JPH089054B2 - Make-up water control device in circulating water system - Google Patents
Make-up water control device in circulating water systemInfo
- Publication number
- JPH089054B2 JPH089054B2 JP3134763A JP13476391A JPH089054B2 JP H089054 B2 JPH089054 B2 JP H089054B2 JP 3134763 A JP3134763 A JP 3134763A JP 13476391 A JP13476391 A JP 13476391A JP H089054 B2 JPH089054 B2 JP H089054B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- amount
- circulating
- tank
- water system
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims description 208
- 230000000717 retained effect Effects 0.000 claims description 17
- 239000000498 cooling water Substances 0.000 claims description 15
- 239000008400 supply water Substances 0.000 claims description 6
- 238000001514 detection method Methods 0.000 claims description 4
- 102000001999 Transcription Factor Pit-1 Human genes 0.000 description 10
- 108010040742 Transcription Factor Pit-1 Proteins 0.000 description 10
- 238000005096 rolling process Methods 0.000 description 10
- 238000001816 cooling Methods 0.000 description 9
- 238000004062 sedimentation Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 239000010802 sludge Substances 0.000 description 6
- 239000002562 thickening agent Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 238000001704 evaporation Methods 0.000 description 5
- 230000008020 evaporation Effects 0.000 description 5
- 239000000126 substance Substances 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- 230000003134 recirculating effect Effects 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 238000009749 continuous casting Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 229910021642 ultra pure water Inorganic materials 0.000 description 1
- 239000012498 ultrapure water Substances 0.000 description 1
- 238000009849 vacuum degassing Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Feedback Control In General (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、循環水系における補給
水制御装置に関し、詳細には、複数の中継槽を含む循環
冷却水系及び洗浄水系からなる循環水系における補給水
制御装置に関し、主として鉄鋼業における真空脱ガス設
備、連続鋳造設備、各種圧延設備、又は電子部品工業に
おける超純水洗浄クローズドシステム等における冷却水
系、洗浄水系への補給水の制御装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a makeup water controller for a circulating water system, and more particularly to a makeup water controller for a circulating water system including a circulating cooling water system including a plurality of relay tanks and a wash water system, mainly in the steel industry. The present invention relates to a cooling water system in a vacuum degassing facility, a continuous casting facility, various rolling facilities, an ultrapure water cleaning closed system in the electronic component industry, and a control device for makeup water to the cleaning water system.
【0002】[0002]
【従来の技術】循環水系は前記鉄鋼業、電子部品工業の
他、化学工業等の各工業界において広く用いられてい
る。かかる循環水系において、保有水量を一定に保持す
ることが必要であるが、系外への水の流出(排出)は不
可避であり、従って、保有水量を出来るだけ一定に保持
すべく、補給水の供給が行われる。2. Description of the Related Art Circulating water systems are widely used in various industries such as the steel industry, the electronic parts industry, and the chemical industry. In such a circulating water system, it is necessary to keep the amount of retained water constant, but outflow (discharge) of water to the outside of the system is unavoidable. Therefore, in order to keep the amount of retained water as constant as possible, make-up water is required. Supply is made.
【0003】その詳細を、図1に示す如き圧延設備にお
ける循環水系の場合を例に挙げて以下説明する。図1に
示す循環水系において、冷却水はスケールピット2,沈
澱池3,濾過器4,冷却塔5,冷水槽6を経由して圧延
設備1に送られ、これにより循環冷却水系が形成されて
いる。又、濾過器4には、逆洗排水槽7が接続されてい
て、循環水系の一部の水が逆洗排水槽7を経て循環冷却
水系に返送される。The details will be described below by taking the case of a circulating water system in a rolling facility as shown in FIG. 1 as an example. In the circulating water system shown in FIG. 1, the cooling water is sent to the rolling equipment 1 via the scale pit 2, the sedimentation basin 3, the filter 4, the cooling tower 5 and the cold water tank 6, whereby the circulating cooling water system is formed. There is. Further, a backwash drainage tank 7 is connected to the filter 4, and a part of the water in the circulating water system is returned to the circulating cooling water system through the backwash drainage tank 7.
