JPS6075337A - Regeneration method of ion exchange resin - Google Patents

Regeneration method of ion exchange resin

Info

Publication number
JPS6075337A
JPS6075337A JP58184284A JP18428483A JPS6075337A JP S6075337 A JPS6075337 A JP S6075337A JP 58184284 A JP58184284 A JP 58184284A JP 18428483 A JP18428483 A JP 18428483A JP S6075337 A JPS6075337 A JP S6075337A
Authority
JP
Japan
Prior art keywords
exchange resin
ion
resin
ion exchange
chamber
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
JP58184284A
Other languages
Japanese (ja)
Inventor
Masao Ogino
正夫 荻野
Shinji Komoguchi
菰口 伸二
Moriyuki Sakai
守幸 坂井
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.)
Sharp Corp
Original Assignee
Sharp 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 Sharp Corp filed Critical Sharp Corp
Priority to JP58184284A priority Critical patent/JPS6075337A/en
Publication of JPS6075337A publication Critical patent/JPS6075337A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To regenerate ion exchange resin readily without using acid or alkali by impressing an electric voltage directly to the ion exchange resin in the water and to remove ions caught by the resin from the resin by the electric attractive force. CONSTITUTION:A vessel 1 is partitioned by an ion-permeative porous membrane 2 to form an anode chamber 7 and a cathode chamber 8 therein, and charging cation exchange resin 5 and anion exchange resin 6 requiring regeneration in respective chambers. Water is filled in both electrode chambers 7, 8 and electric current is fed to the anode plate 3 and a cathode plate 4. Cations (except H ion) such as Na ions captured by the cation exchange resin 5 migrate toward the cathode chamber 8 through a diaphragm 2; on one hand, anions (except OH ion) such as Cl ions captured by the anion exchange resin 6 migrate toward the anode chamber 7 through the diaphragm 2.

Description

【発明の詳細な説明】 く技術分野〉 本発明は、イオン交換樹脂の再生に関するものである。[Detailed description of the invention] Technical fields> The present invention relates to the regeneration of ion exchange resins.

〈従来技術〉 イオン交換樹脂は、母体となる高分子にイオン交換性を
もつ官能基をつげたものであり、水処理、糖・薬品、溶
媒の精製等に利用されている。しかしながら、イオン交
換樹脂の最大の欠点は、イオン交換後の樹脂の再生に、
酸またはアルカリを要し、特に交換基としてスルホン酸
基をもつ強酸性陽イオン交換樹脂、4級アンモニウム基
をもつ強塩基性陰イオン交換樹脂は、再生効率が悪く、
再生には人情の酸、アルカリが必要であるという点であ
り、再生に多大な労力を要するのか現状である。
<Prior Art> Ion exchange resins are made by adding functional groups with ion exchange properties to a polymer base, and are used for water treatment, purification of sugars, drugs, solvents, etc. However, the biggest drawback of ion exchange resins is the regeneration of the resin after ion exchange.
Strongly acidic cation exchange resins that require acid or alkali and have sulfonic acid groups as exchange groups, and strongly basic anion exchange resins that have quaternary ammonium groups have poor regeneration efficiency.
The point is that human acids and alkalis are required for regeneration, and the current situation is that regeneration requires a great deal of effort.

〈発明の目的〉 本発明は、上記の問題に鑑みてなされたものてあり、樹
脂の再生に酸、アルカリを使用することなく、1m単に
再生することを1」的とする。
<Object of the Invention> The present invention has been made in view of the above problems, and its objective is to simply regenerate 1 meter of resin without using acid or alkali.

〈発明の概要〉 この目的は本発明によれば、水中でイオン交換樹脂に直
流電圧を印加し、樹脂によって捕捉されたイオンを電気
的引力によって樹脂から取り除くことによって達成され
る。
SUMMARY OF THE INVENTION This object is achieved according to the invention by applying a DC voltage to the ion exchange resin in water and removing the ions captured by the resin from the resin by means of electrical attraction.

〈実施例〉 以下、本発明の詳細につき図に基づいて説明する。<Example> Hereinafter, details of the present invention will be explained based on the drawings.

第1図、第2図、第3図は、本発明の実施例を示すもの
であり、図中1は容器、2は素焼、セロファン等のイオ
ン透過性多孔質膜、3は陽極板、4は陰極板、5は陽イ
オン交換樹脂、6は陰イオン交換樹脂、7は陽極室、8
は陰極室、9は腸イオン交換樹脂もしくは陰イオン交換
樹脂または陽イオン交換樹脂と陰イオン交換樹脂の混合
物を示す。
1, 2, and 3 show embodiments of the present invention, in which 1 is a container, 2 is an ion-permeable porous membrane such as bisque or cellophane, 3 is an anode plate, and 4 is an anode plate. is a cathode plate, 5 is a cation exchange resin, 6 is an anion exchange resin, 7 is an anode chamber, 8
indicates a cathode chamber, and 9 indicates an intestinal ion exchange resin, an anion exchange resin, or a mixture of a cation exchange resin and an anion exchange resin.

