JPH04346842A - Reactivating method for mixed bed deionizer - Google Patents
Reactivating method for mixed bed deionizerInfo
- Publication number
- JPH04346842A JPH04346842A JP3145399A JP14539991A JPH04346842A JP H04346842 A JPH04346842 A JP H04346842A JP 3145399 A JP3145399 A JP 3145399A JP 14539991 A JP14539991 A JP 14539991A JP H04346842 A JPH04346842 A JP H04346842A
- Authority
- JP
- Japan
- Prior art keywords
- exchange resin
- cation exchange
- anion exchange
- mixed bed
- container
- 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
Links
- 238000000034 method Methods 0.000 title claims abstract 3
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims abstract description 24
- 239000003729 cation exchange resin Substances 0.000 claims abstract description 24
- 239000003957 anion exchange resin Substances 0.000 claims abstract description 22
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000000746 purification Methods 0.000 claims description 9
- 230000001172 regenerating effect Effects 0.000 claims description 3
- 238000005406 washing Methods 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims description 2
- 230000005484 gravity Effects 0.000 abstract description 5
- 238000004140 cleaning Methods 0.000 abstract description 4
- 238000005349 anion exchange Methods 0.000 abstract 1
- 238000011069 regeneration method Methods 0.000 description 6
- 230000008929 regeneration Effects 0.000 description 4
- 239000011347 resin Substances 0.000 description 4
- 229920005989 resin Polymers 0.000 description 4
- 150000001768 cations Chemical class 0.000 description 2
- 206010067482 No adverse event Diseases 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】この発明は、陰イオン交換樹脂と
陽イオン交換樹脂を併用した混床式純水装置のための最
適の再成方法を提供するものである。FIELD OF INDUSTRIAL APPLICATION This invention provides an optimal regeneration method for a mixed bed type water purification apparatus that uses both an anion exchange resin and a cation exchange resin.
【0002】0002
【従来の技術】陰イオン交換樹脂と陽イオン交換樹脂と
を単一の容器内に充填し、それらの樹脂を通して純水を
得るようにした混床式純水装置の再成に当っては、従来
、HClを適用して陽イオン交換樹脂を再成した後、N
aOHを適用して陰イオン交換樹脂を再成することが常
套的に行なわれている。[Prior Art] In reproducing a mixed bed type water purification device in which an anion exchange resin and a cation exchange resin are filled in a single container and pure water is obtained through these resins, Traditionally, after regenerating the cation exchange resin by applying HCl, N
It is routine to apply aOH to regenerate anion exchange resins.
【0003】しかるに、従来の再成方法では、HCl
で一旦再成された陽イオン交換樹脂が、続いて適用され
るNaOHにより能力低下を起こし易い。However, in the conventional regeneration method, HCl
The cation exchange resin once regenerated is likely to suffer a decrease in capacity due to subsequent application of NaOH.
【0004】発明者等の知見によると、HCl による
陽イオン交換樹脂の再成後に、NaOHを適用した場合
、上位に位置する陰イオン交換樹脂を通って流下するN
aOHが中間のレベルを越えて下位の陽イオン交換樹脂
中に流入することが確かめられており、このために先に
処理した陽イオン交換樹脂の再成状態が部分的又は全体
的に悪化する。勿論、上述によって再成が不十分な状態
にある陽イオン交換樹脂を使用するときは、Ca2+や
Mg2+等の硬度成分を有効に取り除くことができない
。According to the findings of the inventors, when NaOH is applied after regeneration of the cation exchange resin with HCl, the N flowing down through the upper anion exchange resin is
It has been found that aOH flows above intermediate levels into the underlying cation exchange resin, thereby partially or totally deteriorating the regeneration conditions of the previously treated cation exchange resin. Of course, when using a cation exchange resin that has been insufficiently regenerated as described above, hard components such as Ca2+ and Mg2+ cannot be effectively removed.
