JPH0615029B2 - Water collection device in treatment tower - Google Patents

Water collection device in treatment tower

Info

Publication number
JPH0615029B2
JPH0615029B2 JP62126950A JP12695087A JPH0615029B2 JP H0615029 B2 JPH0615029 B2 JP H0615029B2 JP 62126950 A JP62126950 A JP 62126950A JP 12695087 A JP12695087 A JP 12695087A JP H0615029 B2 JPH0615029 B2 JP H0615029B2
Authority
JP
Japan
Prior art keywords
tower
water
water collecting
ion exchange
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.)
Expired - Lifetime
Application number
JP62126950A
Other languages
Japanese (ja)
Other versions
JPS63291637A (en
Inventor
一行 小山
義和 竹端
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.)
Ebara Corp
Original Assignee
Ebara Infilco Co 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 Ebara Infilco Co Ltd filed Critical Ebara Infilco Co Ltd
Priority to JP62126950A priority Critical patent/JPH0615029B2/en
Publication of JPS63291637A publication Critical patent/JPS63291637A/en
Publication of JPH0615029B2 publication Critical patent/JPH0615029B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J47/00Ion-exchange processes in general; Apparatus therefor
    • B01J47/02Column or bed processes
    • B01J47/022Column or bed processes characterised by the construction of the column or container

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、イオン交換樹脂を充填した脱塩塔、活性炭
等の吸着剤を充填した吸着塔、砂等の瀘材を充填した処
理塔における集水装置に関し、特に、火力発電所、原子
力発電所等における汽水循環系統の水質を適正に維持す
るため設置された脱塩塔に有効なものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to a desalting tower filled with an ion exchange resin, an adsorption tower filled with an adsorbent such as activated carbon, and a treatment tower filled with a filter material such as sand. The water collecting device is particularly effective for a desalting tower installed to appropriately maintain the water quality of a brackish water circulation system in a thermal power plant, a nuclear power plant, or the like.

〔従来の技術〕[Conventional technology]

従来、復水系統に脱塩装置を入れ且つ外部再生を行う脱
塩処理を目的とした復水脱塩装置は既に開示されてい
る。該復水脱塩装置には、陽イオン交換樹脂と陰イオン
交換樹脂を混合して充填し、原水中の陽イオン及び陰イ
オンを除去する脱塩塔即ち混床式イオン交換塔がある。
Conventionally, a condensate demineralizer for the purpose of desalination treatment in which a demineralizer is placed in a condensate system and external regeneration is already disclosed. The condensate demineralizer includes a desalting tower, that is, a mixed bed ion exchange tower, in which a cation exchange resin and an anion exchange resin are mixed and filled to remove cations and anions in raw water.

ところで、従来の混床式イオン交換塔である脱塩塔に
は、底板式集水装置を適用した脱塩塔、角型集水本管を
用い且つ処理水上部取出し式集水装置を適用した脱塩塔
等が開示されている。
By the way, in the conventional desalting tower which is a mixed bed type ion exchange tower, a desalting tower to which a bottom plate type water collecting device is applied, a square water collecting main pipe and a treated water upper extracting type water collecting device are applied. A desalting tower and the like are disclosed.

まず、底板式集水装置を適用した脱塩塔における集水装
置について、第3図及び第4図を参照して概説する。
First, an outline of a water collecting device in a desalination tower to which a bottom plate type water collecting device is applied will be described with reference to FIGS. 3 and 4.

集水装置50は、脱塩塔53の底部に直径方向に伸長し
て配置された集水本管55を有し、該集水本管55の上
方に配置され且つ該集水本管55に連通する多数の集水
枝管52を有している。これらの集水枝管52は、樹脂
用の底板56の上方に近接して配置されている。処理水
流出口58は、脱塩塔53の底部鏡板60に形成されて
いる。また、樹脂流出口54は、底板56の下面で且つ
集水本管55の上板51側方から下方に伸長している。
図中、57は底板56を支持する支柱、59は底板56
の脱塩塔側壁部に付着した樹脂、61は支持土台を示
す。
The water collecting device 50 has a water collecting main pipe 55 extending in the diametrical direction at the bottom of the desalting tower 53, and is arranged above the water collecting main pipe 55 and at the water collecting main pipe 55. It has a large number of water collection branch pipes 52 communicating with each other. These water collecting branch pipes 52 are arranged near and above the bottom plate 56 for resin. The treated water outlet 58 is formed in the bottom end plate 60 of the desalting tower 53. Further, the resin outlet port 54 extends downward from the lower surface of the bottom plate 56 and from the side of the upper plate 51 of the water collecting main pipe 55.
In the figure, 57 is a support column for supporting the bottom plate 56, and 59 is the bottom plate 56.
The resin adhered to the side wall of the desalting tower of No. 1, 61 indicates a support base.

