JPH1085746A - Electrolytic ionic water preparation process - Google Patents

Electrolytic ionic water preparation process

Info

Publication number
JPH1085746A
JPH1085746A JP24945996A JP24945996A JPH1085746A JP H1085746 A JPH1085746 A JP H1085746A JP 24945996 A JP24945996 A JP 24945996A JP 24945996 A JP24945996 A JP 24945996A JP H1085746 A JPH1085746 A JP H1085746A
Authority
JP
Japan
Prior art keywords
water
electrolytic
voltage
approximately
alkaline
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.)
Pending
Application number
JP24945996A
Other languages
Japanese (ja)
Inventor
Atsushi Takayasu
淳 高安
Naoto Miyashita
直人 宮下
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP24945996A priority Critical patent/JPH1085746A/en
Publication of JPH1085746A publication Critical patent/JPH1085746A/en
Pending legal-status Critical Current

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  • Water Treatment By Electricity Or Magnetism (AREA)
  • Cleaning Or Drying Semiconductors (AREA)

Abstract

PROBLEM TO BE SOLVED: To prepare highly purified ionic water for a long period of time by discharging acidic water and alkaline water for the given time and then applying reverse voltage of the pulse shape less than electrolytic voltage to a positive electrode and a negative electrode to remove metallic ions contained in the electrolytic ionic water. SOLUTION: For instance, when metallic ions are started to increase after electrolysis using the electrolytic voltage of approximately 20V is carried out for the given time, the polarity of a power source 4 is reversed, and the pulse reverse voltage of approximately -10V is applied. The pulse frequency at that time is set as approximately 0.25 Ha , and the reverse voltage application time is set as approximately one minute. During the time of power application, an acidic water discharge valve 15 and an alkaline water discharge valve 16 are closed, while an anode chamber drain outlet valve 17 and a cathode chamber drain outlet valve 18 are opened. Ionic water of increased metallic ion concentration is discharged by the arrangement. After the above treatment, the polarity of the power source 4 is reversed, and the voltage is reversed by approximately 20V, and the opening and closing of valves 15-18 are also reversed. The supply of ionic water is restarted by the arrangement.

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】本発明は電解イオン水生成方
法に関するものであり、特に半導体基板洗浄に用いられ
る高純度電解イオン水の生成方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing electrolytic ionic water, and more particularly to a method for producing high-purity electrolytic ionic water used for cleaning semiconductor substrates.

【0002】[0002]

【従来の技術】従来、半導体ウェハの洗浄は一般に高純
度の酸、アルカリ水溶液を用いて行われてきた。ところ
が、半導体ウェハの大口径化が進み、使用する酸、アル
カリの量が増大し、排水処理にかかる費用も含め、洗浄
工程にかかる費用が増加を続けている。
2. Description of the Related Art Conventionally, cleaning of a semiconductor wafer has been generally carried out using an aqueous solution of a high-purity acid or alkali. However, as the diameter of semiconductor wafers increases, the amount of acid and alkali used increases, and the cost of the cleaning process, including the cost of wastewater treatment, continues to increase.

【0003】そこで、本発明者は、医療分野において用
いられている、例えば、水道水を電気分解し、医療飲料
水として使用するアルカリ性イオン水と、消毒用として
使用する酸性イオン水とを生成する電解イオン水生成装
置を用い、従来の酸、アルカリ水溶液に代えて高純度純
水を電気分解し酸性水、アルカリ性水の電解イオン水を
半導体ウェハ洗浄に使用することを試みた。
Therefore, the present inventor electrolyzes, for example, tap water used in the medical field to produce alkaline ionized water used as medical drinking water and acidic ionized water used for disinfection. Using an electrolytic ionized water generator, an attempt was made to electrolyze high-purity pure water instead of the conventional acid and alkali aqueous solutions and use the electrolytic ionized water of acidic water and alkaline water for cleaning semiconductor wafers.

