過して除去し、前記カ
ソード室にて生成した生成水と合体させることを特徴と
するものである。
Means for Solving the Problems The present invention is a method for removing the carbon dioxide component removing apparatus, and relates to electrolytic water generator with the removal device, method for removing carbon dioxide component is a first aspect of the present invention , Removes carbon dioxide components dissolved in water
It is a method of removing carbon dioxide gas component to generate volatile water.
The raw water in which the carbon dioxide gas component is dissolved is supplied to the anode chamber and the cathode chamber formed by arranging the electrodes in the compartments partitioned by the diaphragm to be electrolyzed, and the produced water generated in the anode chamber is generated. the carbon dioxide component dissolved in the product water due to the pressure difference inside and outside granted to the <br/> permeable membrane by flowing along one side of the gas permeable film is removed by passing through the permeable membrane, the mosquito
It is characterized by being combined with the generated water generated in the sword chamber .

【0006】また、本発明の第2の発明である除去装置
は第1の発明を実施するための装置であり、隔膜にて区
画された区画室に電極を配置して形成したアノード室及
びカソード室を有する電解槽と、前記アノード室及びカ
ソード室に炭酸ガス成分を溶存する原水をそれぞれ供給
する一対の原水供給管路と、前記アノード室及びカソー
ド室にて生成したそれぞれの生成水を流出させて互いに
合体させる一対の流出管路を備えてなる電解装置と、ガ
ス透過膜を内蔵するとともに同透過膜の一側に流通路を
有して前記透過膜の内外に差圧が付与される膜脱気装置
を備え、同膜脱気装置の流通路が前記電解槽のアノード
室側生成水の流出管路に接続されていることを特徴する
ものである。
Further, a removing device according to a second aspect of the present invention is a device for carrying out the first aspect of the invention, in which an anode chamber and a cathode are formed by arranging electrodes in compartments partitioned by a diaphragm. An electrolytic cell having a chamber, the anode chamber and the chamber
Supply raw water with dissolved carbon dioxide to the sword chamber
A pair of raw water supply pipes, the anode chamber and the caustic
Each of the generated water generated in the
An electrolyzer comprising a pair of outflow conduits to be combined, and a membrane degasser that contains a gas permeable membrane and has a flow passage on one side of the permeable membrane to provide a differential pressure between the inside and outside of the permeable membrane. An apparatus is provided, and the flow passage of the membrane degassing device is connected to the outflow pipe of the anode chamber side generated water of the electrolytic cell .

【0007】さらにまた、本発明の第3の発明である電
解水生成装置は、第2の発明である除去装置を利用した
電解水生成装置であって、隔膜にて区画された区画室に
電極を配置して形成したアノード室及びカソード室を有
する電解槽と、前記アノード室及びカソード室に炭酸ガ
ス成分を溶存する原水をそれぞれ供給する一対の原水供
給管路と、前記アノード室及びカソード室にて生成した
それぞれの生成水を流出させて互いに合体させる一対の
流出管路を備えてなる電解装置と、ガス透過膜を内蔵す
るとともに同透過膜の一側に流通路を有して前記透過膜
の内外に差圧が付与される膜脱気装置と、前記各流出管
路を介して前記アノード室及びカソード室にて生成した
それぞれの生成水を供給される処理水貯溜槽と、同処理
水貯溜槽に貯留されている処理水を被電解水として前記
アノード室及びカソード室へ供給する被電解水供給管路
と、前記各流出管路に接続され前記アノード室及びカソ
ード室にて生成した各生成水をそれぞれ独立して排出す
る一対の排出管路を備え、前記膜脱気装置が前記アノー
ド室側生成水の流出管路に配設されていることを特徴と
するものである。当該電解水生成装置においては、前記
処理水貯溜槽に塩を付与する塩付与手段を設けて塩水調
製装置に構成して、同塩水調製装置にて調製された塩水
被電解水として前記電解槽の前記アノード室及びカソ
ード室にそれぞれ供給するようにすることができる。
Furthermore, the electrolyzed water producing apparatus which is the third invention of the present invention utilizes the removing apparatus which is the second invention.
A electrolytic water generation apparatus, have the anode and cathode chambers formed by placing the electrode compartment partitioned by a diaphragm
Carbon dioxide gas in the electrolytic chamber and in the anode chamber and cathode chamber.
A pair of raw water supplies that supply raw water in which
Generated in the feed line and the anode chamber and cathode chamber
A pair of discharged waters that combine with each other
An electrolysis apparatus comprising an outflow conduit, a membrane degassing apparatus having a gas permeable membrane built therein and having a flow passage on one side of the permeable membrane to impart a differential pressure to the inside and outside of the permeable membrane, Generated in the anode chamber and cathode chamber through each outflow line
The treated water storage tank to which each produced water is supplied and the treated water stored in the treated water storage tank are used as electrolyzed water.
Pipeline for supplying electrolyzed water to the anode chamber and cathode chamber
And the anode chamber and cathode
Discharge each generated water generated in the room independently
A pair of discharge line that, Ru der which the membrane degassing device is characterized in that it is disposed in the outlet line of the anode chamber side generated water. In the electrolyzed water producing apparatus, the treated water storage tank is provided with a salt applying means for applying salt to the salt water preparing apparatus, and the salt water prepared by the salt water preparing apparatus is used as electrolyzed water in the electrolytic tank. Of the anode chamber and
It is possible to supply each to the room .

