JPH06317393A - Water quality control method for circulating cooling water in cooling tower - Google Patents

Water quality control method for circulating cooling water in cooling tower

Info

Publication number
JPH06317393A
JPH06317393A JP29446092A JP29446092A JPH06317393A JP H06317393 A JPH06317393 A JP H06317393A JP 29446092 A JP29446092 A JP 29446092A JP 29446092 A JP29446092 A JP 29446092A JP H06317393 A JPH06317393 A JP H06317393A
Authority
JP
Japan
Prior art keywords
water
treatment agent
water treatment
amount
cooling
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
Application number
JP29446092A
Other languages
Japanese (ja)
Inventor
Kunio Takahashi
國男 高橋
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.)
NITSUKISOU EIKO KK
Aqua Unity Co Ltd
Nikkiso Eiko Co Ltd
Original Assignee
NITSUKISOU EIKO KK
Aqua Unity Co Ltd
Nikkiso Eiko 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 NITSUKISOU EIKO KK, Aqua Unity Co Ltd, Nikkiso Eiko Co Ltd filed Critical NITSUKISOU EIKO KK
Priority to JP29446092A priority Critical patent/JPH06317393A/en
Priority to US08/144,020 priority patent/US5403521A/en
Priority to CN93112668A priority patent/CN1094506A/en
Publication of JPH06317393A publication Critical patent/JPH06317393A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To prevent the concentration shortage of a water processing agent due to splashed water from happening by replenishing the water processing agent by a predetermined quantity in response to the quantity of splashed water by predetermined time intervals during an operation separately from a proportional injection of the water processing agent in response to a blow-down quantity. CONSTITUTION:A blow-down quantity by the operation of a blow device (upside down U-shaped siphon pipe) 6 is measured, and cooling water is replenished in response to the measured blow-down quantity. At the same time, a water processing agent is injected in circulating/cooling water of a cooling tower 1 by operating a water processing agent injecting device 12. Also, separately from the proportional injection of the water processing agent in response to the blow-down quantity, the water processing agent is replenished by a predetermined quantity in response to the quantity of splashed water by predetermined time intervals during an operation to maintain the concentration of the water processing agent in the circulating/cooling water always at a desired level. By this method, a dissipated portion of the water processing agent due to the splashed water is compensated, and a concentration shortage of the water processing agent due to splashed water can be prevented from generating.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ブロー装置及び水処理
剤注入装置を備えた冷却塔における循環冷却水の水質管
理方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water quality control method for circulating cooling water in a cooling tower equipped with a blowing device and a water treatment agent injection device.

【0002】[0002]

【従来の技術】冷却塔は一般に知られているように冷却
水を空気と直接接触させて水を蒸発させ、その潜熱によ
り水を冷却するもので、冷却水と空気とを直接接触させ
ているので、単に空気の温度を高くして熱を運ぶ空冷熱
交換器より伝熱効率がよく、小型でしかも低価格にでき
るなどの特徴をもち、従って従来大型から小型のものま
で種々の冷却塔が提案され、冷凍、空調用として実用に
供されている。ところで冷却塔の管理上において生じる
問題としては循環冷却水系に発生する腐蝕障害、スケー
ル障害及びスライム障害等があり、特に開放式循環冷却
水系では、循環冷却水の一部が冷却塔で蒸発するため、
循環冷却水中の溶存塩類は循環冷却水中で濃縮されるこ
とになる。また循環冷却水中にイオンの形態で存在する
カルシウム、シリカ等はスケール生成のもととなってい
る。これらの障害は熱交換効率を低下させるだけでなく
冷凍機や配管等を損傷させることになる。このような障
害を防止するため、循環水中に含まれる塩分やその他の
不純物の含有量を一定の値以下に保つための循環水の一
部を循環冷却水系外へ排出するブローダウン及び防食
剤、スケール防止剤等の薬剤注入が行われている。ブロ
ーダウンによる循環冷却水系の濃縮管理及び薬剤注入管
理は通常循環水の電導率を測定し、それに基づき循環水
の濃度倍率を算出し、ブロー水量を自動制御する方式が
採られている。一方防食剤やスケール防止剤等の水処理
剤は循環水中に適度な濃度を常時保持する必要があり、
この保持投入に必要な水処理剤の量は、設定した薬剤の
保持濃度に基づきブロー量、飛散損失量または補給水量
等に応じて決められ、薬剤注入装置により設定した量の
水処理剤を補給注入するようにしている。
2. Description of the Related Art As is generally known, a cooling tower cools water by directly contacting cooling water with air to evaporate the water and cool the water by its latent heat. The cooling water and the air are in direct contact with each other. Therefore, it has features such as higher heat transfer efficiency than an air-cooled heat exchanger that simply heats the air to transfer heat, can be made compact and at low cost, and therefore various cooling towers from large to small have been proposed. It is used for freezing and air conditioning. By the way, problems that occur in the management of the cooling tower include corrosion damage, scale damage and slime damage that occur in the circulating cooling water system.In particular, in the open type circulating cooling water system, part of the circulating cooling water evaporates in the cooling tower. ,
The dissolved salts in the circulating cooling water will be concentrated in the circulating cooling water. In addition, calcium, silica, etc. existing in the form of ions in the circulating cooling water are a source of scale formation. These obstacles not only reduce the heat exchange efficiency, but also damage the refrigerator, piping, and the like. To prevent such obstacles, a blowdown and an anticorrosive agent that discharges part of the circulating water to keep the content of salt and other impurities contained in the circulating water below a certain value, to the outside of the circulating cooling water system, Drugs such as scale inhibitors are injected. Concentration control and chemical injection control of the circulating cooling water system by blowdown usually employ a method of measuring the electric conductivity of circulating water, calculating the concentration ratio of circulating water based on it, and automatically controlling the amount of blown water. On the other hand, water treatment agents such as anticorrosion agents and scale inhibitors must always maintain an appropriate concentration in circulating water.
The amount of water treatment agent required for this holding and input is determined according to the amount of blown agent, the amount of scattering loss, the amount of makeup water, etc. based on the set retention concentration of the agent, and the amount of water treatment agent set by the agent injection device is replenished. I try to inject it.