次に、角型集水本管を用い且つ処理水上部取出し式集水
装置を適用した脱塩塔における集水装置について、第5
図及び第6図を参照して概説する。この集水装置70に
ついては、イオン交換樹脂は鏡板75の底部に設けられ
た樹脂流出口74から流出する。集水本管71の上方に
は、処理水流出口78の配管77が配置され、集水本管
71と配管77とは連通している。図中、76は集水枝
管72を支持する集水枝管サポータ、80は脱塩塔73
の支持土台を示す。
Next, regarding a water collecting device in a desalination tower using a rectangular water collecting main pipe and applying a treated water upper discharge type water collecting device,
A general description will be given with reference to FIGS. In the water collecting device 70, the ion exchange resin flows out from the resin outlet 74 provided at the bottom of the end plate 75. A pipe 77 of the treated water outlet 78 is arranged above the water collecting main pipe 71, and the water collecting main pipe 71 and the pipe 77 communicate with each other. In the figure, 76 is a water collecting branch pipe supporter that supports the water collecting branch pipe 72, and 80 is a desalting tower 73.
The support base of is shown.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

しかしながら、上記の底板式集水装置を適用した脱塩塔
における集水装置50については、集水枝管52と底板
56とが近接しており、イオン交換樹脂は有効に利用さ
れるが、イオン交換樹脂を原水の処理に使用してイオン
交換能力のなくなった樹脂を脱塩塔53外に取出す場合
の樹脂移送時には、樹脂は底板56の脱塩塔側壁部付近
に付着し、そこに残留し易い状態が生じる問題点を有し
ていた。
However, in the water collecting device 50 in the desalting tower to which the above-mentioned bottom plate type water collecting device is applied, the water collecting branch pipe 52 and the bottom plate 56 are close to each other, and the ion exchange resin is effectively used, but the ion exchange resin is used. When the resin used for treating raw water is used to remove the resin having no ion exchange ability to the outside of the desalting tower 53, the resin adheres to the vicinity of the side wall of the desalting tower of the bottom plate 56 and easily remains there. There was a problem that the condition occurred.

また、上記の角型集水本管71を用い且つ処理水上部取
出し式集水装置を適用した脱塩塔73における集水装置
70については、イオン交換樹脂は鏡板75の底板の曲
面に沿って下方へ滑り落ちて樹脂流出口74から流出す
るため、脱塩塔73内には、樹脂は残留しないが、しか
しながら、処理水流出用配管77及び処理水流出口78
が集水本管71の上方に位置しているため、脱塩塔73
内に充填されたイオン交換樹脂が有効に利用されず、し
かも脱塩塔73内の処理水は処理水流出口78のレベル
までしか排水することができないという問題点を有して
いた。
Further, regarding the water collecting device 70 in the desalting tower 73 using the above-mentioned rectangular water collecting main pipe 71 and applying the treated water upper discharge type water collecting device, the ion exchange resin is along the curved surface of the bottom plate of the end plate 75. Since the resin slides down and flows out from the resin outlet 74, the resin does not remain in the desalting tower 73. However, the treated water outlet pipe 77 and the treated water outlet 78 are provided.
Is located above the main water collection pipe 71, the desalting tower 73
There is a problem that the ion exchange resin filled in the inside is not effectively used, and the treated water in the desalting tower 73 can be discharged only to the level of the treated water outlet 78.