【0004】この循環水系において、スケールピット2
等の各設備から水分が排出されるので、保有水量を一定
に保持するための補給水の供給が必要である。例えば、
排出されるものは、スケールピット2で排出されるスケ
ールの付着水、沈澱池3の排泥中の水分、濾過器4での
逆洗排水、冷却塔5での蒸発及び飛散水分(ドリフトロ
ス)、蒸発による水中溶解物の成分濃縮を防止するため
のブロー水等が挙げられる。一方、排泥中の水分の一部
や、逆洗排水の処理水は循環水系に流入してくる。しか
し、排出量の方が多いため、補給水を供給しないと保有
水量が時間とともに減少して運転不能となることを防止
すると共に、循環系の濃縮度を一定にするため、補給水
の供給が必要となる。In this circulating water system, the scale pit 2
Since water is discharged from each facility, it is necessary to supply makeup water to keep the amount of water held constant. For example,
What is discharged is the water adhering to the scale discharged in the scale pit 2, the water content in the sludge of the sedimentation tank 3, the backwash drainage in the filter 4, the evaporation and scattered moisture in the cooling tower 5 (drift loss). Blow water and the like for preventing the concentration of the dissolved substance in water by evaporation. On the other hand, part of the water in the sludge and the treated water from the backwash drainage flow into the circulating water system. However, since the amount of discharged water is larger, the amount of retained water is prevented from decreasing with time and becoming inoperable unless supplementary water is supplied. Will be needed.
【0005】従来、かかる循環水系における補給水の供
給は下記方法により行われている。即ち、冷水槽6での
水位(レベル)によって補給水量を調節する方法、又
は、予め定めた一定量の補給水を常時供給する方法によ
り行われている。Conventionally, supply of makeup water in such a circulating water system is performed by the following method. That is, it is performed by a method of adjusting the amount of makeup water according to the water level (level) in the cold water tank 6 or a method of constantly supplying a predetermined amount of makeup water.
【0006】[0006]
【発明が解決しようとする課題】ところが、前記従来の
補給水の供給方法においては、基本的に保有水量を一定
に保持するのが容易でないという問題点を有しており、
特に鉄鋼業等で使用される如き数千〜数万m3/Hrの大量
の循環水系の場合において種々の深刻な問題点を生じて
いる。即ち、大量の循環水系の場合、レベルコントロー
ルを容易にするために大量のオーバーフローを吸収する
必要があって、排水設備が大形化すると共に運転コスト
が嵩むこと、補給のタイミングを一つの排槽(例えば冷
水槽6)で行うために過大補給となりがちとなり、補給
水の無駄が多く、薬品処理をする場合にはさらに薬品費
の増大を招く。又、大容量のポンプ用モータを保護する
必要上、スイッチングアワーの関係から滞留時間の長い
大容量の水槽が必要となり、設備コストが高くつくこと
等の問題点を生じている。However, in the above-mentioned conventional supply method of makeup water, there is a problem that it is basically difficult to keep the amount of retained water constant.
Particularly, in the case of a large amount of circulating water system of thousands to tens of thousands m 3 / Hr as used in the steel industry, various serious problems are caused. That is, in the case of a large amount of circulating water system, it is necessary to absorb a large amount of overflow in order to facilitate level control, the drainage facility becomes large and the operating cost increases, and the timing of replenishment is set to one drain tank. Since it is performed in (for example, the cold water tank 6), it tends to be excessively replenished, the replenishment water is wasted a lot, and the chemical cost is further increased when the chemical treatment is performed. Further, since it is necessary to protect a large-capacity pump motor, a large-capacity water tank having a long residence time is required due to switching hours, which causes problems such as high equipment cost.