第1図では再生を要する陽イオン交換樹脂5と陰イオン
交換樹脂6が隔膜2によって区切られ、それぞれ陽極室
7と陰極室8に入っている。両極室に水を満たし通電す
ると、電気的引力により、陽イオン交換樹脂5が捕捉し
たすトリウムイオン等の陽イオン(水素イオンは除く)
は隔膜2を経て陰極室8へ移動する。一方、陰イオン交
換樹脂6が捕捉した塩化物イオン等の陰イオン(水酸化
物イオンは除く)は隔膜2を経て、陽極室7へ移動する
。ある時間が経過すると、陽極室7には、水素イオン以
外の陽イオンはほとんど存在せず、陰極室8にもまた水
酸化物イオン以外の陰イオンかはとんと存在しなくなり
、陽イオン交換樹脂5゜陰イオン交換樹脂6は再生され
、それぞれNa形、C1形の塩形から、交換能力をもつ
H形OH形となる。第2図においても同様な過程により
、それぞれ再生される。
In FIG. 1, a cation exchange resin 5 and an anion exchange resin 6 that require regeneration are separated by a diaphragm 2 and placed in an anode chamber 7 and a cathode chamber 8, respectively. When the bipolar chamber is filled with water and energized, cations such as thorium ions (excluding hydrogen ions) captured by the cation exchange resin 5 due to electrical attraction.
moves through the diaphragm 2 to the cathode chamber 8. On the other hand, anions such as chloride ions (excluding hydroxide ions) captured by the anion exchange resin 6 move to the anode chamber 7 via the diaphragm 2 . After a certain period of time, almost no cations other than hydrogen ions exist in the anode chamber 7, and very few anions other than hydroxide ions exist in the cathode chamber 8, and the cation exchange resin 5 The anion exchange resin 6 is regenerated and changes from the salt form of Na type and C1 type to H type and OH type having exchange ability. In FIG. 2, the respective signals are reproduced through a similar process.

実際にはイオン交換樹脂を一種類たけ単独で用いる場合
や、混床式のように陽イオン交換樹脂と陰イオン交換樹
脂を混合して水処理に用いる場合も多く、その場合は、
第3図に示す様な方法により5再生する。混床式のイオ
ン交換樹脂の再生を例にとると、陽イオン交換樹脂と陰
イオン交換樹脂の混合物9が一対の隔膜2,2によって
区切られた中間室に入っている。それら一対の隔膜2,
2の両側に陽極3.陰極4を置き、水を満たし通電する
と、混合物9中の陽イオン交換樹脂に捕捉されたナトリ
ウム等の陽イオン(水素イオンは除く)は、電気的引力
により隔膜2を経て陰極室8へ移動し、また陰イオン交
換樹脂に捕捉された塩化物イオン等の陰イオン(水酸化
物イオンは除く)は隔膜2を経て陽極室7へ移動する。
In reality, there are many cases where one type of ion exchange resin is used alone, or a mixture of cation exchange resin and anion exchange resin is used for water treatment, such as in a mixed bed system.
The data is reproduced 5 times by the method shown in FIG. Taking mixed bed type ion exchange resin regeneration as an example, a mixture 9 of a cation exchange resin and an anion exchange resin is placed in an intermediate chamber separated by a pair of diaphragms 2, 2. The pair of diaphragms 2,
Anodes on both sides of 2.3. When the cathode 4 is placed, filled with water, and energized, cations such as sodium (excluding hydrogen ions) captured by the cation exchange resin in the mixture 9 move to the cathode chamber 8 via the diaphragm 2 due to electrical attraction. Also, anions such as chloride ions (excluding hydroxide ions) captured by the anion exchange resin move to the anode chamber 7 via the diaphragm 2 .

その結果、混合物9が入っている中間室にはイオン種は
ほとんど存在じよくなり、イオン交換樹脂は再生される
As a result, almost no ionic species exist in the intermediate chamber containing the mixture 9, and the ion exchange resin is regenerated.

以下に具体例を示すが、本発明はこれに限定されるもの
ではない。
Specific examples are shown below, but the present invention is not limited thereto.

(具体例) N a形強酸性陽イオン交換樹脂(ダイヤイオン5K−
1,B )10d、C1形強塩基性陰イオン交換樹脂(
ダイヤイオンSA−10A)20m7!を用いて、第1
図の方法で11生した。通電量と再生樹脂の交4に容量
の関係は第4図のようになり、通電量の増大に伴い交換
容量が増加しており、電気的再生か可能である。
(Specific example) Na type strongly acidic cation exchange resin (Diaion 5K-
1,B) 10d, C1 type strongly basic anion exchange resin (
Diaion SA-10A) 20m7! using the first
I made it to 11th grade using the method shown in the figure. The relationship between the amount of energization and the capacity of the recycled resin is as shown in FIG. 4, and as the amount of energization increases, the exchange capacity increases, and electrical regeneration is possible.

