JPH03275189A - Detection of break point in ion exchange resin and method and equipment for producing pure water and ultrapure water - Google Patents

Detection of break point in ion exchange resin and method and equipment for producing pure water and ultrapure water

Info

Publication number
JPH03275189A
JPH03275189A JP2074062A JP7406290A JPH03275189A JP H03275189 A JPH03275189 A JP H03275189A JP 2074062 A JP2074062 A JP 2074062A JP 7406290 A JP7406290 A JP 7406290A JP H03275189 A JPH03275189 A JP H03275189A
Authority
JP
Japan
Prior art keywords
ion exchange
exchange resin
toc
water
pure water
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
JP2074062A
Other languages
Japanese (ja)
Inventor
Nobuko Hashimoto
橋本 信子
Hitoshi Sato
等 佐藤
Yasunari Uchitomi
内富 康成
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.)
Hitachi Plant Technologies Ltd
Original Assignee
Hitachi Plant Technologies 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 Hitachi Plant Technologies Ltd filed Critical Hitachi Plant Technologies Ltd
Priority to JP2074062A priority Critical patent/JPH03275189A/en
Publication of JPH03275189A publication Critical patent/JPH03275189A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To efficiently produce pure water and ultrapure water by measuring the concn. of total organic carbon(TOC) in water permeated through ion exchange resin and detecting the saturation point of TOC adsorption due to ion exchange resin as the break point of this ion exchange resin. CONSTITUTION:Ultrapure water 7 is produced by successively passing the water 1 treated with a two-stages reverse osmosis through an ion exchange resin device 2, a low-pressure ultraviolet-ray oxidizing device 3, an anion polisher 4, a cartridge polisher 5 and an ultrafiltration device 6. In this producing process, a TOC meter 8 is provided to the outlet side of the ion exchange resin device 2 and TOC of permeated water sent from the device 2 is measured. Saturation point of TOC adsorption due to ion exchange resin is detected as a break point of ion exchange resin. When this ion exchange resin is regenerated at a point of this time, TOC load in the devices after the low-pressure ultraviolet-ray oxidizing device 3 is reduced.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、イオン交換樹脂のブレークポイント(破過点
)の検出方法及び該方法を用いて純水・超純水を製造す
る方法及び装置に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for detecting a break point of an ion exchange resin, and a method and apparatus for producing pure water/ultrapure water using the method. Regarding.

〔従来の技術〕[Conventional technology]

従来、市水から純水を製造するため、イオン交換プロセ
スが利用されている。このイオン交換プロセスにおいて
は、通水を続けると、イオン交換樹脂のブレークポイン
トに達するので、イオン交換樹脂量や市水中のイオジ量
に応じて樹脂の再生処理を行う必要がある。従来、ブレ
ークポイントの検出には、比抵抗(導電率)計が使用さ
れている。
Traditionally, ion exchange processes have been used to produce pure water from city water. In this ion exchange process, if water continues to flow, the break point of the ion exchange resin will be reached, so it is necessary to regenerate the resin depending on the amount of ion exchange resin and the amount of iodine in city water. Conventionally, a resistivity (conductivity) meter has been used to detect breakpoints.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

比抵抗計によりブレークポイントを検出する方法は、イ
オン交換樹脂によって無機イオンが交換され、比抵抗値
が低下したときをブレークポイントとするものであるが
、一般に、市水には有機物も含まれているため、−次純
水装置では次に来る超純水装置で有機物を除去しなけれ
ばならない。
The method of detecting a breakpoint using a resistivity meter is to detect the breakpoint when inorganic ions are exchanged with an ion exchange resin and the resistivity value decreases, but generally city water also contains organic matter. Therefore, organic matter must be removed in the ultra-pure water equipment that follows the ultra-pure water equipment.

すなわち、有機物除去のため、紫外線酸化装置を大きく
したり、また、超純水装置で使用するカーあった。
In other words, in order to remove organic matter, the size of the ultraviolet oxidation equipment was required, and the car used in the ultrapure water equipment was needed.

したがって、本発明は、前記の従来技術の欠点を解消し
、水質の処理目標値を管理するために有機物(TOC)
を検出することができ、イオン交換樹脂のブレークポイ
ントを早期に的確に検出する方法及びこの方法を用いて
純水・超純水を効率よく製造しろる方法及び装置を提供
することを目的とする。
Therefore, the present invention solves the drawbacks of the prior art described above, and aims to reduce organic matter (TOC) in order to manage the treatment target value of water quality.
The purpose of the present invention is to provide a method for early and accurate detection of breakpoints in ion exchange resins, and a method and apparatus for efficiently producing pure water and ultrapure water using this method. .

