JPS6320194B2 - - Google Patents
Info
- Publication number
- JPS6320194B2 JPS6320194B2 JP12252484A JP12252484A JPS6320194B2 JP S6320194 B2 JPS6320194 B2 JP S6320194B2 JP 12252484 A JP12252484 A JP 12252484A JP 12252484 A JP12252484 A JP 12252484A JP S6320194 B2 JPS6320194 B2 JP S6320194B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- ozone
- cooling water
- supply pipe
- roll
- 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
Links
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Description
【発明の詳細な説明】
〔発明の技術分野〕
この発明は、冷間圧延のダイレクト法における
循環ロール冷却水系のオゾンによる水処理方法に
関するものである。DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a method for treating water using ozone in a circulating roll cooling water system in a direct method of cold rolling.
従来この種の水処理方法として第1図に示すも
のがあつた。図において、1はストリツプ、2は
このストリツプを圧延する作業ロール、3はスト
リツプ1に圧延油を噴射するためのヘツダー、4
は作業ロール2に冷却水を噴射するための冷却水
ヘツダー、5は圧延に使用された冷却水と圧延油
を集める排水受槽、6はこの排水受槽から排水を
導入し油分等を分離して浄化する水浄化装置、7
は浄化された水を冷却する冷却塔、8は冷却され
た水を給水配管9を通して冷却水ヘツダー4へ給
水する給水ポンプ、10は給水配管9へ新水を補
給する新水補給管、11は圧延油タンク、12は
この圧延油タンクに貯留している圧延油をヘツダ
ー3から噴射するための圧延油ポンプ、13は水
浄化装置6で分離された油分を再生して圧延油タ
ンク11へ送る圧延油再生装置、14は給水配管
9の内壁に微生物性のスライムが付着することを
防止するためにロール冷却水にオゾンを間欠的に
注入するための間欠オゾン発生供給装置、15は
この間欠オゾン発生供給装置に原料酸素を供給す
る酸素供給装置、16は間欠オゾン発生供給装置
14からオゾンを吸引して冷却水に溶解するよう
に給水配管9のバイパス管9aに設けられたエゼ
クタ、17はこのエゼクタを駆動するためのエゼ
クタポンプである。
A conventional water treatment method of this type is shown in FIG. In the figure, 1 is a strip, 2 is a work roll for rolling this strip, 3 is a header for injecting rolling oil onto the strip 1, and 4 is a header for injecting rolling oil onto the strip 1.
5 is a cooling water header for injecting cooling water to the work roll 2; 5 is a drainage tank that collects the cooling water and rolling oil used in rolling; and 6 is a drainage tank that introduces wastewater from this drainage tank, separates oil, etc., and purifies it. water purification device, 7
8 is a water supply pump that supplies the cooled water to the cooling water header 4 through the water supply pipe 9; 10 is a new water supply pipe that supplies fresh water to the water supply pipe 9; 11 is a cooling tower that cools the purified water; A rolling oil tank 12 is a rolling oil pump for injecting the rolling oil stored in this rolling oil tank from the header 3; 13 is a rolling oil pump that regenerates the oil separated by the water purification device 6 and sends it to the rolling oil tank 11; A rolling oil regeneration device 14 is an intermittent ozone generation and supply device for intermittently injecting ozone into the roll cooling water to prevent microbial slime from adhering to the inner wall of the water supply pipe 9, and 15 is an intermittent ozone generation and supply device. An oxygen supply device that supplies raw oxygen to the generation and supply device; 16 is an ejector provided in the bypass pipe 9a of the water supply pipe 9 to suck ozone from the intermittent ozone generation and supply device 14 and dissolve it in the cooling water; 17 is an ejector provided in the bypass pipe 9a of the water supply pipe 9 This is an ejector pump for driving the ejector.