く効果〉 以上詳細に説明したように、本発明の方法を用いるとイ
オン交換樹脂の再生に酸・アルカリを用いることなく通
電するだけて簡単に再生することができ、イオン交換樹
脂のくり返し使用が容易になり、脱塩再生の自動化にも
非常に有利である。
Effect> As explained in detail above, by using the method of the present invention, ion exchange resin can be easily regenerated by simply applying electricity without using acids or alkalis, and the ion exchange resin can be used repeatedly. This makes it easy to use and is very advantageous for automating desalination and regeneration.

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

第1図乃至第3図は、それぞれ本発明の実施例を示す図
である。第4図は、Na形強酸性陽イオン交換樹脂、C
I!形強塩基性陰イオン交換樹脂を用いて第1図の方法
で再生した場合に於ける、通電量と再生樹脂の交換容量
との関係を示す図である。 符号の説明 1:容器、2:イオン透過性多孔質膜(1召膜)、3:
陽極板、4:陰極板、5:陽イオン交換樹脂、または陽
イオン交換樹脂と陰イオン交換樹脂の混合物。 代理人 弁理士 福 士 愛 彦(他2名)第4図
1 to 3 are diagrams each showing an embodiment of the present invention. Figure 4 shows Na-type strongly acidic cation exchange resin, C
I! FIG. 2 is a diagram showing the relationship between the amount of electricity applied and the exchange capacity of the regenerated resin in the case of regeneration using the method of FIG. 1 using a strongly basic anion exchange resin. Explanation of symbols 1: Container, 2: Ion-permeable porous membrane (1 membrane), 3:
Anode plate, 4: Cathode plate, 5: Cation exchange resin, or a mixture of cation exchange resin and anion exchange resin. Agent Patent attorney Aihiko Fuku (and 2 others) Figure 4

Claims (4)

【特許請求の範囲】[Claims] (1) イオン交換樹脂の両側に電極を置き、水中で直
流電圧を印加することにより再生することを特徴とする
、イオン交換樹脂の再生方法。
(1) A method for regenerating an ion exchange resin, which comprises placing electrodes on both sides of the ion exchange resin and regenerating it by applying a DC voltage in water.
(2)陽イオン交換樹脂と陰イオン交換樹脂をイオン透
過性の多孔質1箱膜を隔てて置き、それらの樹脂の両側
から電圧を印加することを特徴とする特許請求の範囲第
[1+項記載のイオン交換樹脂の再生方法。
(2) A cation-exchange resin and an anion-exchange resin are separated by an ion-permeable porous one-box membrane, and a voltage is applied from both sides of the resins. Method for regenerating the described ion exchange resin.
(3)陽イオン交換樹脂と陰イオン交換樹脂をイオン透
過性の多孔質隔膜を隔てて置き、さらにそれら樹脂の両
側に上記隔膜を隔てて両電極を置き電圧を印加すること
を特徴とする特許請求の範囲第(1)項記載のイオン交
換樹脂の再生方法。
(3) A patent characterized in that a cation exchange resin and an anion exchange resin are separated by an ion-permeable porous membrane, and further, both electrodes are placed on both sides of these resins with the membrane separated, and a voltage is applied. A method for regenerating an ion exchange resin according to claim (1).
(4)陽イオン交換樹脂もしくは陰イオン交換樹脂また
は両交換樹脂の混合物の両側にイオン透過性の多孔質隔
膜を置き、その両側の電極より電圧を印加することを特
徴とする特許請求の範囲第(+]項記載のイオン交換樹
脂の再生方法。
(4) An ion-permeable porous diaphragm is placed on both sides of a cation exchange resin, an anion exchange resin, or a mixture of both exchange resins, and voltage is applied from electrodes on both sides of the membrane. A method for regenerating an ion exchange resin as described in (+).
JP58184284A 1983-09-30 1983-09-30 Regeneration method of ion exchange resin Pending JPS6075337A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58184284A JPS6075337A (en) 1983-09-30 1983-09-30 Regeneration method of ion exchange resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58184284A JPS6075337A (en) 1983-09-30 1983-09-30 Regeneration method of ion exchange resin

Publications (1)

Publication Number Publication Date
JPS6075337A true JPS6075337A (en) 1985-04-27

Family

ID=16150625

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58184284A Pending JPS6075337A (en) 1983-09-30 1983-09-30 Regeneration method of ion exchange resin

Country Status (1)

Country Link
JP (1) JPS6075337A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8133380B2 (en) 2001-11-29 2012-03-13 Ebara Corporation Method for regenerating ion exchanger

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8133380B2 (en) 2001-11-29 2012-03-13 Ebara Corporation Method for regenerating ion exchanger

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