JPH0647556Y2 - Ion exchange resin tower - Google Patents

Ion exchange resin tower

Info

Publication number
JPH0647556Y2
JPH0647556Y2 JP1990036546U JP3654690U JPH0647556Y2 JP H0647556 Y2 JPH0647556 Y2 JP H0647556Y2 JP 1990036546 U JP1990036546 U JP 1990036546U JP 3654690 U JP3654690 U JP 3654690U JP H0647556 Y2 JPH0647556 Y2 JP H0647556Y2
Authority
JP
Japan
Prior art keywords
resin layer
tower
exchange resin
ion exchange
collector
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.)
Expired - Lifetime
Application number
JP1990036546U
Other languages
Japanese (ja)
Other versions
JPH03128430U (en
Inventor
一行 小山
Original Assignee
荏原インフイルコ株式会社
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 荏原インフイルコ株式会社 filed Critical 荏原インフイルコ株式会社
Priority to JP1990036546U priority Critical patent/JPH0647556Y2/en
Publication of JPH03128430U publication Critical patent/JPH03128430U/ja
Application granted granted Critical
Publication of JPH0647556Y2 publication Critical patent/JPH0647556Y2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Treatment Of Water By Ion Exchange (AREA)

Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案は、純水装置,復水脱塩装置等に使用され、内部
にイオン交換樹脂を充填したイオン交換樹脂塔、特に樹
脂層内で再生廃液を集液しかつ逆洗水を分散する改良さ
れた中間集配水機構を備えたイオン交換樹脂塔に関する
ものである。
[Detailed Description of the Invention] [Industrial field of application] The present invention is used for a deionizer, a condensate demineralizer, etc., and is used in an ion exchange resin tower filled with an ion exchange resin, especially in a resin layer. The present invention relates to an ion exchange resin tower equipped with an improved intermediate water collection / distribution mechanism for collecting reclaimed waste liquid and dispersing backwash water.

〔従来の技術〕 イオン交換樹脂塔としては、再生効率のよい下向流通水
・上向流再生方式の向流式イオン交換樹脂塔が多く採用
されるようになってきた。
[Prior Art] As the ion-exchange resin tower, a counter-current type ion-exchange resin tower having a downward flow water / upflow regeneration method with good regeneration efficiency has been widely adopted.

このような向流式イオン交換樹脂塔は、第4図に示すよ
うに、塔11内に樹脂層12が形成され、樹脂層12内の上部
に中間集配水機構13が埋設され、塔11内上部に上部集配
水機構14が、また塔11内下部に下部集配水機構15が配備
されており、通水時には、上部集配水機構14から供給さ
れた原水は樹脂層12を下向流で流過して下部集配水機構
15を経て外部へ流出する。
In such a countercurrent type ion exchange resin tower, as shown in FIG. 4, a resin layer 12 is formed in the tower 11, an intermediate water collecting and distributing mechanism 13 is embedded in the upper portion of the resin layer 12, and An upper water collecting / distributing mechanism 14 is installed in the upper part, and a lower water collecting / distributing mechanism 15 is installed in the lower part of the tower 11.When water flows, the raw water supplied from the upper water collecting / distributing mechanism 14 flows downward in the resin layer 12. Lower water collection and distribution mechanism
It flows to the outside through 15.

また、再生時には、まず中間集配水機構13から逆洗水を
流入させ上部集配水機構14から洗浄排水を流出し、樹脂
層12のそれより上層の目づまりの激しい部分の逆洗を行
ったのち、下部集配水機構15から再生剤を流入させ、ま
た必要に応じて樹脂層12の上方からも再生剤を流入さ
せ、樹脂層12の再生を行ったのち再生廃液は中間集配水
機構13で集液されて外部へ流出する。
Further, at the time of regeneration, first, backwash water is made to flow in from the intermediate water collection and distribution mechanism 13 and washing wastewater is made to flow out from the upper water collection and distribution mechanism 14, and after backwashing the portion of the resin layer 12 above which there is severe clogging, The regenerant is introduced from the lower water collecting / distributing mechanism 15 and also from above the resin layer 12 if necessary, and after the resin layer 12 is regenerated, the regenerated waste liquid is collected by the intermediate water collecting / distributing mechanism 13. It is done and flows out.