【0007】本発明はこの様な事情に着目してなされた
ものであって、その目的は、前記従来のものが有する問
題点を解消し、大形の排水設備等を要することなく、必
要とされる水量に見合った補給水の供給を実現して、保
有水量を一定に保持し得、しかも設備コスト、運転コス
トの低減化、及び水損失量の軽減化を果たし得る循環水
系における補給水制御装置を提供しようとするものであ
る。The present invention has been made by paying attention to such a situation, and an object thereof is to solve the problems of the above-mentioned conventional ones and to make it necessary without requiring a large drainage facility or the like. Water supply in a circulating water system that can supply makeup water in proportion to the amount of stored water, keep the amount of water held, and reduce facility cost, operating cost, and water loss It is intended to provide a device.
【0008】[0008]
【課題を解決するための手段】上記目的を達成するため
に、本発明は次のような構成の循環水系における補給水
制御装置としている。即ち、本発明に係る補給水制御装
置は、保有水量の基準値が定められていて水の流入量と
流出量との少なくともいづれか一方が調節される複数の
中継槽を含む循環冷却水系及び洗浄水系からなる循環水
系において、補給水を水量調節可能に前記循環水系に供
給する水補給手段と、各中継槽に検出部が設けられて各
保有水量を検出する保有水量検出手段と、この保有水量
検出手段が検出した各保有水量の総和と各保有水基準量
の総和とを比較し、その差に応じた供給水量に前記水補
給手段を制御する供給水量制御手段とを含んで構成され
ることを特徴とする循環水系における補給水制御装置で
ある。In order to achieve the above object, the present invention provides a makeup water control device in a circulating water system having the following configuration. That is, the makeup water control apparatus according to the present invention is a circulating cooling water system and a washing water system including a plurality of relay tanks in which a reference value of the amount of retained water is set and at least one of the inflow amount and the outflow amount of water is adjusted. In the recirculating water system, the replenishing water is supplied to the recirculating water system so that the amount of replenishment water can be adjusted, the holding water amount detecting means for detecting the respective holding water amount by providing a detecting section in each relay tank, and the holding water amount detection. Comparing the total sum of each held water amount detected by the means and the total sum of each held water reference amount, and comprising a supply water amount control means for controlling the water supply means to the supply water amount according to the difference. It is a makeup water control device in a characteristic circulating water system.
【0009】[0009]
【作用】本発明に係る循環水系における補給水制御装置
は、前記の如く、補給水を水量調節可能に循環水系に供
給する水補給手段と、循環水系の各中継槽に検出部が設
けられて各保有水量を検出する保有水量検出手段と、こ
の保有水量検出手段が検出した各保有水量の総和と各保
有水基準量の総和とを比較し、その差に応じた供給水量
に前記水補給手段を制御する供給水量制御手段とを有す
る。故に、循環水系の運転中、上記保有水量検出手段に
より保有水量の減少量を随時又は常時確実に把握し得る
と共に、その減少量に見合った補給水を供給水量制御手
段により水補給手段から供給し得る。そのため、各槽で
の水の流入量と流出量が均衡するような補給水の制御が
でき、従って、循環水系の保有水量を一定に保持し得る
と共に、補給水の過大供給を避けることができる。As described above, the makeup water control device for the circulating water system according to the present invention is provided with the water replenishing means for supplying the makeup water to the circulating water system so that the amount of the makeup water can be adjusted, and the detecting portion provided in each relay tank of the circulating water system. The retained water amount detecting means for detecting each retained water amount is compared with the total sum of the retained water amounts detected by the retained water amount detecting means and the total sum of the retained water reference amounts, and the water supply means corresponding to the difference in the supplied water amount. And a supply water amount control means for controlling. Therefore, during operation of the circulating water system, the amount of reduction of the amount of retained water can be surely or always grasped by the retained water amount detecting means, and make-up water corresponding to the reduced amount is supplied from the water supply means by the supply water amount control means. obtain. Therefore, make-up water can be controlled so that the inflow amount and the outflow amount of water in each tank are balanced. Therefore, the amount of water held in the circulating water system can be kept constant and an excessive supply of make-up water can be avoided. .