そこで、この発明の目的は、上記の問題点を解消するこ
とであり、処理塔内から粒状充填物を排出する場合即ち
充填物の移送時に、処理塔内に粒状充填物を残留させる
ことなく、スムースに処理塔から排出できると共に、処
理塔内に充填された粒状物を有効に使用することがで
き、また、処理された処理水を処理塔内に残すことなく
取り出すことができる処理塔における集水装置を提供す
ることである。
Therefore, an object of the present invention is to eliminate the above problems, when discharging the granular packing from the processing tower, that is, when transferring the packing, without leaving the granular packing in the processing tower, It can be smoothly discharged from the treatment tower, the granular material filled in the treatment tower can be effectively used, and the treated water that has been treated can be taken out without being left in the treatment tower. It is to provide a water device.

〔問題点を解決するための手段〕[Means for solving problems]

この発明は、上記の目的を達成するため、次のように構
成されている。即ち、この発明は、処理塔の下部鏡板を
曲面に形成し、前記鏡板の前記曲面の最低部に粒状充填
物流出口を設け、前記処理塔の底部に集水本管を設け、
該集水本管を前記鏡板底部の一部で構成した底板、多数
の集水枝管をそれぞれ取り付けた前記底板から隔置して
立ち上がる一対の側板及び前記各側板に固定した上板か
ら構成し、処理水流出口を前記集水本管を構成する前記
底板に設け、前記粒状充填物出口の上方に貫通路を前記
各側板に跨がって形成したことを特徴とする処理塔にお
ける集水装置に関する。
The present invention is configured as follows to achieve the above object. That is, the present invention, the lower end plate of the treatment tower is formed into a curved surface, a granular packing physical distribution outlet is provided at the lowest part of the curved surface of the end plate, and a water collecting main pipe is provided at the bottom of the processing tower,
The water collecting main is composed of a bottom plate constituted by a part of the bottom part of the end plate, a pair of side plates standing apart from the bottom plate to which a large number of water collecting branch pipes are respectively attached, and an upper plate fixed to each side plate, A treated water outlet is provided in the bottom plate constituting the main water collecting main pipe, and a through passage is formed above the granular packing outlet so as to extend over each of the side plates. .

〔作用〕[Action]

この発明による処理塔における集水装置は、上記のよう
に構成されており、次のように作用する。即ち、この処
理塔における集水装置は、処理塔の下部鏡板を曲面に形
成し、前記鏡板の最底部に粒状充填物流出口を設け、前
記処理塔の底部に集水本管を設け、該集水本管を前記鏡
板底部の一部で構成した底板、多数の集水枝管をそれぞ
れ取り付けた前記底板から隔置して立ち上がる一対の側
板及び前記各側板に固定した上板から構成し、更に処理
水流出口を前記集水本管の前記底板に設けたので、粒状
充填物を前記処理塔内から排出する移送時には、使用済
みの粒状充填物は前記処理塔の下部鏡板の曲面に沿って
下方へ滑り落ち、前記粒状充填物流出口から全てを流出
させることができ、前記処理塔内に残留するようなこと
がない。
The water collecting device in the treatment tower according to the present invention is configured as described above and operates as follows. That is, in the water collecting device in this treatment tower, the lower end plate of the treatment tower is formed into a curved surface, the granular packing physical distribution outlet is provided at the bottom of the end plate, and the water collecting main pipe is provided at the bottom of the treatment tower. The water main pipe is composed of a bottom plate constituted by a part of the bottom part of the end plate, a pair of side plates standing apart from the bottom plate to which a large number of water collecting branch pipes are respectively attached, and an upper plate fixed to each side plate, and further processed. Since the water outlet is provided on the bottom plate of the main water collecting pipe, the used granular packing is moved downward along the curved surface of the lower end plate of the processing tower during transfer for discharging the granular packing from the inside of the processing tower. It is possible to slip off and to make the whole flow out from the granular packed physical distribution outlet, and not to remain in the processing tower.

しかも、前記処理塔内の処理された処理水も前記集水枝
管から前記処理塔の鏡板底部を底板とする前記集水本管
に集められ、前記集水本管を形成する前記底板に形成さ
れた前記処理水流出口から排水される。
Moreover, the treated water that has been treated in the treatment tower is also collected from the water collection branch pipe to the water collection main pipe whose bottom plate is the end plate of the treatment tower, and is formed on the bottom plate forming the water collection main pipe. The treated water is discharged from the outlet.

