JPH04104883A - Slime removing equipment with ozone aqueous solution - Google Patents

Slime removing equipment with ozone aqueous solution

Info

Publication number
JPH04104883A
JPH04104883A JP22009690A JP22009690A JPH04104883A JP H04104883 A JPH04104883 A JP H04104883A JP 22009690 A JP22009690 A JP 22009690A JP 22009690 A JP22009690 A JP 22009690A JP H04104883 A JPH04104883 A JP H04104883A
Authority
JP
Japan
Prior art keywords
ozone
slime
water pipe
water
aqueous solution
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.)
Granted
Application number
JP22009690A
Other languages
Japanese (ja)
Other versions
JP2660089B2 (en
Inventor
Koji Kanamaru
金丸 公二
Nobuyoshi Umiga
信好 海賀
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
Toshiba Corp
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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP22009690A priority Critical patent/JP2660089B2/en
Publication of JPH04104883A publication Critical patent/JPH04104883A/en
Application granted granted Critical
Publication of JP2660089B2 publication Critical patent/JP2660089B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To remove slime in a water pipe with an optimum ozone aq. soln. minimized in metallic corrosion by regulating the flow rate in a water pipe system in accordance with the material of the water pipe. CONSTITUTION:When a valve 13 is closed and valves 11, 12, 15 are opened, water in a water tank 6 is sent to an ozone absorption tower 2 with a pump 9. Ozone is absorbed herein and the obtained ozone aq. soln. is sent to a water pipe system 4 through the valve 12 with a pump 10. Further since the valve 15 is opened, the ozone aq. soln. is separated into a heat exchanger 3 and a by-pass pipeline 21. It is passed through a plant pipeline 5 and returned to the water tank 6. Thereby slime in the water pipe systems 4, 5 and the heat exchanger 3 is removed. In this case, the pump 10 is selected to the volume capable of being pressurized and introduced at several atmospheres. In such a way, even when slime is present in the water pipe systems 4, 5, the flow velocity of the ozone aq. soln. is made high and the removal capacity of the ozone aq. soln. is held constant in the water pipe. Thus, slime is efficiently and uniformly removed.

Description

【発明の詳細な説明】 〔発明の目的〕 (産業上の利用分野) 本発明は、水管内にオゾン水溶液を流入させて水管内の
スライムを除去するオゾン水溶液にょるスライム剥離装
置に関するものである。
[Detailed Description of the Invention] [Object of the Invention] (Industrial Application Field) The present invention relates to a slime removal device using an ozone aqueous solution that removes slime in a water pipe by flowing the ozone aqueous solution into the water pipe. .

(従来の技術) 工業プラントの熱交換器、廃水処理装置などに用いられ
る水管の内壁には水中の微生物が繁殖して付着し、スラ
イムを形成することが多く、このスライムは水管内の水
の流通を妨げて熱交換器または廃水処理の効率を低下さ
せるだけでなく。
(Prior art) Microorganisms in the water often propagate and adhere to the inner walls of water pipes used in heat exchangers and wastewater treatment equipment in industrial plants, forming slime. As well as impeding the flow and reducing the efficiency of heat exchangers or wastewater treatment.

水管が金属材質の場合には、これに対する腐食を生ずる
ので、最近の工業プラントの規模の増大や上質の工業用
水の不足に伴って、スライム防止対策が重要な課題とな
って来ている。
When water pipes are made of metal, corrosion occurs; therefore, with the recent increase in the scale of industrial plants and the shortage of high-quality industrial water, measures to prevent slime have become an important issue.

従来はスライム防止に対して塩素または塩素系薬剤が多
く用いられているが、使用後の残留塩素を含む廃水が環
境汚染を招くので、その処理が必がであるなど使用上の
問題がある。
Conventionally, chlorine or chlorine-based agents have been widely used to prevent slime, but there are problems in its use, such as the fact that wastewater containing residual chlorine after use pollutes the environment and must be treated.

