JPS61254292A - Method for making pure water - Google Patents

Method for making pure water

Info

Publication number
JPS61254292A
JPS61254292A JP60094121A JP9412185A JPS61254292A JP S61254292 A JPS61254292 A JP S61254292A JP 60094121 A JP60094121 A JP 60094121A JP 9412185 A JP9412185 A JP 9412185A JP S61254292 A JPS61254292 A JP S61254292A
Authority
JP
Japan
Prior art keywords
water
ion exchange
raw water
pure water
exchange resin
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.)
Granted
Application number
JP60094121A
Other languages
Japanese (ja)
Other versions
JPH0142753B2 (en
Inventor
Masabumi Imaizumi
今泉 正文
Takahito Motomura
敬人 本村
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries Ltd
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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP60094121A priority Critical patent/JPS61254292A/en
Publication of JPS61254292A publication Critical patent/JPS61254292A/en
Publication of JPH0142753B2 publication Critical patent/JPH0142753B2/ja
Granted legal-status Critical Current

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  • Treatment Of Water By Ion Exchange (AREA)

Abstract

PURPOSE:To stably obtain high purity water while preventing the oxidative deterioration of an ion exchange resin, by adding a nitrogen compound to raw water. CONSTITUTION:In performing the ion exchange of raw water containing residual chlorine by an ion exchange resin, a nitrogen compound such as hydrazine is added to raw water as a reducing agent in an amount of 1.3-2.0 equivalent on the basis of residual chlorine in raw water. By this method, high purity water can be obtained and the stable preserving period thereof can be prolonged.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、純水製造方法に係り、特にイオン交換m脂を
用いて純水を製造するにあたり、イオン交換樹脂の酸化
劣化を防止して、高純度の純水を安定して製造すること
ができる純水製造方法に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for producing pure water, and in particular, a method for preventing oxidative deterioration of an ion exchange resin when producing pure water using an ion exchange resin. , relates to a method for producing pure water that can stably produce highly purified water.

[従来の技術] あるいは超純水を製造する場合、水道水中には塩素が残
留しているため、この残留塩素によりイオン交換樹脂が
酸化されて劣化し1時間の経過と共に処理水水質が低下
するという問題がある。
[Prior art] Alternatively, when producing ultrapure water, chlorine remains in tap water, and this residual chlorine oxidizes and degrades the ion exchange resin, causing the quality of the treated water to deteriorate over the course of an hour. There is a problem.

このため、従来、イオン交換樹脂を用いて純水あるいは
超純水を製造するシステムゆおいては、原水中の残留塩
素を還元剤により還元しイオン交換樹脂の酸化劣化を防
止している。しかして、この還元剤としてはNa2SO
3、NaH3O3゜Na2S205 、に25205等
の硫黄化合物系の還元剤が用いられている。
For this reason, in conventional systems for producing pure water or ultrapure water using ion exchange resins, residual chlorine in raw water is reduced with a reducing agent to prevent oxidative deterioration of the ion exchange resins. However, as this reducing agent, Na2SO
3. Sulfur compound-based reducing agents such as 25205 are used for NaH3O3°Na2S205.

[発明が解決しようとする問題点] しかしながら、従来用いられている硫黄化合物系還元剤
は、原水中の残留塩素の当量より過剰に添加した場合に
は、還元剤から生成するS Os、S 02等の硫黄化
合物が、イオン交換されることなく処理水中にリークし
、処理水純度を低下させるという問題があった。しかも
、処理水中にり一りしたこれらの硫黄化合物は、イオン
交換樹脂への吸着量が非常に小さい上、限外濾過(UF
)膜や逆浸透(RO)膜によっても除去することができ
ず、処理水を更にイオン交換あるいは膜分離処理に供し
ても、高純度の純水を得ることはできなかった。
[Problems to be Solved by the Invention] However, when the conventionally used sulfur compound-based reducing agents are added in excess of the equivalent amount of residual chlorine in the raw water, S Os, S 02 generated from the reducing agent There was a problem in that sulfur compounds such as sulfur compounds leaked into the treated water without being ion-exchanged, reducing the purity of the treated water. Moreover, these sulfur compounds concentrated in the treated water have a very small amount of adsorption on ion exchange resins, and ultrafiltration (UF
) membrane or reverse osmosis (RO) membrane, and even if the treated water was further subjected to ion exchange or membrane separation treatment, highly pure water could not be obtained.

[問題点を解決するための手段] 本発明は上記問題点を解決し、高純度の純水を安定して
得ることができる純水製造方法を提供するものであって
、残留塩素を含有する原水をイオン交換樹脂層に通水し
て純水を得る方法において、原水に窒素化合物を添加す
るものである。
[Means for Solving the Problems] The present invention solves the above problems and provides a method for producing pure water that can stably obtain highly purified water, which does not contain residual chlorine. In a method for obtaining pure water by passing raw water through an ion exchange resin layer, a nitrogen compound is added to the raw water.

以下に本発明につき詳細に説明する。The present invention will be explained in detail below.

本発明においては、残留塩素を含有する原水をイオン交
換樹脂でイオン交換するに際し、原水に還元剤として窒
素化合物を添加する。
In the present invention, when raw water containing residual chlorine is ion-exchanged with an ion exchange resin, a nitrogen compound is added to the raw water as a reducing agent.

本発明で、還元剤として用いられる窒素化合物としては
、ヒドラジン(H2H4)が好適であるが、そのほかに
も、NaNO2,KNO2等が挙げられる。これらの窒
素化合物は、特に精製したものを用いることにより、得
られる純水の純度をより高いものとすることができる。
In the present invention, hydrazine (H2H4) is suitable as a nitrogen compound used as a reducing agent, but other examples include NaNO2, KNO2, and the like. By using particularly purified nitrogen compounds, the purity of the obtained pure water can be made higher.

本発明の方法は、残留塩素を含有する原水からイオン交
換法により純水あるいは超純水を製造する全てのシステ
ムに適用可能であるが、このようなシステムとしては、 ■ 原水を濾過した後、イオン交換装置でイオン交換し
純水を製造するシステム、 あるいは、 ■ 原水を濾過した後、RO膜分離装置→混床式イオン
交換装置→紫外線酸化装置→カートリッジ純水器(非再
生型混床式純水器)→UF膜分離装置に順次送給し、超
純水を製造するシステム、 等が挙げられる。特に本発明の方法は、■の如き超純水
製造システムに採用した場合、極めて顕著な効果を奏す
る。
The method of the present invention is applicable to all systems that produce pure water or ultrapure water from raw water containing residual chlorine by an ion exchange method. A system that produces pure water by exchanging ions with an ion exchange device, or ■ After filtering the raw water, RO membrane separation device → mixed bed ion exchange device → ultraviolet oxidation device → cartridge deionizer (non-regenerative mixed bed type) Examples include a system that sequentially supplies ultrapure water (water purifier) to a UF membrane separation device to produce ultrapure water. In particular, when the method of the present invention is adopted in an ultrapure water production system such as (2), it produces extremely remarkable effects.

本発明において、原水への窒素化合物の添加は、原水が
イオン交換樹脂層に供給される以前であれば良いが、特
にその直前とするのが、他の装置への影響がないことか
ら好ましい。
In the present invention, the nitrogen compound may be added to the raw water as long as it is before the raw water is supplied to the ion exchange resin layer, but it is particularly preferable to add the nitrogen compound immediately before the raw water is supplied to the ion exchange resin layer, since this does not affect other equipment.

窒素化合物の添加量は原水中の残留塩素の当量よりも少
し過剰になるようにするのが好適であり、特に原水中の
残留塩素の1.3〜2.0当量とするのが好ましい、な
お、本発明においては、従来の硫黄系化合物を還元剤と
して添加する方法とは異なり、窒素化合物を残留塩素の
当量のlθ倍程度の大過剰添加した場合においても、処
理水水質の低下の問題はない。
It is preferable that the amount of the nitrogen compound added be slightly in excess of the equivalent of residual chlorine in the raw water, particularly preferably 1.3 to 2.0 equivalents of the residual chlorine in the raw water. In the present invention, unlike the conventional method of adding sulfur-based compounds as reducing agents, even when nitrogen compounds are added in large excess of about lθ times the equivalent of residual chlorine, the problem of deterioration of the quality of treated water is avoided. do not have.

[作用] 窒素化合物としてヒドラジン(N2H4)を添加した場
合、ヒドラジンは、原水中の塩素を2CM2+N2H4
→N2 +4HC1なる反応で還元する。しかして、過
剰のN2H4及び還元反応において生成するHC!Lは
イオン交換樹脂に捕捉されるので処理水中にリークする
ことがなく、また、N2は不活性物質であるから処理水
水質は良好に維持される。しかも、N a HS O3
等の硫黄化合物は陽イオン及び陰イオンの負荷を有する
のに対し、ヒドラジンはイオン交換樹脂の陽イオンに対
する負荷のみであるため、陰イオンブレークの恐れは全
くない。
[Action] When hydrazine (N2H4) is added as a nitrogen compound, hydrazine converts chlorine in raw water into 2CM2+N2H4
→Reduced by the reaction N2 +4HC1. Therefore, excess N2H4 and HC generated in the reduction reaction! Since L is captured by the ion exchange resin, it does not leak into the treated water, and since N2 is an inert substance, the quality of the treated water is maintained at a good level. Moreover, Na HS O3
Whereas sulfur compounds such as hydrazine have a load of cations and anions, hydrazine has only a load of cations of the ion exchange resin, so there is no fear of anion break.