〔実施例〕〔Example〕

以下、図面を参照して、この発明による一例として処理
塔における集水装置を説明する。
Hereinafter, a water collecting device in a treatment tower will be described as an example according to the present invention with reference to the drawings.

第1図において、この発明による処理塔における集水装
置が符号1で示されている。この集水装置1は、処理塔
である脱塩塔3に適用したものであり、脱塩塔3は、復
水脱塩装置の混床式イオン交換塔であり、原水から水中
に含まれる陽イオン及び陰イオンを除去して処理水にす
るという脱塩処理を行うものであり、脱塩塔3の外部の
再生装置によってイオン交換樹脂の再生を行うものであ
る。
In FIG. 1, the water collecting device in the treatment tower according to the present invention is indicated by reference numeral 1. This water collecting device 1 is applied to a desalting tower 3 which is a treatment tower. The desalting tower 3 is a mixed bed type ion exchange tower of a condensate demineralizing equipment, and it is a positive ion contained in water from raw water. A desalting process of removing ions and anions to obtain treated water is performed, and an ion exchange resin is regenerated by a regeneration device outside the desalting tower 3.

即ち、この復水脱塩装置は、原水を処理するのに使用し
てイオン交換能力がなくなった樹脂を脱塩塔3内で再生
せず、脱塩塔3とは別に設けた再生装置によって全ての
樹脂を再生するものである。
That is, this condensate demineralizer does not regenerate the resin, which has been depleted in ion exchange capacity for treating raw water, in the demineralization tower 3 and uses a regenerator provided separately from the demineralization tower 3 This is to regenerate the resin.

脱塩塔3の上部には、原水を脱塩塔3内に流入する原水
流入口13及びイオン交換樹脂を脱塩塔3内に流入する
イオン交換樹脂流入管14が設けられている。また、脱
塩塔3の上部には、多数の原水流入枝管12を取り付け
た原水流入本管15が適当な支持手段(図示省略)によ
って配置されている。原水流入本管15は原水流入口1
3と連通している。
At the upper part of the desalting tower 3, there are provided a raw water inlet 13 through which raw water flows into the desalting tower 3 and an ion exchange resin inflow pipe 14 through which an ion exchange resin flows into the desalting tower 3. Further, a raw water inflow main pipe 15 to which a large number of raw water inflow branch pipes 12 are attached is arranged at an upper portion of the desalting tower 3 by an appropriate supporting means (not shown). Raw water inflow main 15 is raw water inlet 1
It communicates with 3.

更に、脱塩塔3の下部には、原水を処理した処理水を脱
塩塔3外に排出する処理水流出口8及び使用済みのイオ
ン交換樹脂を脱塩塔3外に排出するイオン交換樹脂流出
口4が設けられている。また、脱塩塔3の下部には、処
理水を集める多数の集水枝管2を取付けた集水本管5が
後述のように構成して設置されている。集水本管5は、
処理水流出口8と導通しており、イオン交換樹脂流出口
4とは非導通状態である。
Further, in the lower part of the desalting tower 3, a treated water outlet 8 for discharging treated water obtained by treating raw water to the outside of the desalting tower 3 and an ion exchange resin stream for discharging used ion exchange resin to the outside of the desalting tower 3. An exit 4 is provided. Further, a water collecting main pipe 5 having a large number of water collecting branch pipes 2 for collecting treated water is installed in the lower part of the desalting tower 3 in a structure as described later. The water main 5 is
It is in conduction with the treated water outlet 8 and is in non-conduction with the ion exchange resin outlet 4.

この発明による脱塩塔における集水装置1は、上記の構
成において、次の点に特徴を有している。
The water collecting device 1 in the desalting tower according to the present invention is characterized by the following points in the above configuration.

即ち、脱塩塔3は、その下部を構成する鏡板10を曲面
に形成し、該鏡板10の最底部にイオン交換樹脂流出口
4を設け、更に処理水流出口8を鏡板10の底部に設け
たことである。
That is, in the desalting tower 3, an end plate 10 constituting the lower part thereof is formed into a curved surface, an ion exchange resin outlet 4 is provided at the bottom of the end plate 10, and a treated water outlet 8 is further provided at the bottom of the end plate 10. That is.