次に動作について説明する。ストリツプ1に圧
延油をヘツダー3より噴射して、作業ロール2と
ストリツプ1間の潤滑を行ない、冷却水ヘツダー
4より冷却水を噴射して作業ロール2の冷却を行
う。圧延に使用された冷却水と圧延油は排水受槽
5に集水され、水浄化装置6にて油分および鉄粉
等の夾雑物を除去した後、冷却塔7で水温を下げ
て、給水ポンプ8にて冷却水ヘツダー4に給水す
る。このようにロール冷却水を循環再利用する
と、給水配管9に微生物が繁殖してスライムを生
成する。この給水配管9の内壁へのスライム付着
を防止するため、間欠オゾン発生供給装置14に
吸着されているオゾンを、減圧脱着しかつ溶解さ
せるため循環ロール冷却水の一部をエゼクタポン
プ17により、エゼクタ16に送り、エゼクタ駆
動流体およびオゾン溶解用水として用い、ここで
高濃度オゾン水を作り、給水配管9に注入する。
給水配管9内でオゾン水はロール冷却水と混合さ
れ、給水配管9の内壁を洗浄しながら冷却水ヘツ
ダー4より噴射される。この間にオゾンは自己分
解、水中有機物との反応および殺菌のために減少
する。このようにオゾン水で1日に1〜数回、1
回1分〜数分間洗浄すると、給水配管9内壁への
スライムの付着は防止される。第2図はオゾン半
減期とオゾン注入量の関係図である。 Next, the operation will be explained. Rolling oil is injected onto the strip 1 from a header 3 to lubricate between the work roll 2 and the strip 1, and cooling water is injected from a cooling water header 4 to cool the work roll 2. Cooling water and rolling oil used in rolling are collected in a drainage tank 5, and after removing impurities such as oil and iron powder in a water purification device 6, the water temperature is lowered in a cooling tower 7, and the water is sent to a water supply pump 8. Water is supplied to the cooling water header 4 at. When the roll cooling water is circulated and reused in this manner, microorganisms propagate in the water supply pipe 9 and generate slime. In order to prevent slime from adhering to the inner wall of the water supply pipe 9, a portion of the circulating roll cooling water is pumped into the ejector pump 17 to desorb and dissolve the ozone adsorbed in the intermittent ozone generation and supply device 14 under reduced pressure. 16 and used as an ejector driving fluid and water for dissolving ozone, high-concentration ozone water is made here and injected into the water supply pipe 9.
Ozone water is mixed with roll cooling water in the water supply pipe 9, and is sprayed from the cooling water header 4 while cleaning the inner wall of the water supply pipe 9. During this time, ozone decreases due to autolysis, reaction with organic matter in the water, and disinfection. In this way, use ozonated water once to several times a day.
Cleaning for one to several minutes each time will prevent slime from adhering to the inner wall of the water supply pipe 9. FIG. 2 is a diagram showing the relationship between ozone half-life and ozone injection amount.
従来のコールドストリツプ用冷却水系の水処理
方法は以上のように構成されており、オゾンを注
入するためのオゾン溶解用水として循環ロール冷
却水を用いているため、オゾンの減少速度が速く
て、オゾン半減期が短く、そのため末端の冷却水
ヘツダー部のオゾン濃度をスライム付着防止に必
要な一定のオゾン濃度以上に保つためには、第2
図に示すように、多量のオゾンを注入しなければ
ならない欠点があつた。 The conventional water treatment method for cold strip cooling water systems is configured as described above, and since circulating roll cooling water is used as the ozone dissolving water for injecting ozone, the ozone reduction rate is fast. , the half-life of ozone is short, so in order to keep the ozone concentration in the cooling water header at the end above a certain level required to prevent slime adhesion, it is necessary to
As shown in the figure, there was a drawback that a large amount of ozone had to be injected.