ところで、従来の中間集配水機構13は、第5図及び第6
図に示すように、塔11内の樹脂層12内の上部にコレクタ
本管16及びコレクタ本管16から分岐されてイオン交換樹
脂の流出防止のためにサランネット,金網,ウエッジワ
イヤスクリーン等を巻きつけた複数の多孔管式のコレク
タ枝管17で構成されていた。18はコレクタ本管16のサポ
ート部、19はコレクタ枝管17のサポート部を示す。
By the way, the conventional intermediate water collecting and distributing mechanism 13 is shown in FIGS.
As shown in the figure, the upper part of the resin layer 12 in the tower 11 is wrapped with a collector main pipe 16 and a salan net, a wire net, a wedge wire screen, etc. branched from the collector main pipe 16 to prevent the outflow of the ion exchange resin. It was composed of a plurality of perforated pipe-type collector branches 17 attached. Reference numeral 18 denotes a support portion of the collector main pipe 16, and 19 denotes a support portion of the collector branch pipe 17.

〔考案が解決しようとする課題〕[Problems to be solved by the device]

しかしながら、前記従来の向流式イオン交換樹脂塔の中
間集配水機構13は、樹脂層12中に埋設されているため
に、下向流通水中に原水中の濁質等が樹脂層12の表層付
近で捕捉され、通水差圧が上昇し、樹脂が圧密されて中
間集配水機構13に上部から過大な力が加わることにな
る。
However, since the intermediate water collection and distribution mechanism 13 of the conventional countercurrent ion exchange resin tower is buried in the resin layer 12, turbidity in the raw water in the downward flowing water is near the surface layer of the resin layer 12. The water flow differential pressure rises, the resin is consolidated, and an excessive force is applied to the intermediate water collecting and distributing mechanism 13 from above.

このために、 コレクタ本管16、コレクタ枝管17、各種サポート部1
8,19を補強する必要があり、 通水速度をある一定値以下とし、 上部からの力を低減するために上部の樹脂層を厚くす
る、 等の制約が生じ、さらに、 樹脂層中に埋設されたコレクタ本管16、コレクタ枝管
17、サポート部18,19の全投影面積が、塔断面積の約30
%程度にも達しているために、下向流通水中に樹脂層12
中を流れる液体の流れが乱されることが多い、 という欠点も生じていた。
For this purpose, the collector main pipe 16, collector branch pipe 17, various support parts 1
It is necessary to reinforce 8, 19 and make the water flow rate below a certain value, thicken the upper resin layer to reduce the force from the upper part, etc., and further embed it in the resin layer. Collector main pipe 16, collector branch pipe
17, the total projected area of the support parts 18, 19 is about 30
%, So the resin layer 12
There was also the drawback that the flow of liquid inside was often disturbed.

本考案は、樹脂が圧密されても中間集配水機構に過大な
力がかかることなく、樹脂層中の液体の流れを均一に保
ち、前記従来の制約,欠点などを解決することができる
イオン交換樹脂塔を提供することを目的とするものであ
る。
The present invention is an ion exchange that can keep the flow of liquid in the resin layer uniform without applying excessive force to the intermediate water collection and distribution mechanism even if the resin is compacted, and can solve the above-mentioned conventional restrictions and drawbacks. It is intended to provide a resin tower.

〔課題を解決するための手段〕[Means for Solving the Problems]

本考案は、樹脂層内の上部で集・配水する中間集配水機
構を塔内に配備したイオン交換樹脂塔において、前記中
間集配水機構として、コレクタ本管を樹脂層表面より上
方に設け、該コレクタ本管から先端部にストレーナを付
設した複数の分岐管を樹脂層内に垂下して構成したこと
を特徴とするイオン交換樹脂塔である。
The present invention is an ion-exchange resin tower in which an intermediate water collecting and distributing mechanism for collecting and distributing water in the upper part of the resin layer is provided in the tower, and the collector main pipe is provided above the resin layer surface as the intermediate water collecting and distributing mechanism. The ion exchange resin tower is characterized in that a plurality of branch pipes, each having a strainer attached to a tip portion thereof, are suspended from a collector main pipe into a resin layer.