【0008】[0008]

【発明の作用・効果】本発明の炭酸ガス成分の除去方法
及び除去装置によれば、電解装置に水を供給するととも
に電解装置の両電極に直流電圧を印加して電気分解する
と、アノード室側の生成水が酸性になるとともにカソー
ド室側の生成水がアルカリ性になる。また、カソード室
内では水中に溶存している炭酸ガス成分のうちHCO3 -
及びCO3 2-成分が隔膜を透過してアノード室内へ移行
するため、カソード室内には炭酸ガス成分は存在しなく
なる。一方、アノード室側においては生成水が酸性でp
Hが低いため、HCO3 -及びCO3 2-成分はCO2及びH
2CO3成分に変換されて、アノード室内の生成水は炭酸
ガス成分中CO2及びH2CO3成分のみが溶存するもの
となり、これら両成分のうちCO2の一部がガスとして
除去される。
According to the method and apparatus for removing carbon dioxide gas components of the present invention, when water is supplied to the electrolyzer and a DC voltage is applied to both electrodes of the electrolyzer to cause electrolysis, the anode chamber side The generated water of the above becomes acidic and the generated water of the cathode chamber side becomes alkaline. Further, of the carbon dioxide component dissolved in the water at the cathode chamber HCO 3 -
Since the CO 3 2− component and the CO 3 2− component permeate the diaphragm and move into the anode chamber, the carbon dioxide gas component does not exist in the cathode chamber. On the other hand, in the anode chamber side, the generated water is acidic and p
Since H is low, HCO 3 and CO 3 2− components are CO 2 and H
The CO 2 and H 2 CO 3 components in the carbon dioxide gas component are dissolved in the produced water in the anode chamber after being converted into 2 CO 3 components, and a part of CO 2 in these components is removed as a gas. .

【0009】アノード室側の生成水は、その後膜脱気装
置に供給されてガス透過膜の一側に沿って流動する間に
透過膜の内外の差圧の作用により生成水中のガス分離が
起こり、CO2及びH2CO3成分は透過膜を透過して分
離除去される。従って、膜脱気装置から流出したアノー
ド室側生成水は、炭酸ガス成分をほぼ完全に除去された
状態になり、当該アノード室側生成水をカソード側生成
水と合体すれば、炭酸ガス成分の除去された中性水とな
る。
The produced water on the anode chamber side is then supplied to the membrane degassing device and flows along one side of the gas permeable membrane, so that gas separation in the produced water occurs due to the action of the differential pressure between the inside and outside of the permeable membrane. , CO 2 and H 2 CO 3 components permeate the permeable membrane and are separated and removed. Therefore , the produced water on the anode chamber side that has flowed out from the membrane degasser is in a state in which the carbon dioxide gas component is almost completely removed, and the produced water on the anode chamber side is produced on the cathode side.
When combined with water, it becomes neutral water from which carbon dioxide gas components have been removed .