〔課題を解決するための手段〕[Means to solve the problem]

本発明は、イオン交換樹脂に有機物が吸着されるが、有
機物の吸着は塩類(無機イオン)より先に飽和点に達し
、イオン交換樹脂によって塩類が交換され、比抵抗値が
低下するより先に有機物が吸着されなくなることを見出
し、この知見に基づいて完成したものである。
In the present invention, organic matter is adsorbed to the ion exchange resin, but the organic matter adsorption reaches a saturation point before salts (inorganic ions), and before the salts are exchanged by the ion exchange resin and the specific resistance value decreases. It was discovered that organic substances were no longer adsorbed, and was completed based on this knowledge.

すなわち、本発明によるイオン交換樹脂のブレークポイ
ントの検出方法は、イオン交換樹脂透過水のTOCを測
定し、イオン交換樹脂によるTOC吸着の飽和点をイオ
ン交換樹脂のブレークポイントとすることを特徴とする
That is, the method for detecting the break point of an ion exchange resin according to the present invention is characterized by measuring the TOC of water permeated through the ion exchange resin, and setting the saturation point of TOC adsorption by the ion exchange resin as the break point of the ion exchange resin. .

TOCの測定は、従来公知のTOC計を用いて行うこと
ができる。
TOC measurement can be performed using a conventionally known TOC meter.

本発明によるイオン交換樹脂のブレークポイントの検出
方法は、特に、純水・超純水の製造プロセスに好適に適
用することができ、イオン交換樹脂に通水する水は、市
水ばかりでなく、逆浸透法などによる処理水であっても
よい。
The method for detecting breakpoints in ion exchange resins according to the present invention can be particularly suitably applied to processes for producing pure water and ultrapure water. Water treated by reverse osmosis or the like may also be used.

すなわち、本発明は、さらに、イオン交換樹脂装置、低
圧紫外線酸化装置、アニオンポリラシャ、カートリ・・
ジポリ・・シャー及び限外a過膜装置に順次通水するこ
とGこよって純水・超純水を製造する方法において、イ
オン交換装置からの透過水のTOCを測定し、イオン交
換樹脂によるT。
That is, the present invention further provides an ion-exchange resin device, a low-pressure ultraviolet oxidation device, an anionic polyurethane, a cartridge, etc.
In a method for producing pure water or ultrapure water by sequentially passing water through a dipoly shear and an ultra-a membrane device, the TOC of permeated water from an ion exchange device is measured, and the TOC caused by the ion exchange resin is measured. .

C吸着が飽和点に達したら、イオン交換樹脂を再生する
ことを特徴とする純水・超純水の製造方法及びイオン交
換樹脂装置、低圧紫外線酸化装置、アニオンポリッシャ
ー、カートリッジボリソシャー及び限外口過膜装置から
成る純水・超純水の製造装置において、イオン交換樹脂
装置の出口側にTOC計を設置したことを特徴とする純
水・超純水の製造装置を提供するものである。
A method for producing pure water and ultrapure water, characterized by regenerating the ion exchange resin when C adsorption reaches the saturation point, and an ion exchange resin device, a low pressure ultraviolet oxidation device, an anion polisher, a cartridge borisosher, and an ultrapure water The present invention provides a pure water/ultra pure water producing apparatus comprising a membrane filter device, characterized in that a TOC meter is installed on the outlet side of the ion exchange resin device. .

さらに、本発明の純水・超純水の製造装置においては、
イオン交換樹脂装置の前に逆浸透装置を接続することも
できる。
Furthermore, in the pure water/ultra pure water production apparatus of the present invention,
A reverse osmosis device can also be connected before the ion exchange resin device.

〔実施例〕〔Example〕

次に、実施例に基づいて本発明をさらに詳しく説明する
が、本発明はこれに限定されるものではない。
Next, the present invention will be explained in more detail based on Examples, but the present invention is not limited thereto.

第1図は、本発明の一実施例を示す超純水製造装置の略
本系統図である。第1図に示した超純水製造装置におい
ては、二段逆浸透処理水1をイオン交換樹脂装置2、低
圧紫外線酸化装置3、アニオンポリッシャー4、カート
リッジポリラシャ・−5及び限外口過収装M6に順次通
水し、超純水7を製造する。この超純水製造装置におい
て、イオン交換樹脂装置2の出口側にばTOC計8が設
置されている。
FIG. 1 is a schematic system diagram of an ultrapure water production apparatus showing an embodiment of the present invention. In the ultrapure water production apparatus shown in FIG. Water is sequentially passed through the container M6 to produce ultrapure water 7. In this ultrapure water production apparatus, a TOC meter 8 is installed on the outlet side of the ion exchange resin device 2.

