JPS6231631B2 - - Google Patents

Info

Publication number
JPS6231631B2
JPS6231631B2 JP55146869A JP14686980A JPS6231631B2 JP S6231631 B2 JPS6231631 B2 JP S6231631B2 JP 55146869 A JP55146869 A JP 55146869A JP 14686980 A JP14686980 A JP 14686980A JP S6231631 B2 JPS6231631 B2 JP S6231631B2
Authority
JP
Japan
Prior art keywords
seawater
removal device
biological removal
filter
filter box
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
Application number
JP55146869A
Other languages
Japanese (ja)
Other versions
JPS5771691A (en
Inventor
Daisuke Kobayashi
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.)
Toshiba Corp
Original Assignee
Tokyo Shibaura Electric 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 Tokyo Shibaura Electric Co Ltd filed Critical Tokyo Shibaura Electric Co Ltd
Priority to JP55146869A priority Critical patent/JPS5771691A/en
Publication of JPS5771691A publication Critical patent/JPS5771691A/en
Publication of JPS6231631B2 publication Critical patent/JPS6231631B2/ja
Granted legal-status Critical Current

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  • Water Treatment By Electricity Or Magnetism (AREA)
  • Filtration Of Liquid (AREA)
  • Treatment Of Water By Ion Exchange (AREA)

Description

【発明の詳細な説明】 本発明は海水使用プラントにおいて、熱交換あ
るいは冷却用等の海水経路に使用される生物除去
装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a biological removal device used in a seawater path for heat exchange or cooling in a seawater-using plant.

従来、原子力発電所、化学プラントあるいは火
力発電所においては、所内で発生する種々の熱除
去やそこで使用する真水等の冷却のためあるいは
海水中の塩素等の化学物質を取り出すために海水
を循環水ポンプあるいは海水ポンプにより取水口
より取り入れ、海水配管を介して復水器や熱交換
器あるいは化学物質取出装置へ送り込むことが行
なわれている。
Conventionally, in nuclear power plants, chemical plants, and thermal power plants, seawater is circulated to remove various types of heat generated within the plant, to cool the fresh water used there, or to extract chemicals such as chlorine from seawater. Water is taken in from a water intake using a pump or a seawater pump, and sent to a condenser, heat exchanger, or chemical substance extraction device via seawater piping.

この場合、海水の循環経路の途中にはスクリー
ンやメツシユフイルタもしくはボール洗浄装置等
のフイルタが設けられて、魚類や他の生物の浸入
が防止されている。
In this case, a filter such as a screen, mesh filter, or ball cleaning device is provided along the seawater circulation path to prevent fish and other living things from entering.

しかしながら前記の方法ではスクリーンやメツ
シユフイルタにて除去されない大きさの貝殻や生
物が配管内や熱交換器内等へ流入付着し金属劣化
や腐蝕の原因となり、又スクリーンやメツシユフ
イルタの穴サイズを小さくして圧損を増大させ、
海水ポンプの容量アツプを強いられるという欠点
を有していた。
However, with the above method, shells and organisms that are too large to be removed by the screen or mesh filter may enter the pipes or heat exchanger, causing metal deterioration or corrosion. increases pressure loss,
This had the disadvantage that the capacity of the seawater pump had to be increased.

本発明は、前記事情に鑑みなされたもので、そ
の目的は電流により海水中の生物を死滅させ、こ
れを除去することにより生物の配管内や熱交換器
内等への付着による金属劣化や腐蝕を防止してそ
の寿命を延ばすとともに、海水ポンプの過負荷防
止及び復水器、熱交換器等の効率向上および点検
時の安全性向上を図つた生物除去装置を提供する
ことにある。上記目的は、海水使用プラントにお
ける海水入口側経路に設けられた生物除去装置に
おいて、前記経路へ海水流入方向に沿つてクシ形
スクリーンと、外部電源に接続された格子形電極
と、フイルタボツクスとを順に配置する生物除去
装置により達成される。
The present invention was developed in view of the above circumstances, and its purpose is to kill living things in seawater using electric current, and by removing them, metal deterioration and corrosion caused by living things adhering to pipes, heat exchangers, etc. It is an object of the present invention to provide a biological removal device that prevents overloading of seawater pumps, increases the efficiency of condensers, heat exchangers, etc., and improves safety during inspections. The above object is to provide a biological removal device installed in a seawater inlet route in a seawater-using plant, which includes a comb-shaped screen, a grid-shaped electrode connected to an external power supply, and a filter box along the direction of seawater inflow into the route. This is achieved by biological removal devices arranged in sequence.