【0010】また、本発明の電解水生成装置において
は、最初に原水を電解装置に供給して電気分解するとと
もに、アノード室側生成水を膜脱気装置に供給して溶存
する炭酸ガス成分を分離除去することにより、処理水貯
溜槽に炭酸ガス成分が溶存しない水をアノード室側及び
カソード室側から供給することができ、同水により電気
分解に必要な脱炭酸水を確保し、または電気分解に必要
な所定濃度の塩水を調製することができる。このため、
必要量の脱炭酸水または塩水が調製されると、電解装置
への供給水を原水から処理水貯溜槽に切換て脱炭酸水ま
たは塩水の電気分解を行うことができる。従って、当該
電解水生成装置により、炭酸ガス成分が溶存しない水を
生成することができるとともに、同水を原水として脱炭
酸水または必要濃度の塩水を調製して電気分解して、ア
ノード室側に酸性水を生成することができるとともに、
カソード室側にアルカリ性水を生成することができる。
Further, in the electrolyzed water producing apparatus of the present invention, first, raw water is supplied to the electrolyzing apparatus to be electrolyzed, and the produced water in the anode chamber side is supplied to the membrane degassing apparatus to dissolve dissolved carbon dioxide gas components. By separating and removing, it is possible to supply the treated water storage tank with water in which the carbon dioxide gas component is not dissolved from the anode chamber side and the cathode chamber side, and the decarbonated water necessary for electrolysis is secured by this water, or It is possible to prepare salt water having a predetermined concentration required for decomposition. For this reason,
When the required amount of decarbonated water or salt water is prepared, the feed water to the electrolyzer can be switched from raw water to the treated water storage tank for electrolysis of decarbonated water or salt water. Therefore, the electrolyzed water generator can generate water in which the carbon dioxide gas component is not dissolved, and the same water is used as raw water to prepare decarbonated water or salt water having a required concentration, which is electrolyzed to the anode chamber side. Along with being able to generate acidic water,
It is possible to generate alkaline water on the cathode chamber side.

【0011】[0011]

【実施例】以下本発明の実施例を説明すると、図1には
本発明に係る炭酸ガス成分の除去装置が示されている。
当該除去装置は電解装置10と膜脱気装置20とからな
るもので、電解装置10は電解槽11内に配設されてそ
の内部を2つの区画室に区画する隔膜12と、各区画室
に配設した陽極板13と陰極板14とを備えたもので、
一方の区画室に陽極板13が配設されてアノード室Ra
に形成されており、かつ他方の区画室には陰極板14が
配設されてカソード室Rbに形成されている。電解槽1
1には原水供給源に接続された原水供給管路である
1,第2供給管路11a,11bと、貯溜槽に接続され
た第1,第2流出管路11c,11dが接続されてい
る。第1供給管路11a及び第1流出管路11cはアノ
ード室Raに連結され、かつ第2供給管路11b及び第
2流出管路11dはカソード室Rbに連結されている。
電解装置10においては、各電極板13,14に直流電
圧が印加される。膜脱気装置20は電解装置10におけ
る第1流出管路11cに配設されている。
EXAMPLE An example of the present invention will be described below. FIG. 1 shows a carbon dioxide gas component removing device according to the present invention.
The removal device is composed of an electrolysis device 10 and a membrane degassing device 20, and the electrolysis device 10 is arranged in an electrolytic cell 11 and a diaphragm 12 for partitioning the inside into two compartments, and a partition 12 for each compartment. A positive electrode plate 13 and a negative electrode plate 14 provided,
The anode plate 13 is disposed in one of the compartments and the anode chamber Ra is
And the cathode plate 14 is disposed in the other compartment to form the cathode chamber Rb. Electrolyzer 1
1, the first and second supply pipelines 11a and 11b, which are raw water supply pipelines connected to the raw water supply source, and the first and second outflow pipelines 11c and 11d connected to the reservoir are connected. There is. The first supply pipeline 11a and the first outflow pipeline 11c are connected to the anode chamber Ra, and the second supply pipeline 11b and the second outflow pipeline 11d are connected to the cathode chamber Rb.
In the electrolysis device 10, a DC voltage is applied to each of the electrode plates 13 and 14. The membrane degassing device 20 is arranged in the first outflow conduit 11c of the electrolysis device 10.

【0012】膜脱気装置20は、ハウジング21内に合
成繊維の中空糸を束状にしたモジュール22を内蔵した
もので、モジュール22がガス透過膜を構成している。
当該膜脱気装置20においては、モジュール22を構成
する各中空糸内にアノード室Ra側の生成水が流通し、
一方ハウジング21に設けた管路23を通して負圧が付
与されて中空糸の外側が真空にされる。
The membrane deaerator 20 has a module 21 in which hollow fibers of synthetic fibers are bundled in a housing 21, and the module 22 constitutes a gas permeable membrane.
In the membrane deaerator 20, the generated water on the anode chamber Ra side flows in each hollow fiber forming the module 22,
On the other hand, a negative pressure is applied through the conduit 23 provided in the housing 21 so that the outside of the hollow fiber is evacuated.

【0013】当該除去装置においては、電解装置10の
アノード室Ra及びカソード室Rbに原水を供給すると
ともに電解装置10の両電極13,14に直流電圧を印
加して電気分解するととともに、膜脱気装置20に負圧
を付与してモジュール22の各中空糸の外側を真空状態
として、アノード室Raの生成水を各中空糸の内部を流
通させる。この場合、電解装置10においては、アノー
ド室Ra側の生成水が酸性となり、かつカソード室Rb
側の生成水がアルカリ性となる。また、カソード室Rb
内では、水中に溶存している炭酸ガス成分のうちHCO
3 -及びCO 2−成分が隔膜12を透過してアノード室
Ra内へ移行するため、カソード室Rb内には炭酸ガス
成分は存在しなくなる。一方、アノード室Ra側生成水
は酸性でpHが低いため、HCO 及びCO3 2-成分
はCO2及びH2CO3成分に変換されてアノード室Ra
内の生成水は炭酸ガス成分中CO2及びH2CO3成分の
みを溶存した状態となり、これら両成分のうちCO2
一部がガスとなって除去される。
In the removal device, raw water is supplied to the anode chamber Ra and the cathode chamber Rb of the electrolysis device 10 and a direct current voltage is applied to both electrodes 13 and 14 of the electrolysis device 10 for electrolysis and membrane degassing. A negative pressure is applied to the device 20 to bring the outside of each hollow fiber of the module 22 into a vacuum state, and the generated water in the anode chamber Ra is circulated inside each hollow fiber. In this case, in the electrolysis device 10, the produced water on the anode chamber Ra side becomes acidic and the cathode chamber Rb
The generated water on the side becomes alkaline. Also, the cathode chamber Rb
Of the carbon dioxide gas dissolved in water, HCO
Since the 3 and CO 3 2− components pass through the diaphragm 12 and move into the anode chamber Ra, the carbon dioxide gas component does not exist in the cathode chamber Rb. On the other hand, since the water produced in the anode chamber Ra side is acidic and has a low pH, the HCO 3 and CO 3 2− components are converted into CO 2 and H 2 CO 3 components and the anode chamber Ra
The produced water therein is in a state in which only CO 2 and H 2 CO 3 components in the carbon dioxide gas component are dissolved, and a part of CO 2 of these components is removed as a gas.

【0014】アノード室Ra側の生成水は、その後膜脱
気装置20内にて各中空糸内を流通する間にそれらの内
外の差圧の作用により生成水中のガス分離が起こり、C
2及びH2CO3成分は各中空糸を透過して分離除去さ
れる。従って、カソード室Rb側の生成水、及び膜脱気
装置20から流出したアノード室Ra側の生成水は炭酸
ガス成分をほぼ完全に除去された状態となり、その後合
体して流出する。
The produced water on the side of the anode chamber Ra is separated into gas in the produced water by the action of the pressure difference between the inside and the outside of the hollow fibers while flowing through each hollow fiber in the membrane deaerator 20.
The O 2 and H 2 CO 3 components permeate each hollow fiber and are separated and removed. Therefore, the produced water on the cathode chamber Rb side and the produced water on the anode chamber Ra side that has flowed out from the membrane degassing device 20 are in a state in which the carbon dioxide gas component has been almost completely removed, and then coalesce and flow out.

【0015】図2には本発明の第2実施例である電解水
生成装置が示されている。当該生成装置は電解装置10
と、膜脱気装置20と、塩水調製装置30とを備えてい
る。電解装置10及び膜脱気装置20は、図1に示す第
1実施例の炭酸ガス成分除去装置における電解装置及び
膜脱気装置と同一構成のものである。また、塩水調製装
置30は貯溜槽31と濃食塩水槽32を備え、一定量の
水を貯溜した貯溜槽31内に濃食塩水槽32から一定量
の濃食塩水が添加されて、所定濃度の希食塩水が調製さ
れる。
FIG. 2 shows an electrolyzed water producing apparatus which is a second embodiment of the present invention. The generator is the electrolyzer 10.
And a membrane degassing device 20 and a salt water preparation device 30. The electrolysis device 10 and the membrane degassing device 20 have the same structure as the electrolysis device and the membrane degassing device in the carbon dioxide gas component removing device of the first embodiment shown in FIG. Further, the salt water preparation device 30 includes a storage tank 31 and a concentrated saline solution tank 32, and a fixed amount of concentrated saline solution is added from the concentrated saline solution tank 32 into the storage tank 31 that stores a fixed amount of water to obtain a dilute solution having a predetermined concentration. Saline is prepared.

【0016】しかして、電解装置10においては、電解
槽11が原水供給管路である第1供給管路41aにより
原水供給源に接続されているとともに、被電解水供給管
路である第2供給管路42aにより塩水調製装置30の
貯溜槽31に接続され、また第1流出管路43a,第2
流出管路44aにより貯溜槽31に接続されている。ま
た、各流出管路43a,44aには第1,第2排出管路
45a,46aが接続されている。これら各管路41a
〜46aにはそれぞれ開閉バルブ41b〜46bが介装
されているとともに、第1流出管路43aにおけるバル
ブ43bの下流側に膜脱気装置20が配設されている。
In the electrolysis apparatus 10, however, the electrolytic cell 11 is connected to the raw water supply source by the first supply pipeline 41a which is a raw water supply pipeline , and the electrolyzed water supply pipeline is provided.
It is connected to the storage tank 31 of the salt water preparation device 30 by the second supply pipe line 42a which is a line, and the first outflow pipe line 43a
It is connected to the storage tank 31 by an outflow conduit 44a. Further, the first and second discharge pipelines 45a and 46a are connected to the outflow pipelines 43a and 44a. Each of these pipelines 41a
Opening / closing valves 41b to 46b are respectively provided in the through holes 46a to 46a, and the membrane degassing device 20 is provided downstream of the valve 43b in the first outflow conduit 43a.

【0017】かかる構成の電解水生成装置においては、
各バルブ41b,43b,44bが開放状態でかつ各バ
ルブ42b,45b,46bが閉止状態で原水が電解槽
11へ供給され、電解槽11において第1実施例の除去
装置におけると同様に原水の電気分解が生じて、アノー
ド室Ra側の生成水は炭酸ガス成分中のCO2及びH2
3成分のみが溶存するものとなって、膜脱気装置20
に供給され、またカソード室Rb側の生成水は炭酸ガス
成分が溶存しないものとなって、塩水調製装置30の貯
溜槽31に供給される。アノード室Ra側の生成水は膜
脱気装置20にてCO2及びH2CO3成分を除去され
て、貯溜槽31に供給される。従って、貯溜槽31内の
水は炭酸ガス成分が溶存しない水であって、電気分解に
供する食塩水の調製用の原水として好適である。
In the electrolyzed water producing apparatus having the above construction,
Raw water is supplied to the electrolytic cell 11 with the valves 41b, 43b, 44b in the open state and the valves 42b, 45b, 46b in the closed state, and the raw water is supplied to the electrolytic cell 11 in the same manner as in the removing apparatus of the first embodiment. As a result of the decomposition, the water produced on the side of the anode chamber Ra becomes CO 2 and H 2 C in the carbon dioxide gas component.
Only the O 3 component is dissolved, and the membrane degassing device 20
In addition, the produced water on the cathode chamber Rb side has no carbon dioxide gas dissolved therein and is supplied to the storage tank 31 of the salt water preparation device 30. The produced water on the side of the anode chamber Ra is supplied to the storage tank 31 after the CO 2 and H 2 CO 3 components are removed by the membrane deaerator 20. Therefore, the water in the storage tank 31 is water in which carbon dioxide gas components are not dissolved, and is suitable as raw water for preparing saline solution to be subjected to electrolysis.