イオン交換樹脂装置2に通水したときのTOCの経時変
化をTOC計8で測定した結果を第2図に示す。また、
比較のため、イオン交換樹脂装置2の出口において比抵
抗値を測定し、その経時変化を同様に第2図に示す。第
2図から明らかなとおり、イオン交換樹脂のTOC吸着
は、塩類より先に行われ、イオン交換樹脂に塩類が吸着
され、比抵抗値が低下するより5時間以上早<TOCが
吸着されなくなる。
FIG. 2 shows the results of measuring the change in TOC over time using a TOC meter 8 when water was passed through the ion exchange resin device 2. Also,
For comparison, the specific resistance value was measured at the outlet of the ion exchange resin device 2, and its change over time is similarly shown in FIG. As is clear from FIG. 2, the ion exchange resin adsorbs TOC before the salts, and the ion exchange resin adsorbs the salts and stops adsorbing TOC more than 5 hours earlier than the specific resistance value decreases.

したがって、この時点で、イオン交換樹脂を再生すると
、低圧紫外線酸化装置3以降の装置におけるTOCの負
荷が少なくなるため、効率よく超純水を製造することが
できる。
Therefore, if the ion exchange resin is regenerated at this point, the TOC load on the devices after the low-pressure ultraviolet oxidation device 3 will be reduced, and ultrapure water can be efficiently produced.

〔発明の効果〕〔Effect of the invention〕

本発明の方法によりイオン交換樹脂のブレークポイント
を検出すれば、イオン交換樹脂によるTOC吸着が確実
に行われる。したがって、このブレークポイントの検出
方法を純水・超純水の製造に応用することにより後段の
処理装置への負荷が著しく軽減され、効率よく純水・超
純水を製造することができる。
If the breakpoint of the ion exchange resin is detected by the method of the present invention, TOC adsorption by the ion exchange resin can be reliably performed. Therefore, by applying this breakpoint detection method to the production of pure water and ultrapure water, the load on the subsequent processing equipment is significantly reduced, and pure water and ultrapure water can be efficiently produced.

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

第1図は本発明の一実施例を示す超純水の製造装置の系
統図、第2図はイオン交換装置の透過水のTOC及び比
抵抗値の経時変化図である。 符号の説明 2・・・イオン交換樹脂装置、3・・・低圧紫外線酸化
装置、4・・・アニオンボリッシャー7・・・超純水、
8・・・TOC計 特許出廟人 日立プラント建設株式会社 625− ○O,L ■猾用
FIG. 1 is a system diagram of an ultrapure water production apparatus showing an embodiment of the present invention, and FIG. 2 is a diagram of changes over time in TOC and specific resistance values of permeated water from an ion exchange device. Explanation of symbols 2...Ion exchange resin device, 3...Low pressure ultraviolet oxidation device, 4...Anion bolisher 7...Ultra pure water,
8...TOC meter patent author Hitachi Plant Construction Co., Ltd. 625- ○O,L ■For

Claims (4)