【0004】次に上記試みについて説明する。図2
(A)は、電解イオン水生成装置の要部の概略を示し、
同図(B)は生成装置ユニットを示す。
Next, the above-mentioned attempt will be described. FIG.
(A) shows an outline of a main part of an electrolytic ionized water generator,
FIG. 2B shows a generator unit.

【0005】図2(A)に示すように、電解イオン水生
成装置は、5個の生成装置ユニット100からなり、各
ユニット100は、図2(B)に示すように、イオン交
換隔膜2によって陽極室1aと陰極室1bに分割された
電解槽1を有している。前記陽極室1a内には白金から
なる陽電極3a、陰電極1b内にはチタンからなる陰電
極3bがそれぞれ挿入され、電解電源4から電解電流の
通電が行われるようになっている。前記電解槽1には陽
極室1aに通じる原水供給口5a、陰極室1bに通じる
原水供給口5bがそれぞれ設けられ、また反対側には酸
性水を吐出する吐水口6a及び陽極室の排水口7a、ア
ルカリ性水を吐出する吐水口6b及び陰極室の排水口7
bがそれぞれ設けられている。そして図2(A)に示す
ように、各ユニット100の原水供給口5a、5bは原
水供給管8、酸性水の吐水口6aは共通の吐水管9、ア
ルカリ性水の吐水口6bは共通の吐水管10、陽極室の
排水口7aは共通の排水管11、陰極室の排水口7bは
共通の排水管12にそれぞれ連結されている。なお、1
3、14、15、16、17、18は、何れもバルブで
ある。
As shown in FIG. 2A, the electrolytic ionic water generator comprises five generator units 100. Each unit 100 is formed by an ion exchange membrane 2 as shown in FIG. 2B. It has an electrolytic cell 1 divided into an anode chamber 1a and a cathode chamber 1b. A positive electrode 3a made of platinum is inserted in the anode chamber 1a, and a negative electrode 3b made of titanium is inserted in the negative electrode 1b, so that an electrolytic current flows from an electrolytic power supply 4. The electrolytic cell 1 is provided with a raw water supply port 5a communicating with the anode chamber 1a and a raw water supply port 5b communicating with the cathode chamber 1b. On the other side, a water discharge port 6a for discharging acidic water and a drain port 7a for the anode chamber are provided. , An outlet 6b for discharging alkaline water, and a drain 7 for the cathode chamber
b are provided respectively. Then, as shown in FIG. 2A, the raw water supply ports 5a and 5b of each unit 100 are the raw water supply pipe 8, the acidic water discharge port 6a is a common discharge pipe 9, and the alkaline water discharge port 6b is a common discharge port. The water pipe 10 and the drain port 7a of the anode chamber are connected to a common drain pipe 11, and the drain port 7b of the cathode chamber is connected to a common drain pipe 12. In addition, 1
3, 14, 15, 16, 17, and 18 are all valves.

【0006】次に、この電解イオン水生成装置を用いて
電解イオン水を生成する方法を説明する。まず、原水供
給管8に原水として高純度の純水を供給し、原水供給口
5aより陽極室1a、原水供給口5bより陰極室1b内
に純水を供給した後、陽電極3aと陰電極3bに通電
し、純水を電気分解することによって陽極室1aに酸性
水、陰極室1bにアルカリ性水を電解生成する。そして
各ユニット100で生成した酸性水を吐水口6aより共
通の酸性水の吐水管9、アルカリ性水を吐水口6bより
共通のアルカリ性水の吐水管10にそれぞれ取り出す。
Next, a method for producing electrolytic ionic water using the electrolytic ionic water producing apparatus will be described. First, high-purity pure water is supplied to the raw water supply pipe 8 as raw water, pure water is supplied from the raw water supply port 5a into the anode chamber 1a, and from the raw water supply port 5b into the cathode chamber 1b, and then the positive electrode 3a and the negative electrode are supplied. 3b, electricity is generated, and pure water is electrolyzed to electrolyze acidic water in the anode chamber 1a and alkaline water in the cathode chamber 1b. Then, the acidic water generated in each unit 100 is taken out from a common water discharge pipe 9 from the water discharge port 6a, and the alkaline water is taken out to a common alkaline water discharge pipe 10 from the water discharge port 6b.