更に、集水本管5については、多数の集水枝管2を取り
付けた集水本管5の底板を鏡板10の底部で構成し、一
対の側板6,6及び各側板6,6に取外し可能に固定さ
れた上板9から構成している。詳しくは、例えば、これ
らの側板6,6は脱塩等3の下部鏡板10に溶接等によ
って直接固着されており、また、側板6,6の上端部に
は上板9がボルト等によって取り外し可能に固着されて
いる。従って、集水本管5自体は、脱塩塔3内に充填さ
れたイオン交換樹脂11に対して遮蔽された状態に構成
されている。
Further, regarding the water collecting main pipe 5, the bottom plate of the water collecting main pipe 5 to which a large number of water collecting branch pipes 2 are attached is constituted by the bottom portion of the end plate 10, and the pair of side plates 6 and 6 and the side plates 6 and 6 can be removed. It is composed of an upper plate 9 fixed to. Specifically, for example, these side plates 6 and 6 are directly fixed to the lower end plate 10 of the deionization unit 3 by welding or the like, and the upper plate 9 can be removed by bolts or the like at the upper ends of the side plates 6 and 6. Is stuck to. Therefore, the water collection main pipe 5 itself is configured to be shielded from the ion exchange resin 11 filled in the desalting tower 3.

また、集水枝管2は各々の側板6,6にほぼ垂直方向の
取外し可能に取り付け、更にイオン交換樹脂流出口4の
位置する上方に側板6,6間に跨がって延びる貫通路7
が形成されている。この貫通路7は、側板6,6間に跨
がって延びる半円筒状の形状に形成され、集水本管5と
は完全に遮蔽即ち非導通状態に構成されており、従っ
て、脱塩塔3に充填されたイオン交換樹脂は集水本管5
内には入り込むことができない状態である。
Further, the water collecting branch pipe 2 is detachably attached to each of the side plates 6 and 6 in a substantially vertical direction, and further, a through passage 7 extending over the side plates 6 and 6 above where the ion exchange resin outlet 4 is located.
Are formed. The through passage 7 is formed in a semi-cylindrical shape extending across the side plates 6 and 6, and is completely shielded from the water collecting main pipe 5, that is, in a non-conducting state. The ion exchange resin filled in the tower 3 is the water collection main pipe 5
It is in a state where it cannot enter inside.

多数の集水枝管2は、ウェッジワイヤスクリーン、又は
イオン交換樹脂が通過しないようにネットを巻き付けた
多孔管等の部材から成り、イオン交換樹脂が通過しない
よう構成されている。それ故に、原水が脱塩等3内に充
填されたイオン交換樹脂層11を通過して処理された処
理水は、集水枝管2を通過できるが、イオン交換樹脂は
集水枝管2内に入り込むことはない。
The multiple water collecting branch pipes 2 are made of a member such as a wedge wire screen or a perforated pipe around which a net is wound so that the ion exchange resin does not pass through, and are configured so that the ion exchange resin does not pass through. Therefore, the treated water treated by passing the raw water through the ion-exchange resin layer 11 filled in the desalination 3 can pass through the water collecting branch pipe 2, but the ion-exchange resin enters the water collecting branch pipe 2. There is no such thing.