【0018】当該電解水生成装置においては、貯溜槽3
1内の水が所定量に達すると原水の供給が停止されると
ともに、電解槽11内の水が排出される。一方、塩水調
製装置30においては、貯溜槽31内に濃食塩水槽32
から一定量の濃食塩水が添加されて、所定濃度の希食塩
水が調製される。希食塩水が調製されると、各バルブ4
1b,43b,44bが閉止状態でかつ各バルブ42
b,45b,46bが開放状態で希食塩水が電解槽11
へ供給され、電解槽11においては食塩水の電気分解が
なされ、アノード室Ra内では酸性水が生成されるとと
もに、カソード室Rb内ではアルカリ性水が生成され、
これらの各電解生成水は各排出管路45a,46aを経
て所定の場所へ排出される。
In the electrolyzed water producing apparatus, the storage tank 3
When the water in 1 reaches a predetermined amount, the supply of raw water is stopped and the water in the electrolytic cell 11 is discharged. On the other hand, in the salt water preparation device 30, a concentrated salt water tank 32 is provided inside the storage tank 31.
A fixed amount of concentrated saline solution is added to prepare a dilute saline solution having a predetermined concentration. When diluted saline is prepared, each valve 4
1b, 43b, 44b are closed and each valve 42
b, 45b, 46b are open, and dilute saline is used in the electrolytic cell 11
And is electrolyzed in the electrolytic cell 11 to generate acidic water in the anode chamber Ra and alkaline water in the cathode chamber Rb.
Each of these electrolyzed water is discharged to a predetermined place through each of the discharge pipe lines 45a and 46a.

【0019】このように、当該電解水生成装置において
は、最初に原水を電解装置10に供給して電気分解する
とともにアノード室Ra側の生成水を膜脱気装置20に
供給して、溶存する炭酸ガス成分を分離除去することに
より、塩水調製装置30の貯溜槽31に炭酸ガス成分が
溶存しない水をアノード室Ra側及びカソード室Rb側
から必要量供給することができ、同水により電気分解に
必要な濃度の食塩水を調製することができる。また、必
要量の食塩水が調製されると、電解装置10への供給水
を原水から食塩水に切換て塩水の電気分解を行うことが
できる。従って、当該電解水生成装置により、炭酸ガス
成分が溶存しない水を生成することができるとともに、
同水を原水として必要濃度の食塩水を調製し効率良く電
気分解して、アノード室Ra側に酸性水を生成すること
ができるとともに、カソード室Rb側にアルカリ性水を
生成することができる。
As described above, in the electrolyzed water producing apparatus, the raw water is first supplied to the electrolyzing apparatus 10 for electrolysis, and the produced water on the anode chamber Ra side is supplied to the membrane degassing apparatus 20 to be dissolved. By separating and removing the carbon dioxide gas component, a required amount of water in which the carbon dioxide gas component is not dissolved can be supplied to the storage tank 31 of the salt water preparation device 30 from the anode chamber Ra side and the cathode chamber Rb side, and the electrolysis is performed by the water. It is possible to prepare a saline solution having a required concentration. Further, when a required amount of saline solution is prepared, the supply water to the electrolysis device 10 can be switched from raw water to saline solution to perform electrolysis of saline solution. Therefore, with the electrolyzed water generator, it is possible to generate water in which the carbon dioxide component is not dissolved,
Using the same water as raw water, a saline solution having a required concentration can be prepared and efficiently electrolyzed to generate acidic water on the anode chamber Ra side and alkaline water on the cathode chamber Rb side.

【0020】なお、当該電解水生成装置においては、塩
水調製装置30の貯溜槽31のみを使用するかまたは濃
食塩水槽32を廃止して、貯溜槽31から炭酸ガス成分
を除去された脱炭酸水を電解装置10へ供給して、脱炭
酸水を電気分解するように変更することができる。
In the electrolyzed water producing apparatus, only the storage tank 31 of the salt water preparing apparatus 30 is used, or the concentrated saline solution tank 32 is abolished and the carbon dioxide gas component is removed from the storage tank 31. Can be supplied to the electrolyzer 10 and modified to electrolyze decarbonated water.

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

【図1】本発明に係る炭酸ガス成分の除去装置の概略構
成図である。
FIG. 1 is a schematic configuration diagram of a carbon dioxide gas removing device according to the present invention.

【図2】本発明に係る電解水生成装置の概略構成図であ
る。
FIG. 2 is a schematic configuration diagram of an electrolyzed water generator according to the present invention.

【符号の説明】[Explanation of symbols]

10…電解装置、11c…流出管路、20…膜脱気装
置、30…塩水調製装置、41a,42a…供給管路、
43a,44a…流出管路、45a,46a…排出管
路、Ra…アノード室、Rb…カソード室。
10 ... Electrolysis device, 11c ... Outflow pipe line, 20 ... Membrane degassing device, 30 ... Salt water preparation device, 41a, 42a ... Supply pipe line,
43a, 44a ... Outflow line, 45a, 46a ... Discharge line, Ra ... Anode chamber, Rb ... Cathode chamber.

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平6−296966(JP,A) 特開 平4−108353(JP,A) 特開 平2−52088(JP,A) 特開 平5−138171(JP,A) 特開 平5−220480(JP,A) 特開 平5−123676(JP,A) 実開 平5−26194(JP,U) (58)調査した分野(Int.Cl.7,DB名) C02F 1/46 B01D 19/00 C02F 1/20 ─────────────────────────────────────────────────── ─── Continuation of the front page (56) Reference JP-A-6-296966 (JP, A) JP-A-4-108353 (JP, A) JP-A-2-52088 (JP, A) JP-A-5- 138171 (JP, A) JP-A-5-220480 (JP, A) JP-A-5-123676 (JP, A) Actual Kaihei 5-26194 (JP, U) (58) Fields investigated (Int.Cl. 7 , DB name) C02F 1/46 B01D 19/00 C02F 1/20

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】水に溶存する炭酸ガス成分を除去して中性
水を生成するための炭酸ガス成分の除去方法であり、
酸ガス成分を溶存する原水を、隔膜にて区画された区画
室に電極を配置して形成したアノード室及びカソード室
に供給して電気分解し、前記アノード室にて生成した生
成水をガス透過膜の一側に沿って流動させて同透過膜
に付与した内外の差圧により生成水中に溶存する炭酸
ガス成分を前記透過膜を透過して除去し、前記カソード
室にて生成した生成水と合体させることを特徴とする水
中に溶存する炭酸ガス成分の除去方法。
1. Neutral by removing carbon dioxide gas components dissolved in water
A method of removing carbon dioxide gas components to generate water, in which raw water in which carbon dioxide gas components are dissolved is supplied to an anode chamber and a cathode chamber formed by arranging electrodes in compartments partitioned by a diaphragm to generate electricity. decomposition, the water generated by the anode chamber, wherein the permeable membrane carbon dioxide gas components dissolved in the product water by internal and external differential pressure was applied to the permeable membrane by flowing along one side of the gas permeable membrane Permeate and remove the cathode
A method for removing carbon dioxide gas components dissolved in water, characterized in that it is combined with generated water generated in a chamber .
【請求項2】水に溶存する炭酸ガス成分を除去して中性
水を生成するための炭酸ガス成分の除去装置であり、
膜にて区画された区画室に電極を配置して形成したアノ
ード室及びカソード室を有する電解槽と、前記アノード
室及びカソード室に炭酸ガス成分を溶存する原水をそれ
ぞれ供給する一対の原水供給管路と、前記アノード室及
びカソード室にて生成したそれぞれの生成水を流出させ
て互いに合体させる一対の流出管路を備えてなる電解装
置と、ガス透過膜を内蔵するとともに同透過膜の一側に
流通路を有して前記透過膜の内外に差圧が付与される膜
脱気装置を備え、同膜脱気装置の流通路が前記電解槽
アノード室側生成水の流出管路に接続されていることを
特徴する水中に溶存する炭酸ガス成分の除去装置。
2. Neutral by removing carbon dioxide gas components dissolved in water
A device for removing carbon dioxide gas components for producing water, an electrolytic cell having an anode chamber and a cathode chamber formed by arranging electrodes in compartments partitioned by a diaphragm, and the anode
The raw water containing dissolved carbon dioxide in the chamber and cathode chamber
A pair of raw water supply pipes for supplying the raw water and the anode chamber and
And the generated water generated in the cathode chamber
And a membrane having a gas permeable membrane and having a flow passage on one side of the permeable membrane to provide a differential pressure between the inside and outside of the permeable membrane. A device for removing a carbon dioxide gas component dissolved in water, comprising a deaerator, wherein the flow passage of the membrane deaerator is connected to an outflow pipe of the produced water on the anode chamber side of the electrolytic cell .
【請求項3】炭酸ガス成分を溶存しない水を被電解水と
する電解水生成装置であり、隔膜にて区画された区画室
に電極を配置して形成したアノード室及びカソード室
有する電解槽と、前記アノード室及びカソード室に炭酸
ガス成分を溶存する原水をそれぞれ供給する一対の原水
供給管路と、前記アノード室及びカソード室にて生成し
たそれぞれの生成水を流出させて互いに合体させる一対
の流出管路を備えてなる電解装置と、ガス透過膜を内蔵
するとともに同透過膜の一側に流通路を有して前記透過
膜の内外に差圧が付与される膜脱気装置と、前記各流出
管路を介して前記アノード室及びカソード室にて生成し
たそれぞれの生成水を供給される処理水貯溜槽と、同処
理水貯溜槽に貯留されている処理水を被電解水として前
記アノード室及びカソード室へ供給する被電解水供給管
路と、前記各流出管路に接続され前記アノード室及びカ
ソード室にて生成した各生成水をそれぞれ独立して排出
する一対の排出管路を備え、前記膜脱気装置が前記アノ
ード室側生成水の流出管路に配設されていることを特徴
とする水中に溶存する炭酸ガス成分の除去装置を備えた
電解水生成装置。
3. Water which does not dissolve carbon dioxide gas is used as electrolyzed water.
An electrolytic water generation apparatus for the anode and cathode chambers formed by placing the electrode compartment partitioned by a diaphragm
Carbon dioxide in the electrolytic cell and the anode chamber and cathode chamber
A pair of raw water that supplies raw water in which gas components are dissolved
Generated in the supply line and the anode chamber and cathode chamber
A pair that let each produced water flow out and combine with each other
An electrolysis apparatus comprising an outflow pipe line, and a membrane degassing apparatus having a gas permeable membrane and having a flow passage on one side of the permeable membrane to impart a differential pressure to the inside and outside of the permeable membrane, Generated in the anode chamber and the cathode chamber through each of the outflow pipes.
The treated water storage tank to which each generated water is supplied and the treated water stored in the treated water storage tank are treated as electrolyzed water.
Electrolyzed water supply pipe for supplying to the anode chamber and cathode chamber
Channel, connected to each of the outflow lines and the anode chamber and
Discharge each generated water generated in the sword chamber independently
A pair of discharge line for electrolyte to the membrane degasifier is provided with a device for removing carbon dioxide component dissolved in the water, characterized in that disposed on the outlet line of the anode chamber side generated water Water generator.
【請求項4】請求項3に記載の電解水生成装置におい
て、前記処理水貯溜槽に塩を付与する塩付与手段を設け
て塩水調製装置に構成して、同塩水調製装置にて調製さ
れた塩水を被電解水として前記電解槽の前記アノード室
及びカソード室にそれぞれ供給するようにしたことを特
徴とする電解水生成装置。
4. The electrolyzed water producing apparatus according to claim 3, wherein the treated water storage tank is provided with a salt applying means for applying salt to constitute a salt water preparation apparatus, and the salt water preparation apparatus is prepared. Using the salt water as electrolyzed water, the anode chamber of the electrolytic cell
And a cathode chamber, respectively .
JP01548094A 1994-02-09 1994-02-09 Method and apparatus for removing carbon dioxide component dissolved in water, and electrolyzed water generator equipped with the same Expired - Fee Related JP3509915B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP01548094A JP3509915B2 (en) 1994-02-09 1994-02-09 Method and apparatus for removing carbon dioxide component dissolved in water, and electrolyzed water generator equipped with the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP01548094A JP3509915B2 (en) 1994-02-09 1994-02-09 Method and apparatus for removing carbon dioxide component dissolved in water, and electrolyzed water generator equipped with the same