〔作用〕[Action]

上記構成になる本考案においては、樹脂層中に埋まると
ころはコレクタ枝管の先端部のみで、しかも塔内の流れ
方向に平行に埋まっており、サポート部も樹脂層より上
方に設けることができ、樹脂層中の埋設部の投影面積
は、コレクタ枝管又はストレーナの断面積のみで、塔断
面積の約2%程度ですませることもできる。従って、通
水中に樹脂が圧密されても、コレクタ枝管やストレーナ
等に過大な力が加わることなく、通水速度を大きくする
ことができ、ストレーナ上部の樹脂層を厚くする必要な
く、さらに樹脂層中の流れを乱す可能性が少なく、樹脂
層中で均一な流れを得ることができる。
In the present invention having the above-mentioned structure, only the tip of the collector branch pipe is buried in the resin layer, and further, it is buried in parallel with the flow direction in the tower, and the support portion can be provided above the resin layer. The projected area of the buried portion in the resin layer can be about 2% of the tower cross-sectional area only by the cross-sectional area of the collector branch pipe or strainer. Therefore, even if the resin is consolidated in the water flow, the water flow rate can be increased without applying an excessive force to the collector branch pipe or strainer, and it is not necessary to thicken the resin layer above the strainer. There is little possibility of disturbing the flow in the layer, and a uniform flow can be obtained in the resin layer.

なお、樹脂層の再生時には、コレクタ本管からコレクタ
枝管,ストレーナを経て逆洗水を樹脂層内に分散し、ま
た再生廃液はストレーナで集液されコレクタ枝管,コレ
クタ本管から流出するもので、前記従来の中間集配水機
構と同様に行われる。
When regenerating the resin layer, the backwash water is dispersed from the collector main pipe through the collector branch pipe and strainer into the resin layer, and the regenerated waste liquid is collected by the strainer and flows out from the collector branch pipe and collector main pipe. Then, it is performed in the same manner as the above-mentioned conventional intermediate water collecting and distributing mechanism.

〔実施例〕〔Example〕

本考案の一実施例を図面を参照しつつ説明すれば、第1
図〜第3図において、塔1内の樹脂層2の表面より上方
部にはコレクタ本管3が水平に設けられ、このコレクタ
本管3から分岐された複数のコレクタ枝管4が垂直に下
向きに曲げられ、樹脂層2内上部にまで延長され、各コ
レクタ枝管4の先端部にストレーナ5が付設されてい
る。
An embodiment of the present invention will be described with reference to the drawings.
In FIGS. 3 to 3, a collector main pipe 3 is horizontally provided above the surface of the resin layer 2 in the tower 1, and a plurality of collector branch pipes 4 branched from the collector main pipe 3 are vertically downward. Strainer 5 is attached to the tip of each collector branch pipe 4 by being bent to the inside of the resin layer 2.

ストレーナ5は、樹脂の通過を防ぎ液体のみを通過させ
る多孔性のもので、円柱形又は角柱形とし、撮影面積が
小さく、上方からの力がかかりにくい形状にすることが
好ましい。
The strainer 5 is a porous material that prevents the passage of resin and allows only the liquid to pass, and it is preferable that the strainer 5 has a columnar shape or a prismatic shape, has a small imaging area, and is hard to receive a force from above.

6は、コレクタ本管3のサポート部、7は樹脂層2の上
方部でコレクタ枝管4を支持するサポート部である。
6 is a support part of the collector main pipe 3, and 7 is a support part which supports the collector branch pipe 4 above the resin layer 2.

このように、コレクタ枝管4及びストレーナ5のみが樹
脂層2中に塔内の流れ方向に平行な垂直方向に挿入され
ているから、通水時の樹脂圧密による力がかかりにくい
構造となっており、また中間集配水機構の機能としては
従来と変わるところがない。
Thus, since only the collector branch pipe 4 and the strainer 5 are inserted into the resin layer 2 in the vertical direction parallel to the flow direction in the tower, the structure is less likely to receive the force due to the resin consolidation during water passage. In addition, the function of the intermediate water collection and distribution mechanism is no different from the conventional one.