【0010】又、上記の如く循環水系の保有水量を一定
に保持し得るため、各槽の水位シミュレーションが可能
となり、各槽の送水ポンプのスイッチングアワーの定量
化も可能となる。更に、運転開始時及び停止時における
オーバフローを回避できる。従って、給水設備等を小形
化し得、設備コストの低減が図れると共に運転管理が容
易になって運転コストの低減が図れる。Further, since the amount of water held in the circulating water system can be kept constant as described above, the water level of each tank can be simulated and the switching hour of the water pump of each tank can be quantified. Furthermore, overflow at the time of starting and stopping the operation can be avoided. Therefore, the water supply equipment and the like can be downsized, the equipment cost can be reduced, and the operation management can be facilitated to reduce the operation cost.
【0011】しかも、各槽での保有水量を把握し得ると
共に調整し得るので、各槽での処理を支障なく安全に遂
行し得るようになる。Moreover, since the amount of water held in each tank can be grasped and adjusted, the treatment in each tank can be safely carried out without any trouble.
【0012】[0012]
【実施例】以下、本発明の一実施例を図面に基づき説明
する。図1に、実施例に係る圧延設備冷却用の循環水系
のブロック図を示す。この循環水系において、循環冷却
水系は、圧延設備1の冷却水通路、スケールピット2、
沈澱池3、濾過器4、冷却塔5、冷水槽6を循環的に接
続して形成されている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 shows a block diagram of a circulating water system for cooling rolling equipment according to an embodiment. In this circulating water system, the circulating cooling water system includes a cooling water passage of the rolling facility 1, a scale pit 2,
The sedimentation tank 3, the filter 4, the cooling tower 5, and the cold water tank 6 are cyclically connected to each other.
【0013】上記循環冷却水系において、圧延設備1の
ロールは冷水槽6からポンプ12によって送られてくる冷
却水で冷却される。この冷却水はロールとの熱交換によ
り温度上昇すると共に、圧延時に発生するスケールを含
有して、スケールピット2に流入する。ここでスケール
ピット2の水平断面積をA1、又、水位検出手段21によっ
て検出した水位をL1とすると、スケールピット2の保有
水量はA1×L1となる。In the circulating cooling water system, the rolls of the rolling equipment 1 are cooled by the cooling water sent from the cold water tank 6 by the pump 12. This cooling water rises in temperature due to heat exchange with the rolls, and also contains scale generated during rolling and flows into the scale pit 2. Here, if the horizontal cross-sectional area of the scale pit 2 is A1 and the water level detected by the water level detecting means 21 is L1, the amount of water held in the scale pit 2 is A1 × L1.
【0014】スケールピット2において粗スケールが殆
ど沈澱分離された後、冷却水(処理水)は細かいスケー
ルを除去するためポンプ10により沈澱池3に送られる。
一方、スケールピット2で沈澱した粗スケールはクラブ
バケット等で系外に出、それに伴ってスケール付着水も
系外に出ることになる。沈澱池3の槽の水平断面積をA
2、又、水位検出手段22によって検出した水位をL2とす
ると、該槽の保有水量はA2×L2となる。After most of the coarse scale is precipitated and separated in the scale pit 2, the cooling water (treated water) is sent to the sedimentation tank 3 by the pump 10 to remove fine scale.
On the other hand, the coarse scale settled in the scale pit 2 goes out of the system with a club bucket or the like, and the water attached to the scale goes out of the system accordingly. Set the horizontal cross-sectional area of the tank of sedimentation pond 3 to A
2, and assuming that the water level detected by the water level detecting means 22 is L2, the amount of water held in the tank is A2 × L2.
【0015】沈澱池3において沈澱した細かいスケール
は、排泥ポンプ14によりスラッジシックナー8に送ら
れ、更にポンプ16によりスレッジラグーン又は脱水機9
に送られ、脱水後のケーキは排出され、脱水作用により
出た水は再び沈澱池3に送り戻される。一方、沈澱池3
において細かいスケールの除去後の水は、更に微細なス
ケールを除去するため、濾過器4にポンプ11を介して送
られて濾過され、次いで冷却塔5に送られて大気と接触
して冷却された後、冷水槽6に流入する。このとき、冷
却塔5では蒸発及びドリフトによる系外への水排出があ
る。又、冷水槽6において水の伝導度を測定し、この結
果に基づき濾過後の水の一部は、濃縮度を一定にするた
めにブロー水として排出される。The fine scale that has settled in the settling basin 3 is sent to the sludge thickener 8 by the sludge pump 14 and further sledge lagoon or dehydrator 9 by the pump 16.
The cake after being dehydrated is discharged, and the water discharged by the dehydrating action is sent back to the settling tank 3. On the other hand, settling pond 3
In order to remove finer scales, the water after the removal of finer scales was sent to the filter 4 via the pump 11 to be filtered, and then to the cooling tower 5 to be contacted with the atmosphere and cooled. After that, it flows into the cold water tank 6. At this time, water is discharged to the outside of the system due to evaporation and drift in the cooling tower 5. Further, the conductivity of water is measured in the cold water tank 6, and based on this result, a part of the filtered water is discharged as blow water in order to keep the concentration constant.
【0016】冷水槽6の水の一部は、濾過器4の逆洗用
水として使用され、一定時間に一定量がポンプ13により
排出されて濾過器4に送り込まれる。但し、逆洗条件が
一致しないときは時間が若干変動するときもある。ここ
で冷水槽6の水平断面積をA3、又、水位検出手段23によ
って検出した水位をL3とすると、冷水槽6の保有水量は
A3×L3となる。A part of the water in the cold water tank 6 is used as backwash water for the filter 4, and a fixed amount is discharged by the pump 13 and sent to the filter 4 in a fixed time. However, when the backwash conditions do not match, the time may change slightly. Assuming that the horizontal cross-sectional area of the cold water tank 6 is A3 and the water level detected by the water level detecting means 23 is L3, the amount of water held in the cold water tank 6 is
It will be A3 x L3.
【0017】上記濾過器4での逆洗後の水は、逆洗排水
槽7に流入する。ここで逆洗排水槽7の水平断面積をA
4、又、水位検出手段24によって検出した水位をL4とす
ると、保有水量はA4×L4となる。逆洗排水槽7から逆洗
排水は一定量ずつポンプ15によりスラッジシックナー8
に送られ、凝集沈澱することによって非常に微細なスケ
ール(1〜50μm )は完全に処理され、シックナー8の
底部に堆積する。このシックナー8には前記沈澱池3か
らのスケールも流入し底部に沈澱堆積する。シックナー
8においてスケール分離された水は脱水機9の脱離水と
ともに沈澱池3の入口に再び送られる。The water that has been backwashed in the filter 4 flows into the backwash drain tank 7. Here, the horizontal cross-sectional area of the backwash drainage tank 7 is A
4, and assuming that the water level detected by the water level detecting means 24 is L4, the retained water amount is A4 × L4. A certain amount of backwash drainage from the backwash drainage tank 7 is pumped by the pump 15 to a sludge thickener 8
The very fine scale (1 to 50 μm) is completely processed by coagulation and sedimentation and is deposited on the bottom of the thickener 8. The scale from the settling tank 3 also flows into the thickener 8 and is deposited and deposited on the bottom. The water that has been scale-separated in the thickener 8 is sent again to the inlet of the settling tank 3 together with the desorbed water of the dehydrator 9.