【0007】[0007]

【発明が解決しようとする課題】しかし、このような電
解イオン水生成装置を用いて電解イオン水を長時間連続
して生成すると、陽電極、陰電極から、電極の構成材料
である、白金、鉄、クロム等の金属イオンがイオン水中
に溶解する。
However, when electrolytic ionic water is continuously generated for a long time using such an electrolytic ionic water generator, platinum, which is a constituent material of the electrode, is converted from the positive electrode and the negative electrode. Metal ions such as iron and chromium dissolve in ionic water.

【0008】これらの金属イオンは陽イオンであるた
め、印加された電界により陰電極3bに引き寄せられ、
陰電極3bに付着ないし、電極近傍に集合する。そし
て、これらの金属イオンはアルカリ性イオン水に混入
し、アルカリ性水の吐出口6bより、共通のアルカリ性
水の吐出管10を経由して取り出される。
Since these metal ions are positive ions, they are attracted to the negative electrode 3b by the applied electric field,
It does not adhere to the negative electrode 3b and gathers near the electrode. Then, these metal ions are mixed into the alkaline ionized water, and are extracted from the alkaline water discharge port 6b through a common alkaline water discharge pipe 10.

【0009】ところで半導体装置においては、微量の金
属イオンの付着によって大きく電気的特性が影響を受け
るため、電解イオン水に含まれる金属イオンを取り除く
ことが必要である。
In a semiconductor device, since the electrical characteristics are greatly affected by the adhesion of a small amount of metal ions, it is necessary to remove metal ions contained in electrolytic ionized water.

【0010】これらの陰電極周辺の高濃度の金属陽イオ
ンを除去するためには、陽電極、陰電極間に逆電圧を印
加すれば良い。これにより、陰電極周辺の金属陽イオン
は容易に除去される。しかしながら、この場合には、次
のような不都合が生ずる。すなわち、電解電圧と同程度
ないしそれ以上の逆電圧を印加した場合には、本来の陽
電極が陰電極として作用し、本来の陽電極周辺に金属イ
オンが集まってしまう。また、本来の陰電極が陽電極と
して作用し、新たに金属イオンを溶出してしまう。この
結果、かえって、電解イオン水中の金属イオン濃度を増
加させてしまう。本発明は上記の問題に鑑みなされたも
ので、金属イオンを除去した高純度の電解イオン水を長
時間生成供給することを目的とする。
In order to remove the high concentration of metal cations around the negative electrode, a reverse voltage may be applied between the positive electrode and the negative electrode. Thereby, metal cations around the negative electrode are easily removed. However, in this case, the following inconvenience occurs. That is, when a reverse voltage equal to or higher than the electrolytic voltage is applied, the original positive electrode acts as a negative electrode, and metal ions gather around the original positive electrode. In addition, the original negative electrode acts as a positive electrode, and newly elutes metal ions. As a result, the metal ion concentration in the electrolytic ionic water is rather increased. The present invention has been made in view of the above problems, and has as its object to produce and supply high-purity electrolytic ionized water from which metal ions have been removed for a long time.