【0003】ところで、水質管理、特に防食剤、スケー
ル防止剤等の薬剤注入は、冷却塔内の水槽中の循環冷却
水の導電率を定期的に測定し、その測定データに基づい
て投入量を決められるが、循環冷却水が蒸散して薬剤の
濃縮が設定された上限に達すると、導電率センサがこれ
を感知し、ブローを開始させ、薬剤の濃縮が設定された
上限より小さなディファレンシャル値以下になると、ブ
ローは停止される。従来の方法では、ブロー量と関係な
く薬剤の注入量が設定され、濃縮に関係なく定量注入ポ
ンプで設定した量の薬剤が注入されていた。そのため外
気の低い時は薬剤濃度が高く、外気温が高くなりはじめ
て規定量になるので、時期に応じて知識や経験を有する
者が注入量を決めていた。一方このような管理のできる
者がいない場合には負荷(蒸発量)の多い7〜8月頃を
基準にしてポンプ設定するのが一般的であった。そこで
先に特願平3−11956 号においてブロー量と薬剤注入量
とを直接関連させて管理する方法を提案し、それにより
薬剤の無駄をなくすと共に経時的にも水処理剤の濃度を
常にほぼ一定に保持することができるようになった。
By the way, in water quality control, especially in the injection of chemicals such as anticorrosion agents and scale inhibitors, the conductivity of the circulating cooling water in the water tank in the cooling tower is periodically measured, and the input amount is determined based on the measured data. Although it is determined, when the circulating cooling water evaporates and the concentration of the drug reaches the set upper limit, the conductivity sensor senses this and starts blowing, and the concentration of the drug is less than the differential value smaller than the set upper limit. When, the blow is stopped. In the conventional method, the injection amount of the drug is set regardless of the blow amount, and the amount of the drug set by the metering injection pump is injected regardless of the concentration. Therefore, when the outside air is low, the drug concentration is high, and the outside air temperature starts to rise to reach the prescribed amount, so that a person having knowledge and experience decides the injection amount according to the time. On the other hand, when there is no such person who can manage the pump, it is general to set the pump based on around July to August when the load (evaporation amount) is large. Therefore, in Japanese Patent Application No. 3-11956, a method of directly managing the blow amount and the chemical injection amount was proposed, thereby eliminating the waste of the chemical and keeping the concentration of the water treatment agent almost constant over time. It became possible to keep it constant.

【0004】[0004]

【発明が解決しようとする課題】上記の特許出願におい
て先に提案した、ブロー装置及び水処理剤注入装置を備
えた冷却塔における循環冷却水の水質管理方法は、ブロ
ー装置の作動によるブローダウン量を計測し、計測した
ブローダウン量に応じて水を補給すると共に水処理剤注
入装置を作動させ水処理剤を冷却塔における循環冷却水
中に注入して循環冷却水中の水処理剤の濃度を所望のレ
ベルに維持することからなっている。これにより上述の
ように、ブローダウン操作と水処理剤の注入操作とを一
連の水管理操作として自動的に実施することができ、ま
た計測したブロー装置の作動時間に比例して水処理剤注
入装置による水処理剤の注入量を設定しているので、余
分に注入する必要がなく、しかも水処理剤の濃度を常に
ほぼ一定に保持することができる。しかしながら、実際
の運転においては冷却水は循環や負荷がかかって循環蒸
発する他に冷却塔から飛散することになる。この飛散水
量は使用する冷却塔の構造や形状、或いは冷却塔の設置
場所や気象状態(例えば強風下や強風に晒され易い場
所)によって異なる。そのため上述のようなブロー量に
対して比例注入するだけでは比較的飛散の多い冷却塔の
場合にはブロー量が少ない場合に水処理剤の濃度不足が
生じるという問題点がある。そこで、本発明は、上記の
ような問題点を解決して飛散水による水処理剤の濃度不
足の発生を防止でき、冷却塔の構造に関係なくしかもあ
らゆる運転環境のもとでも循環冷却水中の水処理剤の濃
度を常に所望のレベルに維持することができる冷却塔に
おける循環冷却水の水質管理方法を提供することを目的
としている。
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention The water quality control method for circulating cooling water in a cooling tower provided with a blowing device and a water treatment agent injecting device, previously proposed in the above-mentioned patent application, includes a blowdown amount due to operation of the blowing device. The water treatment agent is supplied according to the measured blowdown amount and the water treatment agent injection device is operated to inject the water treatment agent into the circulating cooling water in the cooling tower to obtain the concentration of the water treating agent in the circulating cooling water. It consists of maintaining at the level of. As a result, as described above, the blowdown operation and the water treatment agent injection operation can be automatically performed as a series of water management operations, and the water treatment agent injection is performed in proportion to the measured operation time of the blower. Since the amount of the water treatment agent injected by the device is set, it is not necessary to inject the water treatment agent in excess, and the concentration of the water treatment agent can always be kept substantially constant. However, in the actual operation, the cooling water is circulated or loaded to circulate and evaporate, and is also scattered from the cooling tower. This amount of splashed water varies depending on the structure and shape of the cooling tower to be used, the installation location of the cooling tower, and the weather conditions (for example, strong wind down or easy exposure to strong wind). Therefore, in the case of a cooling tower in which the amount of blow is relatively large, the concentration of the water treatment agent becomes insufficient in the case of a cooling tower in which the amount of blow is relatively large. Therefore, the present invention can solve the above-mentioned problems and prevent the occurrence of insufficient concentration of the water treatment agent due to splashed water, regardless of the structure of the cooling tower, and in any operating environment, in the circulating cooling water. An object of the present invention is to provide a water quality control method for circulating cooling water in a cooling tower that can always maintain the concentration of a water treatment agent at a desired level.

【0005】[0005]

【課題を解決するための手段】上記の目的を達成するた
めに、本発明の第1の発明による、ブロー装置及び水処
理剤注入装置を備えた冷却塔における循環冷却水の水質
管理方法は、ブロー装置の作動によるブローダウン量を
計測し、この計測したブローダウン量に応じて冷却水を
補給すると共に水処理剤注入装置を作動させ水処理剤を
冷却塔における循環冷却水中に注入し、またブローダウ
ン量に応じた水処理剤の比例注入とは別個に運転中に予
定の時間間隔で水処理剤を飛散水の量に応じて予定の量
づつ補給して循環冷却水中の水処理剤の濃度を常に所望
のレベルに維持することを特徴としている。また、本発
明の第2の発明による冷却塔における循環冷却水の水質
管理方法において、ブロー装置の作動によるブローダウ
ン量を計測し、この計測したブローダウン量に応じて冷
却水を補給すると共に水処理剤注入装置を作動させ水処
理剤を冷却塔における循環冷却水中に注入し、またブロ
ーダウン量に応じた水処理剤の比例注入とは別個に運転
中に冷却水の導電率が水処理剤の初期注入時の導電率よ
り高い時に予定の時間間隔で水処理剤を飛散水の量に応
じて予定の量づつ補給して循環冷却水中の水処理剤の濃
度を常に所望のレベルに維持することを特徴としてい
る。
In order to achieve the above object, a method for controlling the quality of circulating cooling water in a cooling tower equipped with a blowing device and a water treatment agent injection device according to the first invention of the present invention is The blowdown amount due to the operation of the blow device is measured, cooling water is supplied according to the measured blowdown amount, and the water treatment agent injection device is operated to inject the water treatment agent into the circulating cooling water in the cooling tower. Separately from the proportional injection of the water treatment agent according to the blowdown amount, the water treatment agent is replenished at a predetermined time interval during operation at a predetermined time interval according to the amount of scattered water, and the amount of the water treatment agent in the circulating cooling water is increased. The feature is that the concentration is always maintained at a desired level. Further, in the water quality control method for circulating cooling water in a cooling tower according to the second aspect of the present invention, the blowdown amount due to the operation of the blower device is measured, and the cooling water is replenished according to the measured blowdown amount and the water is supplied. The treatment agent injection device is operated to inject the water treatment agent into the circulating cooling water in the cooling tower, and the conductivity of the cooling water during operation is independent of the proportional injection of the water treatment agent according to the blowdown amount. When the conductivity of the water is higher than the initial injection, the water treatment agent is replenished at a predetermined time interval at a predetermined amount according to the amount of scattered water to maintain the concentration of the water treatment agent in the circulating cooling water at a desired level at all times. It is characterized by that.

【0006】[0006]

【作用】本発明の第1の発明による方法においては、ブ
ローダウン量に応じた水処理剤の比例注入とは別個に運
転中に予定の時間間隔で水処理剤を飛散水の量に応じて
予定の量づつ補給することにより、飛散水による水処理
剤の消散分は補償され、循環冷却水中の水処理剤の濃度
を常に所望のレベルに確実に維持することができるよう
になる。また本発明の第2の発明による方法では、飛散
水に対する水処理剤の補給を、冷却水の導電率が水処理
剤の初期注入時の導電率より高い時にのみ行うようにし
たことによって、循環冷却水中の水処理剤の濃度をより
正確に所望のレベルに維持できるようになる。
In the method according to the first aspect of the present invention, the water treatment agent is adjusted at a predetermined time interval during operation separately from the proportional injection of the water treatment agent depending on the blowdown amount according to the amount of the splashed water. By replenishing the water treatment agent in a predetermined amount, the amount of the water treatment agent dissipated by the splashed water is compensated, and the concentration of the water treatment agent in the circulating cooling water can be reliably maintained at a desired level. Further, in the method according to the second aspect of the present invention, the replenishment of the water treatment agent to the splashed water is carried out only when the conductivity of the cooling water is higher than the conductivity at the time of the initial injection of the water treatment agent. The concentration of the water treatment agent in the cooling water can be more accurately maintained at a desired level.

【0007】[0007]