【0018】このような循環冷却水系及び洗浄水系から
なる循環水系において、冷却対象の圧延設備1での蒸発
や、冷却塔5での蒸発やドリフト等により、冷却水が減
少するため、ブロー水を確保しつつ、補給水の供給が必
要となる。そこで、冷水槽6には、流量調節弁25を介設
して有する補給水給水管17によって実現される水補給手
段が接続され、下記の如く補給水を供給する。In the circulating water system consisting of such a circulating cooling water system and a cleaning water system, the cooling water decreases due to evaporation in the rolling facility 1 to be cooled, evaporation or drift in the cooling tower 5, etc. It is necessary to supply makeup water while ensuring it. Therefore, the cold water tank 6 is connected to a water replenishing means realized by a replenishment water supply pipe 17 having a flow rate adjusting valve 25, and supplies replenishment water as described below.
【0019】即ち、各槽の保有水量が前述の如く測定し
て求められるので、循環水系の保有水量の総和ΣQは、
ΣQ=A1×L1+A2×L2+A3×L3+A4×L4の式より求める
ことができ、このΣQを予め定めた一定値になるよう
に、水補給手段により補給水を供給する。そうすると、
各槽での水の流入量と流出量が均衡するような理想的な
補給水供給量制御システムとなる。That is, since the amount of water held in each tank is obtained by measuring as described above, the sum ΣQ of the amount of water held in the circulating water system is
ΣQ = A1 × L1 + A2 × L2 + A3 × L3 + A4 × L4 can be obtained, and the replenishing water is supplied by the water replenishing means so that ΣQ becomes a predetermined constant value. Then,
An ideal make-up water supply control system that balances the inflow and outflow of water in each tank.
【0020】かかる制御は具体的には、次のような制御
回路を使用することにより自動的に行うことができる。
即ち、図2は実施例に係る制御回路ブロック図であり、
処理部18は保有水量検出手段19と、制御手段20と、個別
水位調節手段26と、タイマー回路27とが設けられ、イン
プットポートには各水位検出手段21〜24が接続され、
又、アウトプットポートには各ポンプ10〜15のモータ及
び流量調節弁25の駆動部が接続されている。Specifically, such control can be automatically performed by using the following control circuit.
That is, FIG. 2 is a control circuit block diagram according to the embodiment,
The processing unit 18 is provided with a retained water amount detecting means 19, a control means 20, an individual water level adjusting means 26, and a timer circuit 27, and the water level detecting means 21 to 24 are connected to the input port,
The motors of the pumps 10 to 15 and the drive unit of the flow rate control valve 25 are connected to the output port.
【0021】この処理部18の動作を図3により以下説明
する。動作開始がステップS1によって成されると、タイ
マー回路27からのクロックパルス信号に基づいてステッ
プS2に移行し、各検出手段21〜24からの水位信号は保有
水量検出手段19に送り込まれる。該検出手段19は次のス
テップS3において各水槽2,3,6及び7の保有水量A1
×L1,A2×L2,A3×L3及びA4×L4を検出する。The operation of the processing unit 18 will be described below with reference to FIG. When the operation is started in step S1, the process moves to step S2 based on the clock pulse signal from the timer circuit 27, and the water level signals from the respective detecting means 21 to 24 are sent to the retained water amount detecting means 19. In the next step S3, the detecting means 19 determines the amount A1 of water held in each of the water tanks 2, 3, 6 and 7.
Detects × L1, A2 × L2, A3 × L3 and A4 × L4.
【0022】この各保有水量の値に応じて、各槽での個
別水位調節が次のステップS4で個別水位調節手段26によ
り成される。具体的には、スケールピット2ではポンプ
10を水位L1で停止し、冷水槽6では水位L3を上限100%の
レベルとして警報を発信する等の処置をとり、逆洗排水
槽7では逆洗排水ポンプ15を水位L4で停止する。The individual water level adjustment in each tank is performed by the individual water level adjusting means 26 in the next step S4 in accordance with the value of each held water amount. Specifically, pump in scale pit 2.
10 is stopped at the water level L1, the water level L3 is set at the upper limit of 100% in the cold water tank 6, and an alarm is issued, and the backwash drainage pump 15 is stopped at the water level L4 in the backwash drainage tank 7.
【0023】この個別水位調節と相前後してステップS5
で制御手段20の作動に入り、先ず、全保有水量ΣQを算
出し、次のステップS6に移行して基準保有水量ΣQ0との
比較を行わせ、ΣQ<ΣQ0であればステップS7において
流量調節弁25の開度を制御し、ΣQ0−ΣQの値に応じた
弁開度で補給水を冷水槽6に供給する。尚、保有水量の
制御範囲は計器の誤差を考慮して±2%の範囲とし、流
量調節弁25のオン・オフによりこの範囲に制御するよう
にするのが実用的である。Before and after this individual water level adjustment, step S5
In enters the operation of the control unit 20, first, calculates a fleet water [sum] Q, the process proceeds to step S6 to perform the comparison with the reference held water volume [sum] Q 0, the flow rate in step S7 if [sum] Q <[sum] Q 0 The opening degree of the control valve 25 is controlled to supply makeup water to the cold water tank 6 at a valve opening degree corresponding to the value of ΣQ 0 −ΣQ. Incidentally, it is practical that the control range of the amount of water held is set to a range of ± 2% in consideration of the error of the instrument, and the range is controlled by turning on / off the flow rate control valve 25.
【0024】以上の如くして、全保有水量ΣQが安定
し、且つ個々の水槽での水位変動が小さい理想的な補給
水供給量制御システムが実現される。As described above, an ideal makeup water supply amount control system in which the total amount of water held ΣQ is stable and the fluctuation of the water level in each water tank is small is realized.
【0025】[0025]
【発明の効果】本発明に係る循環水系における補給水制
御装置によれば、保有水量の減少量を随時又は常時確実
に把握し得ると共に、その減少量に見合った補給水を供
給し得るので、各槽での水の流入量と流出量が均衡する
ような補給水の制御ができ、従って、循環水系の保有水
量を一定に保持し得ると共に、補給水の過大供給を避け
ることができるようになる。又、各槽の水位シミュレー
ションが可能であるので、各槽送水ポンプのスイッチン
グアワーの定量化が可能となり、更に、運転開始時及び
停止時におけるオーバフローを回避でき、従って、給水
設備等を小形化し得て設備コストの低減が図れると共
に、運転管理が容易になって運転コストの低減が図れる
ようになる。しかも、各槽での保有水量を把握し得ると
共に調整し得るので、各槽での処理を支障なく安全に遂
行し得るようになる。According to the makeup water control device in the circulating water system of the present invention, the decrease amount of the retained water can be grasped at any time or at all times, and the makeup water corresponding to the decrease amount can be supplied. Make-up water can be controlled so that the inflow and outflow of water in each tank are balanced, so that the amount of water held in the circulating water system can be kept constant and an excessive supply of make-up water can be avoided. Become. In addition, since the water level of each tank can be simulated, it is possible to quantify the switching hour of the water pump for each tank, and to avoid overflows at the start and stop of operation, thus making it possible to miniaturize water supply equipment, etc. Equipment cost can be reduced, operation management can be facilitated, and operation cost can be reduced. Moreover, since the amount of water held in each tank can be grasped and adjusted, the treatment in each tank can be safely performed without any trouble.
【図1】本発明の一実施例に係る圧延設備冷却用の循環
水系を示すブロック図である。FIG. 1 is a block diagram showing a circulating water system for cooling rolling equipment according to an embodiment of the present invention.
【図2】本発明の実施例に係る制御回路ブロック図であ
る。FIG. 2 is a block diagram of a control circuit according to the embodiment of the present invention.
【図3】図2に示す処理部18の動作を説明するフローチ
ャート図である。FIG. 3 is a flowchart diagram illustrating an operation of a processing unit 18 shown in FIG.