【0011】[0011]

【課題を解決するための手段】上記の問題を解決するた
め、本発明にかかる電解イオン水生成方法では、電解槽
を隔膜によって区分することで形成された陽極室と陰極
室にそれぞれ原水供給口を通して原水を充填し、前記陽
極室に挿入された陽電極と前記陰極室に挿入された陰電
極との間に電解電圧を印加し、前記陽極室に充填された
原水を酸性水に、且つ、前記陰極室に充填された原水を
アルカリ性水にそれぞれ電解分離し、前記酸性水を前記
陽極室に接続された酸性水取り出し口から取り出し、前
記アルカリ性水を前記陰極室に接続されたアルカリ性水
取り出し口から取り出してなる電解イオン水生成方法に
おいて、一定時間の前記酸性水、前記アルカリ性水の取
り出し後に、前記陽電極、前記陰電極間に前記電解電圧
以下の逆電圧をパルス状に印加して電解イオン水に含ま
れる金属イオンを除去することを特徴とする。
In order to solve the above problems, in the method for producing electrolytic ionic water according to the present invention, a raw water supply port is provided in an anode chamber and a cathode chamber formed by dividing an electrolytic cell by a diaphragm. Through which raw water is filled, an electrolytic voltage is applied between the positive electrode inserted into the anode chamber and the negative electrode inserted into the cathode chamber, and the raw water filled into the anode chamber is converted into acidic water, and The raw water filled in the cathode compartment is electrolytically separated into alkaline water, respectively, and the acidic water is taken out from an acid water take-out port connected to the anode compartment, and the alkaline water is taken out from an alkaline water take-out port connected to the cathode compartment. In the method for producing electrolytic ionic water taken out from the above, after taking out the acidic water and the alkaline water for a certain time, a reverse voltage equal to or lower than the electrolytic voltage is applied between the positive electrode and the negative electrode. It is applied to the scan form and removing the metal ions contained in the electrolytic ion water.

【0012】また、逆電圧の印加時間に連動して、前記
アルカリ性水の取り出し口を前記アルカリ性水取り出し
口から、排出口に切り替えることを特徴とする。
[0012] Further, in accordance with the application time of the reverse voltage, the outlet of the alkaline water is switched from the outlet of the alkaline water to the outlet.

【0013】[0013]

【発明の実施の形態】以下に、本発明の実施の形態を、
図面を用いて詳細に説明する。本発明の実施の形態で
は、図2に示した電解イオン水生成装置を用いる。図2
(A)は、電解イオン水生成装置の要部の概略を示し、
同図(B)は生成装置ユニットを示す。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below.
This will be described in detail with reference to the drawings. In the embodiment of the present invention, the electrolytic ionized water generator shown in FIG. 2 is used. FIG.
(A) shows an outline of a main part of an electrolytic ionized water generator,
FIG. 2B shows a generator unit.

【0014】図2(A)に示すように、電解イオン水生
成装置は、5個の生成装置ユニット100からなり、各
ユニット100は、図2(B)に示すように、イオン交
換隔膜2によって陽極室1aと陰極室1bに分割された
電解槽1を有している。前記陽極室1a内には白金から
なる陽電極3a、陰電極1b内にはチタンからなる陰電
極3bがそれぞれ挿入され、電解電源4から電解電流の
通電が行われるようになっている。前記電解槽1には陽
極室1aに通じる原水供給口5a、陰極室1bに通じる
原水供給口5bがそれぞれ設けられ、また反対側には酸
性水を吐出する吐水口6a及び陽極室の排水口7a、ア
ルカリ性水を吐出する吐水口6b及び陰極室の排水口7
bがそれぞれ設けられている。そして図2(A)に示す
ように、各ユニット100の原水供給口5a、5bは原
水供給管8、酸性水の吐水口6aは共通の吐水管9、ア
ルカリ性水の吐水口6bは共通の吐水管10、陽極室の
排水口7aは共通の排水管11、陰極室の排水口7bは
共通の排水管12にそれぞれ連結されている。なお、1
3、14、15、16、17、18は、何れもバルブで
ある。
As shown in FIG. 2A, the electrolyzed ionic water generator comprises five generator units 100. Each unit 100 has an ion exchange membrane 2 as shown in FIG. 2B. It has an electrolytic cell 1 divided into an anode chamber 1a and a cathode chamber 1b. A positive electrode 3a made of platinum is inserted in the anode chamber 1a, and a negative electrode 3b made of titanium is inserted in the negative electrode 1b, so that an electrolytic current flows from an electrolytic power supply 4. The electrolytic cell 1 is provided with a raw water supply port 5a communicating with the anode chamber 1a and a raw water supply port 5b communicating with the cathode chamber 1b. On the other side, a water discharge port 6a for discharging acidic water and a drain port 7a for the anode chamber are provided. , An outlet 6b for discharging alkaline water, and a drain 7 for the cathode chamber
b are provided respectively. Then, as shown in FIG. 2A, the raw water supply ports 5a and 5b of each unit 100 are the raw water supply pipe 8, the acidic water discharge port 6a is a common discharge pipe 9, and the alkaline water discharge port 6b is a common discharge port. The water pipe 10 and the drain port 7a of the anode chamber are connected to a common drain pipe 11, and the drain port 7b of the cathode chamber is connected to a common drain pipe 12. In addition, 1
3, 14, 15, 16, 17, and 18 are all valves.