この発明は、上記のような従来の欠点を除去す
る目的でなされたもので、オゾンを注入するため
のオゾン溶解用水として、循環ロール冷却水より
水質のよい水を用いることにより、オゾンの半減
期を長くし、これにより少ないオゾンの注入量で
スライム付着を防止でき、信頼性が高く、かつ経
済性に優れたコールドストリツプ用冷却水系の水
処理方法を提供するものである。
This invention was made for the purpose of eliminating the above-mentioned drawbacks of the conventional technology, and by using water of higher quality than circulating roll cooling water as ozone dissolving water for injecting ozone, the half-life of ozone can be reduced. To provide a water treatment method for a cooling water system for a cold strip that is highly reliable and economically efficient, by increasing the length of time, thereby preventing slime adhesion with a small amount of ozone injection.
以下、この発明の一実施例を図について説明す
る。第3図はこの発明の一実施例を示す系統図で
あり、図において、1〜17は第1図と同一また
は相当部分を示す。18および19は水路切換の
ためのバルブであり、バルブ18は給水配管9の
新水補給管10の合流点と冷却塔7との間に設け
られ、バルブ19は新水供給管10に設けられて
いる。他の構成は第1図と同様である。
An embodiment of the present invention will be described below with reference to the drawings. FIG. 3 is a system diagram showing an embodiment of the present invention, and in the figure, numerals 1 to 17 indicate the same or equivalent parts as in FIG. 1. 18 and 19 are valves for switching water channels, the valve 18 is provided between the confluence of the new water supply pipe 10 of the water supply pipe 9 and the cooling tower 7, and the valve 19 is provided in the new water supply pipe 10. ing. The other configurations are the same as in FIG. 1.
次に動作について説明する。圧延のための動作
は従来と同様であり、このときバルブ18を開、
バルブ19を閉としてロール冷却水を循環する。
次に、給水配管9をオゾン水で洗浄するときは、
まず、通常は閉になつているバルブ19を開に
し、次いで開になつているバルブ18を閉にし、
新水補給管10から給水ポンプ8により、新水だ
けを給水配管9に送水する。そして給水配管9内
の水が新水に入れ替つた段階で、エゼクタポンプ
17を起動して、エゼクタ16により吸引し、間
欠オゾン発生供給装置14よりオゾンを脱着して
新水に溶解させ、給水配管9を洗浄する。オゾン
洗浄が終れば、再びバルブを切り換えて、バルブ
18を開に、バルブ19を閉にしてロール冷却水
を循環する。 Next, the operation will be explained. The operation for rolling is the same as the conventional one; at this time, the valve 18 is opened,
Valve 19 is closed to circulate the roll cooling water.
Next, when cleaning the water supply pipe 9 with ozonated water,
First, open the normally closed valve 19, then close the open valve 18,
Only fresh water is sent from the fresh water supply pipe 10 to the water supply pipe 9 by the water supply pump 8. When the water in the water supply pipe 9 has been replaced with fresh water, the ejector pump 17 is started, the ejector 16 sucks ozone, the intermittent ozone generation and supply device 14 desorbs ozone and dissolves it in the new water, and the ozone is removed from the water supply pipe 9. Wash 9. When the ozone cleaning is finished, the valves are switched again to open the valve 18 and close the valve 19 to circulate the roll cooling water.
なお、上記実施例ではオゾン溶解用水として補
給用新水を用いたが、ロール冷却水よりオゾンの
半減期が長く、かつ水質の安定した水であれば他
の水でも使用可能である。 In the above embodiments, fresh water for replenishment was used as the water for dissolving ozone, but other water can be used as long as it has a longer half-life of ozone than roll cooling water and is stable in quality.
以上のように、この発明によれば、ロール冷却
水系洗浄用のオゾン溶解用水として、循環ロール
冷却水より水質の良い水を用いたので、給水配管
末端でのオゾン濃度を一定以上に保つのに必要な
初期オゾン注入量が少なくてもスライムの付着を
防止でき、信頼性が高いとともに、装置がコンパ
クトになり、経済性にも優れているという効果が
ある。
As described above, according to the present invention, since water of higher quality than circulating roll cooling water is used as the ozone dissolving water for cleaning the roll cooling water system, it is possible to maintain the ozone concentration at the end of the water supply pipe above a certain level. Even if the required initial ozone injection amount is small, slime adhesion can be prevented, the reliability is high, the device is compact, and it is economical.