この発明による脱塩塔における集水装置1は、上記のよ
うな構成であり、次のように作動する。イオン交換樹脂
が原水の処理に使用されてイオン交換能力の無くなった
時、イオン交換樹脂は、矢印Cで示すように、イオン交
換樹脂流出口4から排出されて再生装置に移送させる。
脱塩塔3からイオン交換樹脂が排出されて空になった
時、脱塩塔3には、新たなイオン交換樹脂、或いは再生
装置で再生されたイオン交換樹脂がイオン交換樹脂流入
管14から矢印Bで示すように流入して充填される。脱
塩塔3内にイオン交換樹脂が充填されてイオン交換樹脂
層11が形成された時、原水は、矢印Aで示すように、
原水流入口13から原水流入本管15、次いで原水流入
枝管12を通って脱塩塔3内に均一に分散して流入され
る。
The water collecting device 1 in the desalting tower according to the present invention is configured as described above and operates as follows. When the ion exchange resin is used for the treatment of raw water and the ion exchange capacity is lost, the ion exchange resin is discharged from the ion exchange resin outlet 4 and transferred to the regenerator as shown by arrow C.
When the ion-exchange resin is discharged from the desalting tower 3 and becomes empty, a new ion-exchange resin or an ion-exchange resin regenerated by a regenerator is fed from the ion-exchange resin inflow pipe 14 to the desalting tower 3 by an arrow. Inflow and fill as shown at B. When the ion exchange resin is filled in the desalting tower 3 to form the ion exchange resin layer 11, the raw water is, as shown by an arrow A,
From the raw water inlet 13, the raw water inflow main pipe 15 and then the raw water inflow branch pipe 12 are uniformly dispersed and flown into the desalination tower 3.

脱塩塔3に流入した原水は、イオン交換樹脂層11を通
過する間に原水中に含まれる陽イオン及び陰イオンはイ
オン交換樹脂とイオン交換される。
While the raw water flowing into the desalting tower 3 passes through the ion exchange resin layer 11, cations and anions contained in the raw water are ion-exchanged with the ion exchange resin.

それによって、イオン交換処理された純水の処理水即ち
脱塩水となった処理水は、脱塩塔3の下部に多数配置さ
れた集水枝管2から集水本管5に導入され、次いで矢印
Dで示すように処理水流出口8から脱塩塔3外に流出さ
れる。
As a result, the treated water of the pure water that has been subjected to the ion exchange treatment, that is, the treated water that has become desalted water, is introduced into the water collecting main pipe 5 from the water collecting branch pipes 2 arranged in large numbers at the lower part of the desalting tower 3, and then the arrow As indicated by D, the treated water flows out from the desalination tower 3 through the outlet 8.

ところで、集水本管5を構成する両側面の側板6,6に
は集水枝管2が直接取り付けられており、しかも側板
6,6に跨がって上板9がボルト等で取り外し可能に密
封状態に固着されているので、処理水は集水技管2内に
流入することはできるが、イオン交換樹脂は集水枝管2
内に流入するようなことはなく、勿論集水本管5に入り
込むようなことは生じない。
By the way, the water collecting branch pipes 2 are directly attached to the side plates 6 and 6 on both sides constituting the water collecting main pipe 5, and the upper plate 9 is detachable by bolts or the like across the side plates 6 and 6. The treated water can flow into the water collection tube 2 because it is fixed in a sealed state, but the ion exchange resin does not collect the treated water.
It does not flow into the inside, and of course does not enter the water collecting main pipe 5.

そこで、原水の通水を続けることによって、イオン交換
樹脂のイオン交換能力が低下した時には、原水の通水を
停止して、例えば、バルブ(図示省略)等を開放し、上
記のように、イオン交換樹脂をイオン交換樹脂流出口4
から排出し、脱塩塔3内から使用済みのイオン交換樹脂
を完全に排出した後に、イオン交換樹脂流入管14から
新たなイオン交換樹脂或いは再生された新しいイオン交
換樹脂を脱塩塔3内に充填する。このような作動を繰り
返すことによって、原水に含まれている陽イオン及び陰
イオンを除去し、即ち脱塩処理し、純水即ち脱塩水を得
る。
Therefore, when the ion exchange capacity of the ion exchange resin is reduced by continuing the flow of raw water, the flow of raw water is stopped and, for example, a valve (not shown) is opened, and as described above, Replace the exchange resin with the ion exchange resin outlet 4
The ion exchange resin used in the desalting tower 3 is completely discharged, and then a new ion exchange resin or a regenerated new ion exchange resin is introduced into the desalting tower 3 from the ion exchange resin inflow pipe 14. Fill. By repeating such an operation, the cations and anions contained in the raw water are removed, that is, desalting treatment is performed to obtain pure water, that is, desalted water.

一般に、このサイクルにおいて最大の障害となるのが、
イオン交換樹脂の排出の時に、イオン交換能力が無くな
った樹脂が脱塩塔内に残留して処理水水質、即ち処理し
た水のpH、酸消費量、電気伝導率等、或いは全蒸発残
留物等によって表される特性を悪化させることである
が、この発明による脱塩塔における集水装置1を使用す
れば、イオン交換樹脂そのものをイオン交換能力のある
もののみに極めて容易に管理できるので、処理水水質を
常に正常に且つ均質に保つことができる。また、この処
理塔における集水装置は、脱塩塔以外に吸着塔、濾過塔
にも適用できる。
Generally, the biggest obstacle in this cycle is
When the ion-exchange resin is discharged, the resin whose ion-exchange capacity is lost remains in the desalting tower and the quality of treated water, that is, pH of treated water, acid consumption, electric conductivity, etc., or total evaporation residue, etc. However, if the water collecting device 1 in the desalting tower according to the present invention is used, it is possible to manage the ion exchange resin itself only to have ion exchange capacity. Water quality can always be kept normal and homogeneous. Further, the water collecting device in this treatment tower can be applied to an adsorption tower and a filtration tower in addition to the desalting tower.

〔発明の効果〕〔The invention's effect〕

この発明による処理塔における集水装置は、上記のよう
に構成されており、次のような効果を有する。即ち、こ
の処理塔における集水装置は、処理塔の下部鏡板を曲面
に形成し、前記鏡板の最低部に粒状充填物流出口を設
け、多数の集水枝管を取り付けた集水本管の底板を前記
鏡板の底部で構成し、更に処理水流出口を前記集水本管
の前記底板に設けたので、使用済みの粒状充填物の移送
時には、粒状充填物は前記処理塔の下部鏡板を曲面に沿
って下方へ滑り落ち、前記貫通路を通り、前記粒状充填
物流出口から前記処理塔外に全て流出させることができ
る。
The water collecting device in the treatment tower according to the present invention is configured as described above and has the following effects. That is, in the water collecting device in this treatment tower, the lower end plate of the treatment tower is formed into a curved surface, the granular packing physical distribution outlet is provided at the lowest part of the end plate, and the bottom plate of the main water collecting pipe with a large number of water collecting branch pipes is attached. Since the bottom end of the end plate is formed, and the treated water outlet is provided on the bottom plate of the water collecting main pipe, when the used granular packing is transferred, the granular packing is provided along the curved lower end plate of the processing tower. And then slides downward, passes through the through passage, and all flows out of the processing tower from the granular packed physical distribution outlet.

それ故に、粒状充填物を前記処理塔内に残留させるよう
なことがなく、また前記処理塔内に充填された粒状物を
有効に使用することができる。
Therefore, the granular packing does not remain in the processing tower, and the granular material packed in the processing tower can be effectively used.

また、この発明による処理塔における集水装置は、採水
時には、前記処理塔内に充填された粒状充填物内に原水
の流れを乱す流出管が存在しない構造であるので、前記
処理塔内の粒状物層が極めて有効に利用される。また、
前記処理塔内の水も前記集水枝管のフィルタから前記処
理塔の底部を底板とする前記集水本管に集められ、前記
底板に形成された前記処理水流出口から排水される。
Further, the water collecting device in the treatment tower according to the present invention has a structure in which there is no outflow pipe for disturbing the flow of raw water in the granular packing filled in the treatment tower at the time of water collection. The granular material layer is used very effectively. Also,
Water in the treatment tower is also collected from the filter of the water collecting branch pipe to the water collecting main pipe having the bottom portion of the treatment tower as a bottom plate, and is discharged from the treated water outlet formed in the bottom plate.

従って、この発明による処理塔における集水装置を使用
すれば、処理水水質を常に正常に且つ均質に保つことが
でき、処理水水質が常に安定しているので、処理水に対
する信頼度が極めて高いものとなる。
Therefore, by using the water collecting device in the treatment tower according to the present invention, the treated water quality can always be kept normal and uniform, and the treated water quality is always stable, so that the reliability of the treated water is extremely high. Will be things.