【0015】次に、この電解イオン水生成装置を用いて
電解イオン水を生成する方法を説明する。まず、原水供
給管8に原水として高純度の純水を供給し、原水供給口
5aより陽極室1a、原水供給口5bより陰極室1b内
に純水を供給した後、陽電極3aと陰電極3bに通電
し、純水を電気分解することによって陽極室1aに酸性
水、陰極室1bにアルカリ性水を電解生成する。そして
各ユニット100で生成した酸性水を吐水口6aより共
通の酸性水の吐水管9、アルカリ性水を吐水口6bより
共通のアルカリ性水の吐水管10にそれぞれ取り出す。
Next, a method for producing electrolytic ionic water using the electrolytic ionic water producing apparatus will be described. First, high-purity pure water is supplied to the raw water supply pipe 8 as raw water, pure water is supplied from the raw water supply port 5a into the anode chamber 1a, and from the raw water supply port 5b into the cathode chamber 1b, and then the positive electrode 3a and the negative electrode are supplied. 3b, electricity is generated, and pure water is electrolyzed to electrolyze acidic water in the anode chamber 1a and alkaline water in the cathode chamber 1b. Then, the acidic water generated in each unit 100 is taken out from a common water discharge pipe 9 from the water discharge port 6a, and the alkaline water is taken out to a common alkaline water discharge pipe 10 from the water discharge port 6b.

【0016】また、電解イオン水を長時間連続して生成
すると、陽極室、陰極室から、電極材料である白金、
鉄、クロム等の金属イオンがイオン水中に溶解し、イオ
ン水を汚染する。そのため、電極周辺の金属イオンを遊
離し、除去を行う必要がある。
When the electrolytic ionic water is continuously generated for a long time, platinum, which is an electrode material, is removed from the anode chamber and the cathode chamber.
Metal ions such as iron and chromium dissolve in the ionic water and contaminate the ionic water. Therefore, it is necessary to release and remove metal ions around the electrodes.

【0017】以下に、図1を用いて、金属イオンを除去
する方法を説明する。図1は、本発明の実施の形態にか
かる電解水生成時における、電解電圧と、バルブ操作の
関係を示したものである。
Hereinafter, a method of removing metal ions will be described with reference to FIG. FIG. 1 shows a relationship between an electrolysis voltage and a valve operation during generation of electrolyzed water according to the embodiment of the present invention.

【0018】図1では、横軸に経過時間を取って有る。
また、縦軸には図2に示した生成装置での陽電極3a、
陰電極3b間に印加する印加電圧が取って有る。また、
印加電圧の変化に合わせて、図2に示したバルブ15、
16、17、18の開閉状態を示している。
In FIG. 1, the elapsed time is shown on the horizontal axis.
The vertical axis represents the positive electrode 3a in the generator shown in FIG.
An applied voltage is applied between the negative electrodes 3b. Also,
The valve 15 shown in FIG.
The open / closed state of 16, 17, 18 is shown.