第1図は従来のコールドストリツプ用冷却水系
の水処理方法を示す系統図、第2図はオゾン半減
期とオゾン注入量の関係図、第3図はこの発明の
一実施例によるコールドストリツプ用冷却水系の
水処理方法を示す系統図である。
各図中、同一符号は同一または相当部分を示
し、1はストリツプ、2は作業ロール、5は排水
受槽、6は水浄化装置、7は冷却塔、8は給水ポ
ンプ、9は給水配管、10は新水補給管、11は
圧延油タンク、13は圧延油再生装置、14は間
欠オゾン発生供給装置、15は酸素供給装置、1
6はエゼクタ、17はエゼクタポンプ、18,1
9はバルブである。
Fig. 1 is a system diagram showing a conventional water treatment method for a cold strip cooling water system, Fig. 2 is a diagram showing the relationship between ozone half-life and ozone injection amount, and Fig. 3 is a cold strip cooling water treatment method according to an embodiment of the present invention. FIG. 2 is a system diagram showing a water treatment method for a lip cooling water system. In each figure, the same reference numerals indicate the same or equivalent parts, 1 is a strip, 2 is a work roll, 5 is a waste water tank, 6 is a water purification device, 7 is a cooling tower, 8 is a water supply pump, 9 is a water supply pipe, 10 1 is a new water supply pipe, 11 is a rolling oil tank, 13 is a rolling oil regeneration device, 14 is an intermittent ozone generation and supply device, 15 is an oxygen supply device, 1
6 is an ejector, 17 is an ejector pump, 18,1
9 is a valve.
Claims (1)
水系にオゾンを間欠的に注入して微生物障害を防
止するコールドストリツプ用冷却水系の水処理方
法において、オゾンを注入するためのオゾン溶解
水用として、循環ロール冷却水より水質のよい水
を用いることを特徴とするコールドストリツプ用
冷却水系の水処理方法。 2 オゾン溶解用水として、ロール冷却水系への
補給用新水を用いることを特徴とする特許請求の
範囲第1項記載のコールドストリツプ用冷却水系
の水処理方法。 3 オゾン注入時にバルブの切換によりロール冷
却水の循環を停止し、新水を供給してオゾン注入
を行うことを特徴とする特許請求の範囲第2項記
載のコールドストリツプ用冷却水系の水処理方
法。[Scope of Claims] 1. In a water treatment method for a cold strip cooling water system in which ozone is intermittently injected into the roll cooling water system in the direct method of cold rolling to prevent microbial damage. A water treatment method for a cold strip cooling water system, characterized in that water of higher quality than circulating roll cooling water is used as ozone-dissolved water. 2. A water treatment method for a cold strip cooling water system according to claim 1, characterized in that fresh water for replenishing the roll cooling water system is used as the ozone dissolving water. 3. The cold strip cooling water system according to claim 2, characterized in that during ozone injection, circulation of roll cooling water is stopped by switching a valve, and fresh water is supplied to perform ozone injection. Processing method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12252484A JPS61490A (en) | 1984-06-12 | 1984-06-12 | Water treatment of cooling water system for cold strip mill |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12252484A JPS61490A (en) | 1984-06-12 | 1984-06-12 | Water treatment of cooling water system for cold strip mill |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61490A JPS61490A (en) | 1986-01-06 |
| JPS6320194B2 true JPS6320194B2 (en) | 1988-04-26 |
Family
ID=14837982
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12252484A Granted JPS61490A (en) | 1984-06-12 | 1984-06-12 | Water treatment of cooling water system for cold strip mill |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61490A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102397893A (en) * | 2011-11-30 | 2012-04-04 | 东北大学 | Water supply device of after-rolling cooling system |
-
1984
- 1984-06-12 JP JP12252484A patent/JPS61490A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61490A (en) | 1986-01-06 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |