JPS5876117A - Precoated filtering type water treating system - Google Patents
Precoated filtering type water treating systemInfo
- Publication number
- JPS5876117A JPS5876117A JP56172740A JP17274081A JPS5876117A JP S5876117 A JPS5876117 A JP S5876117A JP 56172740 A JP56172740 A JP 56172740A JP 17274081 A JP17274081 A JP 17274081A JP S5876117 A JPS5876117 A JP S5876117A
- Authority
- JP
- Japan
- Prior art keywords
- water
- precoating
- filter aid
- slurry
- filtering
- 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
Landscapes
- Filtration Of Liquid (AREA)
Abstract
Description
【発明の詳細な説明】
本発明はグリコ−)濾過式水処理システムに係シ、特に
原子力発電所の復水浄化に使用するに好適なプリコート
濾過式水処理システムに関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a glycofiltration type water treatment system, and more particularly to a precoated filtration type water treatment system suitable for use in condensate purification at a nuclear power plant.
従来の原子力発電所の復水浄化システムの代表的な一例
を第1図に示す。原子P1で発生した蒸気2は蒸気ター
ビン3を回転させ発電を行った後。Figure 1 shows a typical example of a conventional condensate purification system for a nuclear power plant. After the steam 2 generated by the atom P1 rotates the steam turbine 3 and generates electricity.
復水器4により復水5に々る。復水中には固形状やイオ
ン状の不純物(鉄が主体である。)が含まれており、発
電所の安全性、信頼性向上のためにこれらを除去する必
要がある。濾過脱塩器6及び脱塩器7は不純物を除去す
る装置で、濾過脱塩器6i粉状のイオン交換樹脂を複数
の円筒状のエレメントにプリコートして特に固形物を濾
過する。Condensate water is supplied to condensate 5 by condenser 4. Condensate contains solid and ionic impurities (mainly iron), which must be removed to improve the safety and reliability of power plants. The filtration demineralizer 6 and the demineralizer 7 are devices for removing impurities, and in the filtration demineralizer 6i, a plurality of cylindrical elements are precoated with powdered ion exchange resin to particularly filter solid matter.
又、脱塩器7は粒状のイオン交換樹脂を充填したもので
イオン状の不純物の除去を目的とする。このシステムに
おいて現在問題となっているのは濾過脱塩器6の濾過助
剤即ち、粉状のイオン交換樹脂の寿命が短いことである
。濾過寿命が短いために濾過助剤の廃棄物が大量に発生
し、しかも放射性物質を含んでいるためその処理、処分
に苦慮している。対策としては大別して2つあり、1つ
は濾過寿命の増大法の開発、もう1つは濾過助剤の再利
用が考えられる。濾過助剤の長寿命化に関して効果的な
長寿命濾過方式を考案する。長寿命濾過方式とは、第2
図に示すように採水中に再度プリコート操作を行なうも
のであシ、これにより内部濾過時間(運転初期の濾過差
圧ΔPの上昇速度が緩やかな部分)が長ズなり濾過寿命
が増大する効果がある。The demineralizer 7 is filled with granular ion exchange resin and is intended to remove ionic impurities. A current problem in this system is that the filter aid in the filtration demineralizer 6, that is, the powdered ion exchange resin has a short lifespan. Due to the short filtration life, a large amount of filter aid waste is generated, and since it contains radioactive materials, it is difficult to process and dispose of it. There are two main countermeasures: one is the development of a method to extend the life of the filtration, and the other is the reuse of filter aids. To devise an effective long-life filtration method for extending the life of filter aids. The long-life filtration method is the second
As shown in the figure, the pre-coat operation is performed again during water sampling, which lengthens the internal filtration time (the portion where the filtration differential pressure ΔP rises slowly at the beginning of operation) and has the effect of increasing the filtration life. be.
本発明の目的は、長寿命濾過方式を利用し、良好な復水
浄化を行ない得るグリコ−IJ’過式水式水処理システ
ム供するにある。An object of the present invention is to provide a Glyco-IJ' filtration type water treatment system that utilizes a long-life filtration system and can perform good condensate purification.
われわれが開発した長寿命化方式を採用するために、従
来のプリコー)濾過式水処理システムにプリコートタン
ク及びプリコートポンプを一組付加する解決策を案出し
た。In order to adopt the long-life method that we have developed, we devised a solution by adding a pre-coat tank and a pre-coat pump to the conventional Precor filtration water treatment system.
第3図をもとに本発明の一実施例を説明する。An embodiment of the present invention will be described based on FIG.
濾過助剤はプリコートタンク8内で攪拌器9で水と混合
され、スラリーになる。スラリーはプリコートポンプ1
1で濾過脱塩器6に送入される。濾過脱塩器6は一般に
複数基あり、それぞれ内部に複数のエレメント13を有
する。濾過脱塩器6に送入されたスラリー中の濾過助剤
はエレメント13の表面に層を形成する。これがプリコ
ート操作である。エレメント13を透過した水はプリコ
ートタンク8とプリコートポンプ11の吸込側へ戻り循
環する。プリコートタンク8内の水がクリヤになるとプ
リコート操作を終了する。プリコート操作は、複数の濾
過脱塩器6についてそれぞれ個別に行なうことが多い。The filter aid is mixed with water in the precoat tank 8 by an agitator 9 to form a slurry. Slurry is precoat pump 1
1 and sent to a filtration demineralizer 6. There are generally a plurality of filtration demineralizers 6, each having a plurality of elements 13 inside. The filter aid in the slurry fed into the filter demineralizer 6 forms a layer on the surface of the element 13. This is the precoat operation. The water that has passed through the element 13 returns to the precoat tank 8 and the suction side of the precoat pump 11 for circulation. When the water in the pre-coating tank 8 becomes clear, the pre-coating operation is completed. The precoat operation is often performed individually for each of the plurality of filtration demineralizers 6.
プリコート操作が終ると復水5を復水ポンプ7によシ濾
過脱塩器6に送−人し、復水浄化を開始する。復水中の
不純物を除去された水は処理水14となり、後段のプロ
セスへ送られる。水の流れの切換えは切換パルプ15で
行なう。When the precoat operation is completed, the condensate 5 is sent to the filtration demineralizer 6 by the condensate pump 7, and condensate purification is started. The water from which impurities in the condensate have been removed becomes treated water 14 and is sent to the subsequent process. The flow of water is switched by a switching pulp 15.
次に、プリコートタンク10において濾過助剤と水を攪
拌器9で混合しスラリーを作成し1、プリコートポンプ
12で復水浄化中の濾過脱塩器6にスラリーを送入する
。この操作によシエレメント13のプリコート層の上に
もう懸濁プリコート層が形成される。Next, in the pre-coat tank 10, the filter aid and water are mixed with the stirrer 9 to create a slurry 1, and the slurry is sent with the pre-coat pump 12 to the filtration demineralizer 6 which is in the process of purifying condensate. By this operation, a suspension precoat layer is formed on the precoat layer of the element 13.
本発明による濾過式水処理システムにより、われわれの
考案した長寿命濾過方式が効果的に利用でき、濾過助剤
の長寿命化がはかれる効果がある。The filtration type water treatment system according to the present invention enables effective use of the long-life filtration method devised by us, and has the effect of extending the life of the filter aid.
本発明によれば、一定の濾過助剤で長時間復水中の不純
物の除去を行なうことができるので、濾過助剤の廃棄物
を減少させる効果がある。従って、濾過助剤の購入費及
び俳棄物の処理、処分費用が低減する。According to the present invention, since impurities in condensate water can be removed for a long time using a certain filter aid, there is an effect of reducing waste of the filter aid. Therefore, the cost of purchasing filter aids and the cost of processing and disposing waste materials are reduced.