また、窒素化合物がN a N 02やK N O2の
場合も、HCl l!:N a N O3あるいはK 
N O3が生ずるが、これらはイオン交換樹脂で捕捉さ
れる。
Also, when the nitrogen compound is NaN02 or KNO2, HCl l! :N a N O3 or K
N O3 is produced and these are captured by the ion exchange resin.

このため、本発明によれば、原水中の残留塩素を還元す
ることにより、イオン交換樹脂の酸化劣化を防止し、長
期間にわたって安定したイオン交換処理を可能とし、し
かも還元剤の過剰分によりイオン交換処理水の水質を低
下させることもない。
Therefore, according to the present invention, by reducing the residual chlorine in raw water, it is possible to prevent oxidative deterioration of the ion exchange resin and to perform stable ion exchange treatment over a long period of time. There is no reduction in the quality of the exchange treated water.

[実施例] 以下に本発明を実施例及び比較例を挙げて更に具体的に
説明するが、本発明はその要旨を超えない限り、以下の
実施例に限定されるものではない。
[Examples] The present invention will be described in more detail below with reference to Examples and Comparative Examples, but the present invention is not limited to the following Examples unless it exceeds the gist thereof.

比較例1 横浜市水道水(塩素濃度0.3ppm、導電率120ル
s/cm)を、RO膜分離装置→混床式イオン交換装置
→カートリッジ純水器に順次通水して純水を製造するシ
ステムにおいて、温床式イオン交換装置への供給側にお
いて、原水にN a HS O3をlOppm添加して
、純水の製造を行った0通水は5V=33 (hr−’
) で行い。
Comparative Example 1 Pure water was produced by sequentially passing Yokohama city tap water (chlorine concentration 0.3 ppm, conductivity 120 s/cm) through an RO membrane separation device → mixed bed ion exchange device → cartridge deionizer In this system, on the supply side to the hotbed type ion exchanger, 10ppm of Na HS O3 is added to the raw water to produce pure water.
).

用いた混床式イオン交換装置及びカートリッジ純水器の
仕様は下記の通りである。
The specifications of the mixed bed ion exchange device and cartridge deionizer used are as follows.

イオン  ゛ カラム本体:50mmφX10X100O陽イオン交換
樹脂:ダイヤイオンPK228(三菱化成工業補装) 200m!;L 陰イオン交換樹脂:ダイヤイオンPA312(三菱化成
工業■製) 400m文 カ −  ト  リ  −  シ カラム本体:25mmφX 600 m m Hイオン
交換樹脂:ダイヤイオンSMN−UP(三菱化成工業補
装、 陽・陰イオン混合樹脂) カートリッジ純水器の出口側に設けられたCIA水質計
により、処理水の水質を調べたところ、頭初において比
抵抗16MΩ・Cmであったものが、1.5時間後には
IOMΩ・cmに低下し、処理水の純度が経時的に低下
することが判明した。
Ion Column body: 50mmφX10X100O Cation exchange resin: Diaion PK228 (Mitsubishi Chemical Co., Ltd.) 200m! ; L Anion exchange resin: Diaion PA312 (manufactured by Mitsubishi Chemical Industries, Ltd.) 400 m column body: 25 mm φ When the quality of the treated water was examined using a CIA water quality meter installed on the outlet side of the cartridge water purifier, the specific resistance was 16MΩ・Cm at the beginning, but after 1.5 hours It was found that the purity of the treated water decreased over time.

実施例1 N a HS O3(7)代りに、N 2 H4を10
ppm添加したこと以外は比較例1と同様にして純水の
製造を行い、カートリッジ純水器の出口側において処理
水の水質を調べた。
Example 1 Instead of N a HS O3 (7), N 2 H4 was added to 10
Pure water was produced in the same manner as in Comparative Example 1 except that ppm was added, and the quality of the treated water was examined on the outlet side of the cartridge water purifier.

その結果、処理水の水質は17MΩ・cmで一定してお
り、24時間通水後においても水質が低下することはな
かった。
As a result, the quality of the treated water was constant at 17 MΩ·cm, and the water quality did not deteriorate even after water flow for 24 hours.