【0005】[0005]
【発明が解決しようとする課題】この発明は、上述に着
目し、混床式の純水装置の再成に当って陰イオン交換樹
脂と陽イオン交換樹脂の両者の比重差を考慮して、その
適用順序を規定することにより、陰イオン交換樹脂及び
陽イオン交換樹脂の確実な再成を可能にしたものである
。[Problems to be Solved by the Invention] Focusing on the above, the present invention takes into account the difference in specific gravity between anion exchange resin and cation exchange resin when regenerating a mixed bed type water purification device. By specifying the order of application, it is possible to reliably regenerate the anion exchange resin and cation exchange resin.
【0006】[0006]
【課題を解決するための手段】即ち、この発明は、単一
容器内に陰イオン交換樹脂及び陽イオン交換樹脂をそれ
ぞれ充填して成る混床式純水装置の使用において、水そ
の他の洗浄媒体による撹拌、洗浄操作後に、最初に容器
上部よりNaOHを適用して陰イオン交換樹脂を再成し
、次で容器下部よりHCl を使用することによって陽
イオン交換樹脂を再成する操作を行なうことを特徴とし
ている。[Means for Solving the Problems] That is, the present invention provides water and other cleaning media in the use of a mixed bed type water purification device in which an anion exchange resin and a cation exchange resin are respectively filled in a single container. After stirring and washing operations, the anion exchange resin is first regenerated by applying NaOH from the top of the container, and then the cation exchange resin is regenerated by using HCl from the bottom of the container. It is a feature.
【0007】[0007]
【発明の実施例】図1は、前述した混床式純水装置の構
成を概略的に表わしたものである。同図において、(1
) は実質上単一構造とした容器、(2)及び(3)
は容器(1) 内に、それぞれ充填した陰イオン交換樹
脂及び陽イオン交換樹脂、(5) は容器上部の取入れ
口、(6) は容器下部の取出し口を示す。DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 schematically shows the configuration of the mixed bed type water purification apparatus described above. In the same figure, (1
) is a substantially unitary container, (2) and (3)
1 shows the anion exchange resin and cation exchange resin filled in the container (1), (5) shows the intake port at the top of the container, and (6) shows the outlet at the bottom of the container.
【0008】この発明は、上述のような混床式純水装置
を使用するものであって、通常の稼働時は、原水を取入
れ口(5) から連続注水することにより、これを取出
し口(6)から純水として取り出すことができるように
なっている。そうして、所定量の(一定稼働時間経過後
の)通水が終了したならば、圧搾空気ないしは水その他
の洗浄媒体を取入れ口(5) より供給し、これによっ
て陰イオン交換樹脂(2) 、陽イオン交換樹脂(3)
を全体的に撹拌し、洗浄する訳であるが、この洗浄操
作を終えた時点では、それらの樹脂は、各々の比重差に
従って上位に陰イオン交換樹脂(2) が、又下位に陽
イオン交換樹脂(3) がそれぞれ位置している。[0008] The present invention uses the above-mentioned mixed bed type water purification device, and during normal operation, raw water is continuously injected from the intake port (5) and is taken out from the outlet (5). 6) can be extracted as pure water. Then, when a predetermined amount of water (after a certain operating time) has been passed, compressed air, water, or other cleaning medium is supplied from the intake port (5), and this causes the anion exchange resin (2) to flow through the anion exchange resin (2). , cation exchange resin (3)
The entire resin is stirred and washed, but at the end of this washing operation, the anion exchange resin (2) is placed at the top according to the difference in specific gravity, and the cation exchange resin (2) is placed at the bottom. Resin (3) is located respectively.
【0009】この発明では、上記に鑑み、最初に容器上
部の取入れ口(5) からNaOHを所要量注入して、
陰イオン交換樹脂(2) を再成する。これによって、
陰イオン交換樹脂(2) の全量が再成されてから、下
位の陽イオン交換樹脂(3) 中にNaOHが浸入した
としても、既に陽イオンは、NaやCaにより置換され
ているために、悪影響を受けることがない。次いで、H
Cl を適用し、これを取出し口(6) より適量注入
すると、上位の陰イオン交換樹脂(2) に対しては比
重差により実質上影響を影響を与えることなく、陽イオ
ン交換樹脂(3) を全体的かつ確実に再成することが
可能となる。In this invention, in view of the above, the required amount of NaOH is first injected from the intake port (5) at the top of the container.