1--圧延設備 2--スケールピット
3--沈澱池 4--濾過器 5--冷却塔
6--冷水槽 7--逆洗排水槽 8--スラッジシックナー
9--脱水機 10,11,12,13,14,15,16--ポンプ
17--補給水給水管 18--処理部 19--保有水量検出手段
20--制御手段 21,22,23,24--水位検出手段 25--
流量調節弁 26--個別水位調節手段
27--タイマー回路1--Rolling equipment 2--Scale pit
3-Sedimentation tank 4-Filter 5-Cooling tower
6--Cold water tank 7--Backwash drain tank 8--Sludge thickener
9--Dehydrator 10, 11, 12, 13, 14, 15, 16--Pump
17--Makeup water supply pipe 18--Treatment part 19--Water holding amount detection means
20--Control means 21, 22, 23, 24--Water level detection means 25--
Flow control valve 26--individual water level control means
27--timer circuit
Claims (1)
流入量と流出量との少なくともいづれか一方が調節され
る複数の中継槽を含む循環冷却水系及び洗浄水系からな
る循環水系において、補給水を水量調節可能に前記循環
水系に供給する水補給手段と、各中継槽に検出部が設け
られて各保有水量を検出する保有水量検出手段と、この
保有水量検出手段が検出した各保有水量の総和と各保有
水基準量の総和とを比較し、その差に応じた供給水量に
前記水補給手段を制御する供給水量制御手段とを含んで
構成されることを特徴とする循環水系における補給水制
御装置。1. A circulating water system including a circulating cooling water system and a wash water system, which includes a plurality of relay tanks in which a reference value of the retained water amount is set and at least one of an inflow amount and an outflow amount of water is adjusted, Water replenishing means for supplying water to the circulating water system so that the amount of water can be adjusted, holding water amount detecting means for detecting each holding water amount by providing a detection unit in each relay tank, and each holding water amount detected by this holding water amount detecting means And the sum total of the reference amount of each held water, and a supply water amount control means for controlling the water replenishing means to supply water amount according to the difference, and replenishment in the circulating water system characterized by the following: Water control device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3134763A JPH089054B2 (en) | 1991-06-06 | 1991-06-06 | Make-up water control device in circulating water system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3134763A JPH089054B2 (en) | 1991-06-06 | 1991-06-06 | Make-up water control device in circulating water system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04361821A JPH04361821A (en) | 1992-12-15 |
| JPH089054B2 true JPH089054B2 (en) | 1996-01-31 |
Family
ID=15135992
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3134763A Expired - Lifetime JPH089054B2 (en) | 1991-06-06 | 1991-06-06 | Make-up water control device in circulating water system |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH089054B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105983589A (en) * | 2015-02-25 | 2016-10-05 | 鞍钢股份有限公司 | Rinsing water control method for cleaning unit |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114477329B (en) * | 2022-02-22 | 2023-01-06 | 江苏舜维环境工程有限公司 | Cement plant integrates water treatment facilities |
| DE102022210057A1 (en) | 2022-09-23 | 2024-03-28 | Sms Group Gmbh | Method and computer program for operating a production plant for a metal product |
| CN116944265A (en) * | 2023-08-02 | 2023-10-27 | 中冶沈勘秦皇岛工程设计研究总院有限公司 | Economical and applicable treatment device for hot rolling laminar cooling water circulation system |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59169611A (en) * | 1983-03-16 | 1984-09-25 | Kobe Steel Ltd | Method for controlling shape of rolling material |
| JP3000709U (en) * | 1994-02-02 | 1994-08-16 | 政美 立柳 | Mountain burdough coarse sorter |
-
1991
- 1991-06-06 JP JP3134763A patent/JPH089054B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105983589A (en) * | 2015-02-25 | 2016-10-05 | 鞍钢股份有限公司 | Rinsing water control method for cleaning unit |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04361821A (en) | 1992-12-15 |
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