【0019】以下に図1の内容を時間に沿って説明す
る。電解電圧20Vで一定時間電解を行った後、金属イ
オンが増加し始める時点で、図2(A)の電源4の極性
を反転し、−10Vのパルス逆電圧を加える。ここで、
パルス周波数は0.25(Hz)とし、逆電圧印加時間
は1分間でよい。このパルス電圧印加時間中、電解水生
成時には開いている酸性水吐出口バルブ15、アルカリ
性水吐出口バルブ16を閉じ、電解水生成時には閉じて
いる陽極室排水口バルブ17、陰極室排水口バルブ18
を開く。これにより、パルス電圧印加中の金属イオン濃
度の増加したイオン水を排出する。この操作を約1分間
続けた後、再度、図2(A)の電源4の極性を反転し、
印加電圧を20Vにあげ、同時に酸性水吐出口バルブ1
5、アルカリ性水吐出口バルブ16を開き、陽極室排水
口バルブ17、陰極室排水口バルブ18を閉じる。これ
によって再度イオン水を供給する事ができる。
The contents of FIG. 1 will be described below in time. After performing electrolysis at an electrolysis voltage of 20 V for a certain period of time, at the time when the number of metal ions starts to increase, the polarity of the power supply 4 in FIG. here,
The pulse frequency may be 0.25 (Hz) and the reverse voltage application time may be one minute. During the application of the pulse voltage, the acidic water discharge valve 15 and the alkaline water discharge valve 16 which are open when the electrolytic water is generated are closed, and the anode chamber drain valve 17 and the cathode chamber discharge valve 18 which are closed when the electrolytic water is generated.
open. As a result, ion water having an increased metal ion concentration during application of the pulse voltage is discharged. After this operation is continued for about 1 minute, the polarity of the power supply 4 shown in FIG.
Increase the applied voltage to 20V, and at the same time
5. The alkaline water discharge valve 16 is opened, and the anode chamber drain valve 17 and the cathode chamber drain valve 18 are closed. Thereby, ion water can be supplied again.

【0020】尚、上記のように、金属陽イオンは陰電極
周辺に主として集まっているので、陽電極周辺のイオン
による汚染が少ないときには、パルス電圧印加中にアル
カリ性水のみを排出し、酸性水は通常通り使用する事も
できる。
As described above, since metal cations are mainly collected around the negative electrode, when there is little contamination by ions around the positive electrode, only alkaline water is discharged during pulse voltage application, and acidic water is discharged. Can be used as usual.

【0021】上述のパルス電圧印加中の陽極室1a、陰
極室1b内に残存する鉄イオンの相対的な濃度(残存
率)変化の様子を図3に示す。ここに示したように、パ
ルス電圧印加直後に残存鉄イオンは急激に減少し、排水
中には高濃度の鉄イオン排水が排出される。以後、残存
鉄イオン濃度は緩やかに減少し、約40秒で安定する。
実際にパルス電圧印加前には500(ppt)程度であ
った排水中の鉄イオン濃度は、1分間パルス電圧印加し
た後では、10(ppt)以下にまで減少していた。
FIG. 3 shows how the relative concentration (residual rate) of iron ions remaining in the anode chamber 1a and the cathode chamber 1b during the application of the pulse voltage changes. As shown here, immediately after the application of the pulse voltage, the residual iron ions rapidly decrease, and high-concentration iron ion wastewater is discharged into the wastewater. Thereafter, the residual iron ion concentration gradually decreases and stabilizes in about 40 seconds.
Actually, the iron ion concentration in the waste water, which was about 500 (ppt) before the pulse voltage was applied, was reduced to 10 (ppt) or less after the pulse voltage was applied for 1 minute.

【0022】以後、この操作を繰り返す事により、長期
間安定して高純度のイオン水を供給する事ができる。上
記の実施の形態では濃度変化の様子を鉄イオンを例に取
って述べたが、本発明の適用はこれに限られるものでは
なく、白金、クロム等、全ての金属不純物に同様に適用
する事ができる。
Thereafter, by repeating this operation, high-purity ion water can be supplied stably for a long period of time. In the above-described embodiment, the state of the concentration change has been described by taking iron ions as an example. However, the application of the present invention is not limited to this, and the same applies to all metal impurities such as platinum and chromium. Can be.

【0023】また、上記の実施の形態では、10V、
0.25(Hz)のパルス逆電圧を1分間印加する例を
示したが、パルス電圧、パルス間隔、パルス印加時間と
もにこれに限る事はなく、イオン水生成装置の形状、生
成条件に応じて設定すればよい。また、上記の実施の形
態では、電解電圧は20Vとしたが、これに限らないこ
とは言うまでもない。
Further, in the above embodiment, 10 V,
Although an example in which a pulse reverse voltage of 0.25 (Hz) is applied for one minute has been described, the pulse voltage, pulse interval, and pulse application time are not limited to these, but may be determined according to the shape of the ion water generator and the generation conditions. Just set it. In the above embodiment, the electrolysis voltage is set to 20 V, but it is needless to say that the present invention is not limited to this.

【0024】[0024]

【発明の効果】本発明を用いる事により、金属イオン濃
度の低い電解イオン水を安定して生成する事ができる。
According to the present invention, electrolytic ion water having a low metal ion concentration can be produced stably.

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

【図1】本発明の実施の形態にかかる電解イオン水生成
方法における、電解電圧、バルブ開閉の対応を示してい
る。
FIG. 1 shows correspondence between an electrolytic voltage and a valve opening / closing in a method for producing electrolytic ionic water according to an embodiment of the present invention.

【図2】本発明の実施の形態にかかる電解イオン水生成
に用いる電解イオン水生成装置を示している。
FIG. 2 shows an electrolytic ionic water generator used for electrolytic ionic water generation according to an embodiment of the present invention.

【図3】パルス電圧印加中の陽極室1a内、陰極室1b
内に残存する鉄イオンの相対的な濃度(残存率)変化の
様子を示している。
FIG. 3 shows the inside of the anode chamber 1a and the cathode chamber 1b during application of a pulse voltage.
3 shows how the relative concentration (residual rate) of iron ions remaining in the inside changes.

【符号の説明】[Explanation of symbols]

1・・・・電解槽 1a・・・陽極室 1b・・・陰極室 2・・・・隔膜 3a・・・陽電極 3b・・・陰電極 4・・・・電解電源 5a、5b・・・原水供給口 6a・・・酸性水吐出口 6b・・・アルカリ性水吐出口 7a・・・陽極室排水口 7b・・・陰極室排水口 8・・・・原水供給管 9・・・・酸性水共通吐水管 10・・・アルカリ性水共通吐水管 11・・・陽極室排水共通排水管 12・・・陰極室排水共通排水管 15・・・酸性水吐出口バルブ 16・・・アルカリ性水吐出口バルブ 17・・・陽極水排水口バルブ 18・・・陰極水排水口バルブ 100・・生成ユニット 1 ... Electrolyzer 1a ... Anode chamber 1b ... Cathode chamber 2 ... Diaphragm 3a ... Positive electrode 3b ... Negative electrode 4 ... Electrolysis power supply 5a, 5b ... Raw water supply port 6a ・ ・ ・ Acid water discharge port 6b ・ ・ ・ Alkaline water discharge port 7a ・ ・ ・ Anode chamber drain port 7b ・ ・ ・ Cathode chamber drain port 8 ・ ・ ・ ・ Raw water supply pipe 9 ・ ・ ・ ・ Acid water Common discharge pipe 10 ・ ・ ・ Alkaline water common discharge pipe 11 ・ ・ ・ Anode chamber drain common drain pipe 12 ・ ・ ・ Cathode chamber drain common drain pipe 15 ・ ・ ・ Acid water discharge valve 16 ・ ・ ・ Alkaline water discharge valve 17 ・ ・ ・ Anode water drain valve 18 ・ ・ ・ Cathode water drain valve 100 ・ ・ Generation unit