これに対して、本発明者の一人はオゾン水溶液がスライ
ムの分解剥離に有効であり、かつ処理後の残留オゾンは
自己分解して汚染源とならないことを考慮し、オゾン水
溶液を利用したスライムの剥離方法を特願昭50−13
6186 (特公昭56−12181)および特願昭5
1−34197 (特公昭5g −27997)で提案
した。
On the other hand, one of the inventors of the present invention considered that an aqueous ozone solution is effective in decomposing and removing slime, and that residual ozone after treatment self-decomposes and does not become a source of pollution. Patent application for method 1977-13
6186 (Special Publication No. 56-12181) and Patent Application No. 5
1-34197 (Tokuko Showa 5g-27997).

(発明が解決しようとする課題) しかしながら工業プラントに用いられる水管の材質は同
じでなく、例えば熱交換器の内部配管には一般に電気銅
が用いられるのに対して、装置間を接続する水管には一
般に軟鋼が使用されるので、同一の流速でオゾン水溶液
を流すと、材質の差によっては管の腐食を招くという問
題がある。
(Problem to be solved by the invention) However, the materials of water pipes used in industrial plants are not the same. For example, electrolytic copper is generally used for the internal piping of heat exchangers, whereas electrolytic copper is used for water pipes connecting equipment. Generally, mild steel is used, so if the ozone aqueous solution is flowed at the same flow rate, there is a problem that depending on the material, the pipe may corrode.

本発明は上記の問題を考慮してなされたもので、管の材
質が異っても管の腐食を最小限にして水管内のスライム
を能率よく、かつ均一に除去できるオゾン水溶液による
スライム剥離装置を提供することを目的としている。
The present invention was made in consideration of the above problems, and is a slime stripping device using an ozone aqueous solution that can efficiently and uniformly remove slime in water pipes while minimizing corrosion of the pipes even if the pipes are made of different materials. is intended to provide.

〔発明の構成〕[Structure of the invention]

(課題を解決するための手段および作用)上記の目的を
達成するために本発明は、オゾン水溶液をスライムの付
着した水管内に送入してスライムの剥離を行う装置にお
いて、水管材質に応じた適当な流速でオゾン水溶液を流
し、これによって管の腐食を生ずることなく能率よく、
かつ均一にスライムの剥離ができるようにしたものであ
る。
(Means and effects for solving the problem) In order to achieve the above object, the present invention provides an apparatus for peeling off slime by feeding an aqueous ozone solution into a water pipe to which slime is attached. By flowing the ozone aqueous solution at an appropriate flow rate, this can be done efficiently without causing corrosion of the pipes.
Moreover, the slime can be peeled off evenly.

例えば、水管の材料が冷却水系に最も広く利用されてい
る軟鋼5S−41の場合にはオゾン水溶液の流速を早く
して処理した方が、スライムの均一な剥離の面からも腐
食の面からも有利になる。
For example, if the material of the water pipe is mild steel 5S-41, which is the most widely used material for cooling water systems, it is better to treat it by increasing the flow rate of the ozone aqueous solution, both from the standpoint of uniform stripping of slime and from the standpoint of corrosion. It will be advantageous.

また発明者の実験によれば、熱交換器に広く利用されて
いる電気銅の場合、オゾン水溶液の流速が1 m/se
cで空気に対して約5倍もの腐食量を示すが、0.5m
/see程度になるとオゾン水溶液の方が腐食量が少な
くなるという結果が得られた。
Furthermore, according to the inventor's experiments, in the case of electrolytic copper, which is widely used in heat exchangers, the flow rate of ozone aqueous solution is 1 m/sec.
c shows about 5 times the amount of corrosion compared to air, but 0.5 m
The results showed that the ozone aqueous solution resulted in less corrosion when the amount of corrosion reached approximately /see.

これらの実験結果をまとめると第1表(工業用水第33
5号昭和61年8月より抜翠)のようになる。
The results of these experiments are summarized in Table 1 (Industrial Water No. 33)
No. 5 (No. 5 removed from August 1986).

以下余白 従って、オゾン水溶液によるスライム剥離装置において
は、軟鋼を用いた水管では流速を速くし、電気銅を用い
た熱交換器ではバイパス配管を設けて流速を低下させる
ことによって水管の腐食をも考慮した能率的で均一な水
管のスライム剥離が可能となる。
Margin below Therefore, in a slime removal device using an ozone aqueous solution, corrosion of the water pipes is taken into account by increasing the flow velocity in water pipes made of mild steel, and by installing bypass piping and lowering the flow velocity in heat exchangers using electrolytic copper. This enables efficient and uniform slime removal from water pipes.

(実施例) 本発明の一実施例を第1図に示す。(Example) An embodiment of the present invention is shown in FIG.

第1図において、1はオゾン発生器、2はオゾンを水中
に吸収してオゾン水溶液を作るオゾン吸収塔、3はスラ
イムを防止すべきプラントの熱交換器、4,5は同じく
スライムを防止すべきプラントの水管、6は水槽、7は
余剰オゾンを分解して排出するオゾン分解塔である。
In Figure 1, 1 is an ozone generator, 2 is an ozone absorption tower that absorbs ozone into water and creates an ozone aqueous solution, 3 is a heat exchanger in a plant that is supposed to prevent slime, and 4 and 5 are also used to prevent slime. 6 is a water tank, and 7 is an ozone decomposition tower that decomposes and discharges excess ozone.

第1図のように構成された装置において、通常のプラン
ト運転中はバルブ13.14は開いており、バルブ11
.12.15は閉している。水槽6内の水はポンプ9に
よって水管4へ送られ、熱交換器3および水管5を通っ
て水槽6に戻り、水の循環が行われる。
In a device configured as shown in FIG. 1, during normal plant operation, valves 13 and 14 are open and valve 11 is open.
.. 12.15 is closed. The water in the water tank 6 is sent to the water pipe 4 by the pump 9, returns to the water tank 6 through the heat exchanger 3 and the water pipe 5, and the water is circulated.

熱交換器を含む水管系統のスライム剥離を行うときは、
バルブ13を閉じ、バルブ11.12.15を開くと、
水槽6内の水はポンプ9によってオゾン吸収塔2へ送ら
れ、ここ紀でオゾンを吸収したオゾン水溶液はポンプ1
0によってバルブ12を経て水管系統4へ送られる。ま
た、バルブ15が開いているので、オゾン水溶液は熱交
換器3とバイパス配管21に分流し、プラント配管5を
通って水槽6へ戻り、これによって水管系統4,5と熱
交換器3のスライム剥離が行われる。
When removing slime from water pipe systems including heat exchangers,
When valve 13 is closed and valves 11.12.15 are opened,
The water in the water tank 6 is sent to the ozone absorption tower 2 by a pump 9, and the ozone aqueous solution that has absorbed ozone in this period is pumped to the ozone absorption tower 2.
0 is sent to the water pipe system 4 via the valve 12. Also, since the valve 15 is open, the ozone aqueous solution is diverted to the heat exchanger 3 and the bypass pipe 21, returns to the water tank 6 through the plant pipe 5, and the slime in the water pipe system 4, 5 and the heat exchanger 3 is thereby Peeling is performed.

この場合、ポンプ10は散気圧で加圧注入できるような
容量で選定する。こうすれば水管系統4゜5内にスライ
ムがあってもオゾン水溶液の流速が高くなり、オゾン水
溶液の剥離能力が水管内で一定に保持され、能率よく、
かつ均一なスライム剥離が行われる。また熱交換器バイ
パス用の配管21は熱交換器3側の流速が0.5m/s
ee程度となるようにサイズを選定する。こうすれば電
気銅を使用した熱交換器のスライム剥離を金属腐食を最
少にして高能率に行うことが可能となる。
In this case, the pump 10 is selected to have a capacity that allows pressurized injection at diffused pressure. In this way, even if there is slime in the water pipe system 4.5, the flow rate of the ozone aqueous solution will be high, the stripping ability of the ozone aqueous solution will be maintained constant within the water pipe, and the process will be carried out efficiently.
Moreover, uniform peeling of the slime is performed. In addition, the heat exchanger bypass piping 21 has a flow velocity of 0.5 m/s on the heat exchanger 3 side.
The size is selected so that it is about ee. This makes it possible to remove slime from a heat exchanger using electrolytic copper with high efficiency while minimizing metal corrosion.

本発明の他の実施例を第2図に示す。Another embodiment of the invention is shown in FIG.

第2図は銅を用いた熱交換器以外にバイパス配管を設は
オゾン水溶液の流速を調整するものであり、熱交換器の
入口に電動の調節弁23を設けて流速を制御している。
In Fig. 2, bypass piping is installed in addition to the heat exchanger using copper to adjust the flow rate of the ozone aqueous solution, and an electric control valve 23 is installed at the inlet of the heat exchanger to control the flow rate.