〔考案の効果〕[Effect of device]

以上述べたように本考案によれば、投影面積が小さいた
めに、従来のようにコレクタ管上部の樹脂層を厚くした
り、各種補強を強化する必要がなく、樹脂量も低減さ
れ、コンパクトは構造になり、通水速度を大にすること
が可能になり、さらに集配水機構の樹脂層内での通水時
の流れの乱れが少なく、全樹脂層で均一な流れを得るこ
とができる等の多くの極めて有用な効果を奏するもので
ある。
As described above, according to the present invention, since the projected area is small, it is not necessary to thicken the resin layer on the upper part of the collector tube and strengthen various reinforcements as in the conventional case, the amount of resin is reduced, and the compact size is reduced. The structure makes it possible to increase the water flow rate. Furthermore, there is little turbulence in the flow of water in the resin layer of the water collection and distribution mechanism, and a uniform flow can be obtained in all resin layers. It has many extremely useful effects.

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

第1図は本考案の一実施例を示す縦断面図、第2図は第
1図のI−I線断面図、第3図は第1図の部分的拡大説
明図で、第4図は従来の向流式イオン交換樹脂塔の説明
図、第5図は従来例を示す縦断面図、第6図は第5図の
II−II線断面図である。 1,11……塔、2,12……樹脂層、3,16……コレクタ本管、
4,17……コレクタ枝管、5……ストレーナ、6,7,18,19
……サポート部、 13……中間集配水機構、14……上部集配水機構、 15……下部集配水機構。
1 is a longitudinal sectional view showing an embodiment of the present invention, FIG. 2 is a sectional view taken along the line I--I of FIG. 1, FIG. 3 is a partially enlarged explanatory view of FIG. 1, and FIG. FIG. 5 is an explanatory view of a conventional countercurrent type ion exchange resin tower, FIG. 5 is a longitudinal sectional view showing a conventional example, and FIG.
FIG. 11 is a sectional view taken along line II-II. 1,11 …… Tower, 2,12 …… Resin layer, 3,16 …… Collector main,
4,17 …… Collector branch pipe, 5 …… Strainer, 6,7,18,19
…… Support section, 13 …… Intermediate water collection and distribution mechanism, 14 …… Upper water collection and distribution mechanism, 15 …… Lower water collection and distribution mechanism.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】樹脂層内の上部で集・配水する中間集配水
機構を塔内に配備したイオン交換樹脂塔において、前記
中間集配水機構として、コレクタ本管を樹脂層表面より
上方に設け、該コレクタ本管から先端部にストレーナを
付設した複数の分岐管を樹脂層内に垂下して構成したこ
とを特徴とするイオン交換樹脂塔。
1. An ion exchange resin tower in which an intermediate water collecting and distributing mechanism for collecting and distributing water in an upper portion of the resin layer is provided in the tower, and a collector main pipe is provided above the resin layer surface as the intermediate water collecting and distributing mechanism. An ion-exchange resin tower, characterized in that a plurality of branch pipes having a strainer attached to the tip end thereof are suspended from the collector main pipe into a resin layer.
JP1990036546U 1990-04-06 1990-04-06 Ion exchange resin tower Expired - Lifetime JPH0647556Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1990036546U JPH0647556Y2 (en) 1990-04-06 1990-04-06 Ion exchange resin tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1990036546U JPH0647556Y2 (en) 1990-04-06 1990-04-06 Ion exchange resin tower

Publications (2)

Publication Number Publication Date
JPH03128430U JPH03128430U (en) 1991-12-25
JPH0647556Y2 true JPH0647556Y2 (en) 1994-12-07

Family

ID=31542872

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1990036546U Expired - Lifetime JPH0647556Y2 (en) 1990-04-06 1990-04-06 Ion exchange resin tower

Country Status (1)

Country Link
JP (1) JPH0647556Y2 (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS542916A (en) * 1977-06-09 1979-01-10 Kawasaki Steel Co Method of feeding materials onto molten steel having flux layer in interfacial surface
JPS558805A (en) * 1978-07-03 1980-01-22 Japan Organo Co Ltd Regeneration of ineffective ion exchange resin
JPS5725257A (en) * 1980-07-24 1982-02-10 Nippon Kokan Kk <Nkk> Horizontal continuous casting device

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS542916A (en) * 1977-06-09 1979-01-10 Kawasaki Steel Co Method of feeding materials onto molten steel having flux layer in interfacial surface
JPS558805A (en) * 1978-07-03 1980-01-22 Japan Organo Co Ltd Regeneration of ineffective ion exchange resin
JPS5725257A (en) * 1980-07-24 1982-02-10 Nippon Kokan Kk <Nkk> Horizontal continuous casting device

Also Published As

Publication number Publication date
JPH03128430U (en) 1991-12-25

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