第1図は従来の復水浄化システムを示す路線図、第2図
は長寿命濾過方式を説明する図、第3図は6
第1頁の続き
0発 明 者 久保田昌治
日立市幸町3丁目1番1号株式
%式%
東京都千代田区丸の内−丁目5
番1号株式会社日立製作所内
0発 明 者 沼崎誠−
日立市幸町3丁目1番1号株式
%式%Figure 1 is a route map showing a conventional condensate purification system, Figure 2 is a diagram explaining a long-life filtration system, and Figure 3 is a diagram showing a long-life filtration system. 1-1 Stock % formula % Hitachi, Ltd., 5-5 Marunouchi, Chiyoda-ku, Tokyo 0 Inventor Makoto Numazaki - 3-1-1 Saiwaimachi, Hitachi City Stock % formula %
Claims (1)
を特徴とするプリコート濾過式水処理システム。 2、特許請求の範囲第1項において、プリコート式水処
理システムの濾過器のエレメントが微小孔を有する金属
製であることを特徴とするプリコート濾過式水処理シス
テム。[Claims] 1. Precoating is performed separately before and during water sampling. For pre-coating of filter aids in sampled water. A pre-coat filtration water treatment system characterized by the addition of a pre-coat tank and a Glycode pump. 2. The precoat filtration type water treatment system according to claim 1, wherein the filter element of the precoat type water treatment system is made of metal having micropores.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56172740A JPS5876117A (en) | 1981-10-30 | 1981-10-30 | Precoated filtering type water treating system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56172740A JPS5876117A (en) | 1981-10-30 | 1981-10-30 | Precoated filtering type water treating system |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5876117A true JPS5876117A (en) | 1983-05-09 |
Family
ID=15947431
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56172740A Pending JPS5876117A (en) | 1981-10-30 | 1981-10-30 | Precoated filtering type water treating system |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5876117A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60248212A (en) * | 1984-05-23 | 1985-12-07 | Kurita Water Ind Ltd | Removal of impurity from liquid |
FR2804616A1 (en) * | 2000-02-08 | 2001-08-10 | Mitaka Filter Kogyo Kabushiki | FILTERING APPARATUS AND OPENING / CLOSING VALVE FOR THE FILTERING APPARATUS |
-
1981
- 1981-10-30 JP JP56172740A patent/JPS5876117A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60248212A (en) * | 1984-05-23 | 1985-12-07 | Kurita Water Ind Ltd | Removal of impurity from liquid |
FR2804616A1 (en) * | 2000-02-08 | 2001-08-10 | Mitaka Filter Kogyo Kabushiki | FILTERING APPARATUS AND OPENING / CLOSING VALVE FOR THE FILTERING APPARATUS |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6080315A (en) | Process for the partial desalination of water | |
JPS5876117A (en) | Precoated filtering type water treating system | |
RU2686074C1 (en) | Method of processing liquid radioactive wastes | |
PL152603B1 (en) | A method for regenerating fit for repeated use in nuclear power plants boric acid solutions from radioactive wastes and solutions from nuclear power plants | |
JP2001239138A (en) | Device for treating liquid | |
JP3388920B2 (en) | Power plant wastewater treatment method and apparatus | |
JPH10192718A (en) | Resin regenerator for condensate desalter | |
JP3369725B2 (en) | Condensate desalination equipment | |
JPS60175516A (en) | Precoat filtering type condensed water treatment apparatus | |
JP6137972B2 (en) | Method and apparatus for inhibiting corrosion of nuclear reactor structure | |
JP2892811B2 (en) | Ion exchange resin, condensate desalination tower and condensate purification device using this resin | |
SU1264966A1 (en) | Method of regeneration of anion exchanger filters of chemical demineralizing plant | |
JP2694969B2 (en) | Method for cleaning up a power plant having a filtration tower equipped with a hollow fiber module | |
JP2543767B2 (en) | Condensate desalination method | |
JP2003090895A (en) | Method and device for demineralizing condensate | |
KR890004710B1 (en) | Method and apparatus for regeneration of ion-exchange resin in mixed-bed ion-exchanger | |
JPS58119388A (en) | Optimum filter aid of precoat filtering type water treating system | |
JPH0747242A (en) | Non-aid type filter | |
JP2677380B2 (en) | Method for collecting backwash wastewater from condensate demineralizer | |
JPH09308881A (en) | Washing of condensed water desalting apparatus | |
JPH07209489A (en) | Radioactive waste solution disposing device | |
JPH09239362A (en) | Device for supplying makeup water to condenser | |
JPS58161895A (en) | Method and device removing chlorine in radioactive liquid waste | |
JPH09206567A (en) | Method for filtering heater drain in power plant and device therefor | |
JPS62132584A (en) | Condensate desalting tower |