Regenerate the anion exchange resin (2). by this,
Even if NaOH intrudes into the lower cation exchange resin (3) after the entire amount of the anion exchange resin (2) has been regenerated, the cations have already been replaced by Na and Ca. There will be no adverse effects. Then, H
When Cl is applied and an appropriate amount is injected from the outlet (6), the upper anion exchange resin (2) is virtually unaffected due to the difference in specific gravity, and the cation exchange resin (3) can be completely and reliably regenerated.
【0010】0010
【発明の効果】叙上のように、この発明は、混床式純水
装置における陰イオン交換樹脂と陽イオン交換樹脂の両
者の比重比を考慮して、それらの樹脂の確実な再成を実
現し得る最適の再成処理を行なうものであるので、溶存
酸素等の陰イオンによって置換処理されるものや、Ca
やMg等の硬度成分であって陽イオンにより置換処理さ
れるもののいずれについても、これを効果的に除去し、
所望の純水を製造することができる。[Effects of the Invention] As described above, the present invention takes into consideration the specific gravity ratio of both anion exchange resin and cation exchange resin in a mixed bed type water purification device, and ensures reliable regeneration of these resins. Since it performs the most suitable regeneration treatment that can be realized, it
Effectively removes hardness components such as and Mg that are replaced by cations,
Desired pure water can be produced.
【図1】混床式純水装置の構成を概略的に表わした説明
図である。FIG. 1 is an explanatory diagram schematically showing the configuration of a mixed bed type pure water apparatus.
1 容器 2 陰イオン交換樹脂 3 陽イオン交換樹脂 1 Container 2 Anion exchange resin 3 Cation exchange resin
Claims (1)
脂(2) 及び陽イオン交換樹脂(3) をそれぞれ充
填して成る混床式純水装置の使用において、水その他の
洗浄媒体による撹拌、洗浄操作後に、最初に容器上部よ
りNaOHを適用して陰イオン交換樹脂を再成し、次で
容器下部よりHCl を適用することによって陽イオン
交換樹脂を再成する操作を行なうことを特徴とする混床
式純水装置の再成方法。[Claim 1] In the use of a mixed bed type water purification device consisting of a single container (1) filled with an anion exchange resin (2) and a cation exchange resin (3), After stirring and washing operations, NaOH is first applied from the top of the container to regenerate the anion exchange resin, and then HCl is applied from the bottom of the container to regenerate the cation exchange resin. A method for regenerating a mixed bed type water purification system.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3145399A JPH04346842A (en) | 1991-05-20 | 1991-05-20 | Reactivating method for mixed bed deionizer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3145399A JPH04346842A (en) | 1991-05-20 | 1991-05-20 | Reactivating method for mixed bed deionizer |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04346842A true JPH04346842A (en) | 1992-12-02 |
Family
ID=15384361
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3145399A Pending JPH04346842A (en) | 1991-05-20 | 1991-05-20 | Reactivating method for mixed bed deionizer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04346842A (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5068964A (en) * | 1973-09-29 | 1975-06-09 | ||
JPH02126943A (en) * | 1988-11-06 | 1990-05-15 | Kotobuki Kogyo Kk | Method for regenerating ion-exchange resin of mixed-bed deionizer |
-
1991
- 1991-05-20 JP JP3145399A patent/JPH04346842A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5068964A (en) * | 1973-09-29 | 1975-06-09 | ||
JPH02126943A (en) * | 1988-11-06 | 1990-05-15 | Kotobuki Kogyo Kk | Method for regenerating ion-exchange resin of mixed-bed deionizer |
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