以下図面を用いて本発明の一実施例を説明す
る。
An embodiment of the present invention will be described below with reference to the drawings.

第1図は海水使用プラントにおける熱交換系統
図、第2図は本発明の一実施例の斜視図をそれぞ
れ示している。
FIG. 1 shows a heat exchange system diagram in a seawater-using plant, and FIG. 2 shows a perspective view of an embodiment of the present invention.

第1図に示す熱交換系統は、海水を取り入れる
取水口1と、取水した海水を移送する海水ポンプ
2と、海水配管3と、熱交換器4と、排水用ポン
プ5と放出口6及び前記取水口1に取り付けられ
た生物除去装置7等によつて構成されている。
The heat exchange system shown in FIG. 1 includes a water intake 1 that takes in seawater, a seawater pump 2 that transfers the taken seawater, a seawater pipe 3, a heat exchanger 4, a drainage pump 5, a discharge port 6, and the It is composed of a biological removal device 7 and the like attached to the water intake 1.

前記生物除去装置7は第2図に示すように全体
として箱状を成しており、その内部にはクシ形ス
クリーン8、格子形銅板電極9及びフイルタボツ
クス10,11が順次配置されている。
As shown in FIG. 2, the organism removal device 7 has a box shape as a whole, and a comb-shaped screen 8, a lattice-shaped copper plate electrode 9, and filter boxes 10 and 11 are arranged in this order.

前記格子形銅板電極9は絶縁材12よつて周囲
を電気的に絶縁されるとともに電源端子13と電
流計23を介して外部電源14に接続されてい
る。
The lattice-shaped copper plate electrode 9 is electrically insulated from its surroundings by an insulating material 12 and is connected to an external power source 14 via a power terminal 13 and an ammeter 23.

さらに前記フイルタボツクス10,11は第4
図に示すようにそれぞれ異なるサイズの多数の海
水透過孔10a,11aを有するとともに、その
海水流出側前面に鋼製ネツト15,15が取り付
けられており、又フイルタボツクス10,11内
に溜つた生物の死骸を除去するために洗浄用高圧
ノズル16と死骸取入口17が相対向して設けら
れ、前記死骸取入口17は排出用配管18、排出
用ポンプ5及び仕切弁19を介して放出口6に連
通している。
Further, the filter boxes 10 and 11 are arranged in the fourth filter box.
As shown in the figure, it has a large number of seawater permeation holes 10a, 11a of different sizes, and steel nets 15, 15 are attached to the front side of the seawater outflow side, and the filter boxes 10, 11 are equipped with a large number of seawater permeation holes 10a, 11a. A cleaning high-pressure nozzle 16 and a carcass intake port 17 are provided opposite to each other in order to remove the carcasses of the carcass. is connected to.

前記格子形銅板電極9、フイルタボツクス1
0,11及び洗浄用高圧ノズル16は取水口1に
ボルト、ナツトにより固定された第3図に示すよ
うなサポートフレーム20に取り付けられてい
る。
The grid-shaped copper plate electrode 9 and the filter box 1
0, 11 and the high-pressure cleaning nozzle 16 are attached to a support frame 20 as shown in FIG. 3, which is fixed to the water intake port 1 with bolts and nuts.

このサポートフレーム20には外部電源14よ
り格子形銅板電極9側の反対側が接続されていて
取水口1より入る海水中に通電される。
This support frame 20 is connected to an external power source 14 on the side opposite to the lattice-shaped copper plate electrode 9, so that the seawater entering from the water intake port 1 is energized.