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】電解槽を隔膜によって区分することで形成
された陽極室と陰極室にそれぞれ原水供給口を通して原
水を充填し、前記陽極室に挿入された陽電極と前記陰極
室に挿入された陰電極との間に電解電圧を印加し、前記
陽極室に充填された原水を酸性水に、且つ、前記陰極室
に充填された原水をアルカリ性水にそれぞれ電解分離
し、前記酸性水を前記陽極室に接続された酸性水取り出
し口から取り出し、前記アルカリ性水を前記陰極室に接
続されたアルカリ性水取り出し口から取り出してなる電
解イオン水生成方法において、一定時間の前記酸性水、
前記アルカリ性水の取り出し後に、前記陽電極、前記陰
電極間に前記電解電圧以下の逆電圧をパルス状に印加し
て電解イオン水に含まれる金属イオンを除去することを
特徴とする電解イオン水生成方法。
1. An anode chamber and a cathode chamber formed by dividing an electrolytic cell by a diaphragm are each filled with raw water through a raw water supply port, and are inserted into the anode chamber and the cathode chamber. An electrolytic voltage is applied between the negative electrode and the raw water filled in the anode chamber into acidic water, and the raw water filled in the cathode chamber is electrolytically separated into alkaline water. Taking out from the acidic water outlet connected to the chamber, the alkaline water is taken out from the alkaline water outlet connected to the cathode chamber, in the electrolytic ionic water generation method, the acidic water for a certain time,
After taking out the alkaline water, a reverse voltage less than the electrolytic voltage is applied in a pulsed manner between the positive electrode and the negative electrode to remove metal ions contained in the electrolytic ionic water. Method.
【請求項2】前記逆電圧の印加時間に連動して、前記ア
ルカリ性水の取り出し口を前記アルカリ性水取り出し口
から、排出口に切り替えることを特徴とする請求項1に
記載の電解イオン水生成方法。
2. The method according to claim 1, wherein the outlet of the alkaline water is switched from the outlet of the alkaline water to the outlet in conjunction with the application time of the reverse voltage. .
JP24945996A 1996-09-20 1996-09-20 Electrolytic ionic water preparation process Pending JPH1085746A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24945996A JPH1085746A (en) 1996-09-20 1996-09-20 Electrolytic ionic water preparation process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24945996A JPH1085746A (en) 1996-09-20 1996-09-20 Electrolytic ionic water preparation process

Publications (1)

Publication Number Publication Date
JPH1085746A true JPH1085746A (en) 1998-04-07

Family

ID=17193281

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24945996A Pending JPH1085746A (en) 1996-09-20 1996-09-20 Electrolytic ionic water preparation process

Country Status (1)

Country Link
JP (1) JPH1085746A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007501702A (en) * 2003-08-08 2007-02-01 パイオネティックス, インコーポレイテッド Selectable ion concentration with electrolytic ion exchange
JP2012006011A (en) * 2008-08-29 2012-01-12 Yoji Hayakawa Aqueous environmental battery
US9090493B2 (en) 2005-10-06 2015-07-28 Pionetics Corporation Electrochemical ion exchange treatment of fluids
US9757695B2 (en) 2015-01-03 2017-09-12 Pionetics Corporation Anti-scale electrochemical apparatus with water-splitting ion exchange membrane

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007501702A (en) * 2003-08-08 2007-02-01 パイオネティックス, インコーポレイテッド Selectable ion concentration with electrolytic ion exchange
US9090493B2 (en) 2005-10-06 2015-07-28 Pionetics Corporation Electrochemical ion exchange treatment of fluids
JP2012006011A (en) * 2008-08-29 2012-01-12 Yoji Hayakawa Aqueous environmental battery
US9757695B2 (en) 2015-01-03 2017-09-12 Pionetics Corporation Anti-scale electrochemical apparatus with water-splitting ion exchange membrane

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