【特許請求の範囲】[Claims] (1)イオン交換樹脂透過水のTOCを測定し、イオン
交換樹脂によるTOC吸着の飽和点をイオン交換樹脂の
ブレークポイントとすることを特徴とするイオン交換樹
脂のブレークポイントの検出方法。
(1) A method for detecting a break point in an ion exchange resin, which comprises measuring the TOC of water permeated through the ion exchange resin, and setting the saturation point of TOC adsorption by the ion exchange resin as the break point of the ion exchange resin.
(2)イオン交換樹脂装置、低圧紫外線酸化装置、アニ
オンポリッシャー、カートリッジポリッシャー及び限外
ろ過膜装置に順次通水することによって純水・超純水を
製造する方法において、イオン交換装置からの透過水の
TOCを測定し、イオン交換樹脂によるTOC吸着が飽
和点に達したら、イオン交換樹脂を再生することを特徴
とする純水・超純水の製造方法。
(2) In a method for producing pure water/ultrapure water by sequentially passing water through an ion exchange resin device, a low-pressure ultraviolet oxidation device, an anion polisher, a cartridge polisher, and an ultrafiltration membrane device, permeated water from the ion exchange device A method for producing pure water or ultrapure water, which comprises measuring the TOC of the ion exchange resin and regenerating the ion exchange resin when the TOC adsorption by the ion exchange resin reaches a saturation point.
(3)イオン交換樹脂装置、低圧紫外線酸化装置、アニ
オンポリッシャー、カートリッジポリッシャー及び限外
ろ過膜装置から成る純水・超純水の製造装置において、
イオン交換樹脂装置の出口側にTOC計を設置したこと
を特徴とする純水・超純水の製造装置。
(3) In a pure water/ultra pure water production device consisting of an ion exchange resin device, a low pressure ultraviolet oxidation device, an anion polisher, a cartridge polisher, and an ultrafiltration membrane device,
A pure water/ultra pure water production device characterized by a TOC meter installed on the outlet side of an ion exchange resin device.
(4)イオン交換樹脂装置の前に逆浸透装置が設置され
ている請求項3記載の純水・超純水の製造装置。
(4) The pure water/ultra pure water production apparatus according to claim 3, wherein a reverse osmosis device is installed in front of the ion exchange resin device.
JP2074062A 1990-03-23 1990-03-23 Detection of break point in ion exchange resin and method and equipment for producing pure water and ultrapure water Pending JPH03275189A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2074062A JPH03275189A (en) 1990-03-23 1990-03-23 Detection of break point in ion exchange resin and method and equipment for producing pure water and ultrapure water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2074062A JPH03275189A (en) 1990-03-23 1990-03-23 Detection of break point in ion exchange resin and method and equipment for producing pure water and ultrapure water

Publications (1)

Publication Number Publication Date
JPH03275189A true JPH03275189A (en) 1991-12-05

Family

ID=13536335

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2074062A Pending JPH03275189A (en) 1990-03-23 1990-03-23 Detection of break point in ion exchange resin and method and equipment for producing pure water and ultrapure water

Country Status (1)

Country Link
JP (1) JPH03275189A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05293468A (en) * 1992-04-17 1993-11-09 T & C Technical:Kk Fresh water generating mechanism
JP2006075820A (en) * 2004-08-10 2006-03-23 Kobelco Eco-Solutions Co Ltd Method and apparatus for treating waste water
JP2013208566A (en) * 2012-03-30 2013-10-10 Kurita Water Ind Ltd Breakthrough detection method and operation method of ion exchange device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05293468A (en) * 1992-04-17 1993-11-09 T & C Technical:Kk Fresh water generating mechanism
JP2006075820A (en) * 2004-08-10 2006-03-23 Kobelco Eco-Solutions Co Ltd Method and apparatus for treating waste water
JP2013208566A (en) * 2012-03-30 2013-10-10 Kurita Water Ind Ltd Breakthrough detection method and operation method of ion exchange device

Similar Documents

Publication Publication Date Title
CA1251145A (en) Reverse osmosis system
JP3200301B2 (en) Method and apparatus for producing pure or ultrapure water
US5310486A (en) Multi-stage water treatment system and method for operating the same
US5935441A (en) Water purification process
JPH1085743A (en) Method and apparatus for treating water containing boron
US4036751A (en) Method of treating water containing chromate
JP6362299B2 (en) Operation method of ion exchange resin apparatus and ion exchange resin apparatus
JPH03275189A (en) Detection of break point in ion exchange resin and method and equipment for producing pure water and ultrapure water
JP5915295B2 (en) Pure water production method
JPS62110795A (en) Device for producing high-purity water
JPH1080684A (en) Device and method for treating boron-containing water
JPH07962A (en) Production of pure water
JPH09122690A (en) Method for decomposing organic nitrogen and water treatment apparatus
JP3951200B2 (en) Pure water production equipment
JP3993370B2 (en) Method for recovering Cr (V1) from anion exchange resin tower
JP2002361246A (en) Method and device for manufacturing drinking water
JP3178969B2 (en) Pure or ultrapure water production equipment
JPH04210288A (en) Production of super pure water
JP2001335315A (en) Apparatus and method for refining boron eluent
JP4411669B2 (en) Regeneration method of cation exchange resin
JPH11156357A (en) Water purifying apparatus
JP2003190948A (en) Method and apparatus for ion exchange treatment of vanadium-containing water
JP2008062223A (en) Membrane filtering method and membrane filtering system
JPH01245893A (en) Method for making ultrapure water
JP3673393B2 (en) Regeneration method of ion adsorption membrane for ultrapure water production and ultrapure water production method