以上述べた構成の生物除去装置において、取水
口1より取り入れられた海水中の比較的大きな生
物や異物はクシ形スクリーン8にて除去され、こ
こで除去し得なかつた小さな生物は第6図に示す
ような格子形銅板電極9の間に海水とともに流れ
込むが外部電源14により電源端子13とサポー
トフレーム20を介して供給された電流が海水中
を流れることにより死滅し、小さな異物とともに
フイルタボツクス10に流れ込む。
In the biological removal device configured as described above, relatively large organisms and foreign objects in the seawater taken in from the water intake port 1 are removed by the comb-shaped screen 8, and small organisms that could not be removed here are shown in Figure 6. As shown, seawater flows between the grid-shaped copper plate electrodes 9, but the electric current supplied by the external power source 14 through the power terminal 13 and the support frame 20 flows through the seawater, causing the seawater to flow into the filter box 10 along with small foreign matter. Flow into.

前記フイルタボツクス10の海水流入側と流出
側の透過孔のサイズは同一であるが海水流出側前
面に配置された第5図に示すような鋼製ネツト1
5より通過率が小さくなつているため生物の死骸
と異物はここに溜る。
The size of the permeation holes on the seawater inflow side and the outflow side of the filter box 10 are the same, but a steel net 1 as shown in FIG. 5 is arranged on the front side of the seawater outflow side.
Since the passage rate is lower than in 5, dead organisms and foreign matter accumulate here.

尚フイルタボツクス10を通過したさらに小さ
な生物の死骸や異物は、同様にして次のフイルタ
ボツクス11にて除去されるが前記フイルタボツ
クス10,11の透過孔をあまり小さくすると圧
損が増大するため、透過孔11aのサイズを透過
孔10aのサイズより小さくしておき、鋼製ネツ
ト15により除去率を向上させる。
Incidentally, even smaller carcasses of living organisms and foreign matter that have passed through the filter box 10 are removed in the next filter box 11 in the same manner. The size of the hole 11a is made smaller than the size of the permeation hole 10a, and the removal rate is improved by the steel net 15.

そしてフイルタボツクス10,11に溜つた生
物の死骸や異物の状態は差圧検出計21によつて
検出され、定期的に洗浄用高圧ノズル16より純
水を噴射し、仕切弁19を開放して排出用ポンプ
5を作動させ、第7図に示すような死骸取入口1
7より放出口6へ放出する。
The condition of dead organisms and foreign matter accumulated in the filter boxes 10 and 11 is detected by the differential pressure detector 21, and pure water is periodically injected from the high-pressure cleaning nozzle 16 and the gate valve 19 is opened. The discharge pump 5 is operated to open the carcass intake port 1 as shown in FIG.
7 to the discharge port 6.

尚外部電源14等の事故により電流が流れない
場合にはフイルタボツクス10,11及び鋼製ネ
ツト15に生物が付着することが考えられるた
め、この時には上蓋22をはずし、サポートフレ
ーム20よりフイルタボツクスと鋼製ネツトを取
り出し交換する。
If the current does not flow due to an accident with the external power supply 14, etc., living organisms may adhere to the filter boxes 10, 11 and the steel net 15, so in this case, remove the top cover 22 and remove the filter box from the support frame 20 Remove the steel net and replace it.

以上説明したように本発明によれば、取水口を
通過した海水中の生物は電流により死滅しフイル
タボツクスにより除去され、又フイルタボツクス
にて捕獲できない生物の幼虫や微生物は死滅して
いるために排水口より放出され、いずれも冷却系
統の海水配管、復水器および熱交換器等の内壁に
付着することがなく、金属劣化や腐蝕を防止する
ことができるとともに循環水ポンプ等の過負荷を
防止し、その運転効率の向上とプラント設備の寿
命の延長及び安全性向上に多大の効果を有する。
As explained above, according to the present invention, organisms in the seawater that have passed through the water intake are killed by the electric current and removed by the filter box, and the larvae and microorganisms of organisms that cannot be captured by the filter box are killed. It is discharged from the drain and does not adhere to the inner walls of the cooling system's seawater piping, condensers, heat exchangers, etc., preventing metal deterioration and corrosion and reducing overload of circulating water pumps, etc. It has a great effect on improving operating efficiency, extending the life of plant equipment, and improving safety.