実施例1より、本発明の方法によれば、極めて高純度の
純水を長期間安定して製造することができることが明ら
かである。
From Example 1, it is clear that according to the method of the present invention, extremely high purity pure water can be stably produced over a long period of time.

[効果] 以上詳述した通り、本発明の純水製造装置は、原水中の
残留塩素の還元剤として窒素化合物を添加するものであ
り、 ■ 硫黄化合物を還元剤として添加する従来法に比し、
高純度の純水を製造し得る。
[Effects] As detailed above, the pure water production apparatus of the present invention adds a nitrogen compound as a reducing agent for residual chlorine in raw water. ,
High purity pure water can be produced.

■ 還元剤の過剰添加によりイオン交換処理水の水質が
低下することがない。
■ The quality of ion exchange treated water does not deteriorate due to excessive addition of reducing agent.

■ このため還元剤の添加量の抑制等の煩雑な操作を必
要としない。
(2) Therefore, there is no need for complicated operations such as controlling the amount of reducing agent added.

■ 窒素化合物は硫黄化合物に比し、大気中で安定で劣
化し難く、安定保存期間が長いことから、処理操作が簡
便である。
- Compared to sulfur compounds, nitrogen compounds are more stable in the atmosphere, less susceptible to deterioration, and have a longer stable storage period, making treatment operations easier.

等の効果が奏される。Effects such as this are produced.

このため、本発明によれば極めて高純度の純水あるは超
純水を長期間安定して製造することができ、LSIや超
LSIの洗浄工程における超純水の製造等、各種分野に
おいて工業的に極めて有利である。
Therefore, according to the present invention, extremely high-purity pure water or ultrapure water can be produced stably for a long period of time, and can be used industrially in various fields, such as the production of ultrapure water in the cleaning process of LSIs and ultra-LSIs. This is extremely advantageous.

Claims (2)

【特許請求の範囲】[Claims] (1)残留塩素を含有する原水をイオン交換樹脂層に通
水して純水を得る方法において、原水に窒素化合物を添
加することを特徴とする純水製造方法。
(1) A method for producing pure water, characterized in that a nitrogen compound is added to the raw water in a method for obtaining pure water by passing raw water containing residual chlorine through an ion exchange resin layer.
(2)窒素化合物がヒドラジンであることを特徴とする
特許請求の範囲第1項に記載の純水製造方法。
(2) The method for producing pure water according to claim 1, wherein the nitrogen compound is hydrazine.
JP60094121A 1985-05-01 1985-05-01 Method for making pure water Granted JPS61254292A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60094121A JPS61254292A (en) 1985-05-01 1985-05-01 Method for making pure water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60094121A JPS61254292A (en) 1985-05-01 1985-05-01 Method for making pure water

Publications (2)

Publication Number Publication Date
JPS61254292A true JPS61254292A (en) 1986-11-12
JPH0142753B2 JPH0142753B2 (en) 1989-09-14

Family

ID=14101589

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60094121A Granted JPS61254292A (en) 1985-05-01 1985-05-01 Method for making pure water

Country Status (1)

Country Link
JP (1) JPS61254292A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01119344A (en) * 1987-11-02 1989-05-11 Tokyo Organ Chem Ind Ltd Method for decreasing eluate of cation-exchange resin of high acidity
JPH01119345A (en) * 1987-11-02 1989-05-11 Tokyo Organ Chem Ind Ltd Method for decreasing eluate of anion-exchange resin of high basicity
JPH0299146A (en) * 1988-10-05 1990-04-11 Tokyo Organ Chem Ind Ltd Method for reducing eluted substance from mixed resin bed
US4941897A (en) * 1987-11-05 1990-07-17 L & H Technologies, Inc. Microporous filter and method

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5550481A (en) * 1978-10-03 1980-04-12 Asahi Denka Kogyo Kk Removing method of residual chlorine in salt water

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5550481A (en) * 1978-10-03 1980-04-12 Asahi Denka Kogyo Kk Removing method of residual chlorine in salt water

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01119344A (en) * 1987-11-02 1989-05-11 Tokyo Organ Chem Ind Ltd Method for decreasing eluate of cation-exchange resin of high acidity
JPH01119345A (en) * 1987-11-02 1989-05-11 Tokyo Organ Chem Ind Ltd Method for decreasing eluate of anion-exchange resin of high basicity
US4941897A (en) * 1987-11-05 1990-07-17 L & H Technologies, Inc. Microporous filter and method
JPH0299146A (en) * 1988-10-05 1990-04-11 Tokyo Organ Chem Ind Ltd Method for reducing eluted substance from mixed resin bed

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JPH0142753B2 (en) 1989-09-14

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