また、プラントを停止できない場合は、熱交換器として
の能力が維持される程度の間欠運転を行う方式を採用す
ることも可能である。
Furthermore, if the plant cannot be stopped, it is also possible to adopt a method of performing intermittent operation to the extent that the capacity of the heat exchanger is maintained.

〔発明の効果〕〔Effect of the invention〕

以上説明したように本発明によれば、水管系統の流速を
水管の材質に応じて調節できるようにしているので、金
属腐食を最少にした最適なオゾン水溶液による水管内の
スライムの剥離を行うことが可能となる。
As explained above, according to the present invention, the flow rate of the water pipe system can be adjusted according to the material of the water pipe, so slime in the water pipe can be removed using an optimal ozone aqueous solution that minimizes metal corrosion. becomes possible.

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

第1図は本発明の一実施例を示す系統図、第2図は本発
明の他の実施例を示す系統図である。 1・・・オゾン発生器   2・・・オゾン吸収塔3・
・・熱交換器     4,5・・プラント用水管6・
・・水槽       7・・・オゾン分解塔8・ブロ
ワ 11〜17・−バルブ 9.10・・ポンプ 21・・バイパス配管 22・・配水管 23・・電動調節弁 (8733)  代理人 弁理士 猪 股 祥 晃(ほ
か1名)第1図
FIG. 1 is a system diagram showing one embodiment of the present invention, and FIG. 2 is a system diagram showing another embodiment of the invention. 1... Ozone generator 2... Ozone absorption tower 3.
・・Heat exchanger 4, 5・・Plant water pipe 6・
・・Water tank 7・・Ozone decomposition tower 8・Blowers 11 to 17・・Valve 9.10・・Pump 21・・Bypass piping 22・・Water pipe 23・・Electric control valve (8733) Agent Patent attorney Inomata Yoshiaki (and 1 other person) Figure 1

Claims (1)

【特許請求の範囲】[Claims] オゾン発生器、オゾン発生器からのオゾンを水中に吸収
してオゾン水溶液をつくるオゾン吸収塔、オゾン水溶液
をスライムを除去すべき水管系統へ送るポンプ、水の循
環通路を通常の系統運転とスライム剥離運転とに切換え
るバルブ類を備えたオゾン水溶液によるスライム剥離装
置において、スライム剥離運転時にスライムを除去すべ
き水管系統の一部の流速を制御するバイパス配管あるい
は調整弁を設けたことを特徴とするオゾン水溶液による
スライム剥離装置。
An ozone generator, an ozone absorption tower that absorbs ozone from the ozone generator into water and creates an ozone aqueous solution, a pump that sends the ozone aqueous solution to the water pipe system where slime is to be removed, and a water circulation path for normal system operation and slime removal. An ozone aqueous slime removal device equipped with valves for switching between operation and operation, characterized in that it is equipped with bypass piping or a regulating valve that controls the flow rate of a part of the water pipe system in which slime is to be removed during slime removal operation. Slime peeling device using aqueous solution.
JP22009690A 1990-08-23 1990-08-23 Slime stripper with ozone aqueous solution Expired - Lifetime JP2660089B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22009690A JP2660089B2 (en) 1990-08-23 1990-08-23 Slime stripper with ozone aqueous solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22009690A JP2660089B2 (en) 1990-08-23 1990-08-23 Slime stripper with ozone aqueous solution

Publications (2)

Publication Number Publication Date
JPH04104883A true JPH04104883A (en) 1992-04-07
JP2660089B2 JP2660089B2 (en) 1997-10-08

Family

ID=16745863

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22009690A Expired - Lifetime JP2660089B2 (en) 1990-08-23 1990-08-23 Slime stripper with ozone aqueous solution

Country Status (1)

Country Link
JP (1) JP2660089B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015085211A (en) * 2013-10-28 2015-05-07 多田電機株式会社 Apparatus and method for ozone sterilization of cooling tower

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015085211A (en) * 2013-10-28 2015-05-07 多田電機株式会社 Apparatus and method for ozone sterilization of cooling tower

Also Published As

Publication number Publication date
JP2660089B2 (en) 1997-10-08

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