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

第1図は本発明の生物除去装置を含む海水使用
プラントにおける熱交換系統図、第2図は本発明
の生物除去装置の斜視図、第3図はサポートフレ
ームの斜視図、第4図はフイルタボツクスの斜視
図、第5図は鋼製ネツトの正面図、第6図は格子
形銅板の斜視図、第7図は死骸取入口部分を示す
斜視図である。 1……取水口、2……海水ポンプ、3……海水
配管、4……熱交換器、5……排出用ポンプ、6
……放出口、7……生物除去装置、8……クシ形
スクリーン、9……格子形銅板電極、10,11
……フイルタボツクス、14……外部電源、15
……鋼製ネツト、16……洗浄用高圧ノズル、1
7……死骸取入口、19……仕切弁、20……サ
ポートフレーム、21……差圧検出計。
Fig. 1 is a heat exchange system diagram in a seawater-using plant including the biological removal device of the present invention, Fig. 2 is a perspective view of the biological removal device of the present invention, Fig. 3 is a perspective view of the support frame, and Fig. 4 is a diagram of the filter. FIG. 5 is a front view of the steel net, FIG. 6 is a perspective view of the lattice-shaped copper plate, and FIG. 7 is a perspective view of the carcass inlet. 1... Water intake, 2... Seawater pump, 3... Seawater piping, 4... Heat exchanger, 5... Discharge pump, 6
...Discharge port, 7...Biological removal device, 8...Comb-shaped screen, 9...Grid-shaped copper plate electrode, 10, 11
...Filter box, 14...External power supply, 15
...Steel net, 16...High pressure nozzle for cleaning, 1
7...Carcass intake port, 19...Gate valve, 20...Support frame, 21...Differential pressure detection meter.

Claims (1)

【特許請求の範囲】 1 海水使用プラントにおける海水入口側経路に
設けられた生物除去装置において、前記経路へ海
水流入方向に沿つてクシ形スクリーンと、外部電
源に接続された格子形電極と、フイルタボツクス
とを順に配置したことを特徴とする生物除去装
置。 2 フイルタボツクスには、洗浄用高圧ノズルが
付設されて成る特許請求の範囲第1項記載の生物
除去装置。
[Claims] 1. A biological removal device installed in a seawater inlet route in a seawater-using plant, which includes a comb-shaped screen, a grid-shaped electrode connected to an external power source, and a filter along the direction of seawater inflow into the route. A biological removal device characterized in that boxes are arranged in order. 2. The biological removal device according to claim 1, wherein the filter box is provided with a high-pressure nozzle for cleaning.
JP55146869A 1980-10-22 1980-10-22 Organism removing device Granted JPS5771691A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55146869A JPS5771691A (en) 1980-10-22 1980-10-22 Organism removing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55146869A JPS5771691A (en) 1980-10-22 1980-10-22 Organism removing device

Publications (2)

Publication Number Publication Date
JPS5771691A JPS5771691A (en) 1982-05-04
JPS6231631B2 true JPS6231631B2 (en) 1987-07-09

Family

ID=15417400

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55146869A Granted JPS5771691A (en) 1980-10-22 1980-10-22 Organism removing device

Country Status (1)

Country Link
JP (1) JPS5771691A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3343586A1 (en) * 1983-11-29 1985-06-05 Herbert Dr. 1000 Berlin Pilgrimm Method for sterilizing a medium and device for conduct thereof
JP3776647B2 (en) * 1999-10-19 2006-05-17 株式会社東芝 Antifouling device for seawater contact structure and its performance deterioration monitoring method
KR100717645B1 (en) 2006-03-21 2007-05-11 주식회사 파워이십일 A device for prevent shellfish from cling to cooling water filter of a power plant by using high voltage impulse current
JP6590823B2 (en) * 2013-11-06 2019-10-16 アルク アロマ ピュレ アーベーArc Aroma Pure Ab Method comprising separation and high voltage pulse treatment prior to digestion or further purification

Also Published As

Publication number Publication date
JPS5771691A (en) 1982-05-04

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