Publications (2)

Publication Number Publication Date
JPH07214066A JPH07214066A (en) 1995-08-15
JP3509915B2 true JP3509915B2 (en) 2004-03-22

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ID=11889961

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Country Link
JP (1) JP3509915B2 (en)

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* Cited by examiner, † Cited by third party
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JP4680610B2 (en) * 2005-01-19 2011-05-11 ホシザキ電機株式会社 Method and apparatus for producing sanitized water
JP2007130593A (en) * 2005-11-11 2007-05-31 Hoshizaki Electric Co Ltd Electrolytic water generator

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0829315B2 (en) * 1988-08-15 1996-03-27 オルガノ株式会社 Demineralized water production equipment
JPH088838B2 (en) * 1990-08-25 1996-01-31 龍夫 岡崎 Manufacturing method of boiled noodles
JPH0526194U (en) * 1991-09-18 1993-04-06 イーグル工業株式会社 Electrolytic water purifier
JP2624918B2 (en) * 1991-11-07 1997-06-25 株式会社ガラキシヤ Acidic / alkaline water production method
JPH05138171A (en) * 1991-11-25 1993-06-01 Eagle Ind Co Ltd Electrolytic water purifier
JPH05220480A (en) * 1992-02-10 1993-08-31 Miura Co Ltd Pure water manufacturing apparatus
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Also Published As

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