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

第1図はこの発明による処理塔における集水装置の一実
施例を示す断面図、第2図は第1図の線II−IIにおける
断面図、第3図は従来の脱塩塔における集水装置の一例
を示す断面図、第4図は第3図の線IV−IVにおける一部
断面図、第5図は従来の脱塩塔における集水装置の別の
例を示す断面図、及び第6図は第5図の線VI−VIにおけ
る一部断面図である。 1……脱塩塔における集水装置、2……集水枝管、3…
…脱塩塔、4……イオン交換樹脂流出口、5……集水本
管、6……側板、7……貫通路、8……処理水流出口、
9……上板、10……鏡板、11……イオン交換樹脂
層、12……原水流入枝管、13……原水流入口、14
……イオン交換樹脂流入管、15……原水流入本管。
FIG. 1 is a sectional view showing an embodiment of a water collecting device in a treatment tower according to the present invention, FIG. 2 is a sectional view taken along line II-II in FIG. 1, and FIG. 3 is water collecting in a conventional desalting tower. Sectional drawing which shows an example of an apparatus, FIG. 4 is a partial sectional view in the line IV-IV of FIG. 3, FIG. 5 is a sectional view which shows another example of the water collecting apparatus in the conventional desalination tower, and FIG. FIG. 6 is a partial sectional view taken along line VI-VI in FIG. 1 ... Water collecting device in desalting tower, 2 ... Water collecting branch pipe, 3 ...
… Desalination tower, 4 …… Ion exchange resin outlet, 5 …… Water collecting main pipe, 6 …… Side plate, 7 …… Through passage, 8 …… Treatment water outlet,
9 ... Upper plate, 10 ... End plate, 11 ... Ion exchange resin layer, 12 ... Raw water inflow branch pipe, 13 ... Raw water inlet, 14
…… Ion exchange resin inflow pipe, 15 …… Raw water inflow main pipe.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】処理塔の下部鏡板を曲面に形成し、前記鏡
板の前記曲面の最底部に粒状充填物流出口を設け、前記
処理塔の底部に集水本管を設け、該集水本管を前記鏡板
底部の一部で構成した底板、多数の集水枝管をそれぞれ
取り付けた前記底板から隔置して立ち上がる一対の側板
及び前記各側板に固定した上板から構成し、処理水流出
口を前記集水本管を構成する前記底板に設け、前記粒状
充填物流出口の上方に貫通路を前記各側板に跨がって形
成したことを特徴とする処理塔における集水装置。
1. A lower end plate of a treatment tower is formed into a curved surface, a granular packing physical distribution outlet is provided at the bottom of the curved surface of the end plate, and a water collecting main pipe is provided at the bottom of the processing tower. A bottom plate constituted by a part of the bottom part of the end plate, a pair of side plates standing apart from the bottom plate to which a large number of water collecting branch pipes are respectively attached, and an upper plate fixed to each side plate, and a treated water outlet is A water collecting device in a treatment tower, wherein the water collecting main is provided on the bottom plate, and a through passage is formed above the granular packed physical distribution outlet so as to extend over the side plates.
JP62126950A 1987-05-26 1987-05-26 Water collection device in treatment tower Expired - Lifetime JPH0615029B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62126950A JPH0615029B2 (en) 1987-05-26 1987-05-26 Water collection device in treatment tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62126950A JPH0615029B2 (en) 1987-05-26 1987-05-26 Water collection device in treatment tower

Publications (2)

Publication Number Publication Date
JPS63291637A JPS63291637A (en) 1988-11-29
JPH0615029B2 true JPH0615029B2 (en) 1994-03-02

Family

ID=14947907

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62126950A Expired - Lifetime JPH0615029B2 (en) 1987-05-26 1987-05-26 Water collection device in treatment tower

Country Status (1)

Country Link
JP (1) JPH0615029B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104353505B (en) * 2014-11-21 2017-04-05 青海盐湖工业股份有限公司 Large ion switch
JP2017217594A (en) * 2016-06-06 2017-12-14 株式会社ディスコ Ion exchange unit and method for replacing ion exchange resin

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5425272A (en) * 1977-07-28 1979-02-26 Japan Organo Co Ltd Single column vertical floor type ion exchange apparatus
JPS6144293U (en) * 1984-08-29 1986-03-24 オルガノ株式会社 Water tower of condensate desalination equipment

Also Published As

Publication number Publication date
JPS63291637A (en) 1988-11-29

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