【実施例】以下添付図面を参照して本発明の実施例につ
いて説明する。図1には、本発明の方法を実施している
冷却塔及び水管理装置の一例を示し、1は冷却塔で、こ
の冷却塔1には冷却水の循環管路2、3及び水補給管4
が連接されている。また冷却塔1の下部水槽内にはオー
バーフロー管5が配設され、このオーバーフロー管5の
上端を跨いでブロー装置を構成している逆U字形のサイ
ホンパイプ6が取付けられ、サイホンパイプ6の一端に
は下部水槽内の冷却水をサイホンパイプ6へ送り込んで
サイホン現象を生じさせるポンプから成る水供給手段7
が取付けられ、またサイホンパイプ6の他端はオーバー
フロー管5内へ伸びている。サイホンパイプ6の屈曲し
た頂上部には空気を供給してサイホン現象を止める空気
供給管8が連通しており、この空気供給管8は適当な形
式の開閉弁9が取付けられている。水供給手段7及び空
気供給管8における開閉弁9はブロー動作制御装置10に
接続され、サイホンパイプ6によるブロー操作を制御す
るように構成されている。11は冷却水の導電率を検出す
る検出器で、この検出器11で検出された導電率を表す信
号はブロー動作制御装置10に供給される。12は防食剤や
スケール防止剤等の水処理剤を冷却水中に導入する水処
理剤注入装置であり、ブロー動作制御装置10によって動
作制御される。また13はブロー装置における水供給手段
7及び空気供給管8の開閉弁9の動作に応動して水供給
手段7の作動開始時点から開閉弁9の開放時点までのサ
イホン現象継続時間すなわちブロー時間を計測するブロ
ー時間設定用タイマー装置であり、このタイマー装置13
で計測したブロー時間信号はブロー動作制御装置10に送
られ、計測したブロー時間に比例して水処理剤注入装置
12の動作を制御するのに用いられる。また、図1におい
て14は水処理剤の飛散補充動作制御装置で、この飛散補
充動作制御装置14には検出器11で検出された導電率を表
す信号が供給される。そして飛散補充動作制御装置14
は、検出器11で検出した導電率が水処理剤の初期注入時
の導電率より高い時にのみ一定の時間間隔で予定の時間
水処理剤注入装置12を作動させ、予定量の水処理剤を冷
却水中に補給させるように構成されている。この場合、
使用する冷却塔1の形状や設置場所の気象状態等を考慮
して飛散水の量を割り出し、それに基づいて飛散補充動
作制御装置14による補充動作の頻度や補充量を設定でき
るようにされている。さらに、図示してないが、ブロー
装置を構成している各要素、水処理剤注入装置、タイマ
ー装置及び各動作制御装置の電源としては同一の電源、
例えば太陽電池を用いることができ、駆動電源として太
陽電池を利用した場合には既存の冷却塔に対して特別な
電気的配線工事をする必要なしに本発明の方法を実施す
ることができる。
Embodiments of the present invention will be described below with reference to the accompanying drawings. FIG. 1 shows an example of a cooling tower and a water management apparatus for carrying out the method of the present invention. Reference numeral 1 is a cooling tower, and in this cooling tower 1, cooling water circulation pipe lines 2 and 3 and a water supply pipe are provided. Four
Are connected. Further, an overflow pipe 5 is arranged in the lower water tank of the cooling tower 1, and an inverted U-shaped siphon pipe 6 which constitutes a blower is installed across the upper end of the overflow pipe 5, and one end of the siphon pipe 6 is attached. Is a water supply means 7 including a pump for sending the cooling water in the lower water tank to the siphon pipe 6 to cause the siphon phenomenon.
Is attached, and the other end of the siphon pipe 6 extends into the overflow pipe 5. An air supply pipe 8 for supplying air to stop the siphon phenomenon communicates with the bent top of the siphon pipe 6, and an opening / closing valve 9 of an appropriate type is attached to the air supply pipe 8. The on-off valve 9 in the water supply means 7 and the air supply pipe 8 is connected to the blow operation control device 10 and is configured to control the blow operation by the siphon pipe 6. Reference numeral 11 is a detector for detecting the conductivity of the cooling water, and a signal representing the conductivity detected by the detector 11 is supplied to the blow operation control device 10. Reference numeral 12 is a water treatment agent injection device for introducing a water treatment agent such as an anticorrosive agent or a scale inhibitor into the cooling water, and its operation is controlled by the blow operation control device 10. Further, 13 is the duration of the siphon phenomenon from the start of the operation of the water supply means 7 to the opening of the open / close valve 9, that is, the blow time, in response to the operation of the water supply means 7 and the opening / closing valve 9 of the air supply pipe 8 in the blower. This is a timer device for setting the blow time to be measured.
The blow time signal measured by is sent to the blow operation control device 10, and the water treatment agent injection device is proportional to the blow time measured.
Used to control 12 movements. Further, in FIG. 1, reference numeral 14 is a splash replenishment operation control device for the water treatment agent, and the splash replenishment operation control device 14 is supplied with a signal representing the conductivity detected by the detector 11. And the scattering supplement operation control device 14
Is only when the conductivity detected by the detector 11 is higher than the conductivity at the time of the initial injection of the water treatment agent, the water treatment agent injection device 12 is operated at a predetermined time interval at a predetermined time interval, and a predetermined amount of the water treatment agent is supplied. It is configured to be supplied in cooling water. in this case,
The amount of splashed water is calculated in consideration of the shape of the cooling tower 1 to be used, the weather condition of the installation location, etc., and the frequency and amount of replenishment operation by the splash replenishment operation control device 14 can be set based on that. . Further, although not shown, the same power source is used as the power source of each element constituting the blowing device, the water treatment agent injection device, the timer device and each operation control device,
For example, a solar cell can be used, and when the solar cell is used as a driving power source, the method of the present invention can be carried out without the need for special electrical wiring work for an existing cooling tower.

【0008】このように構成した装置を用いて実際に冷
却水を管理する操作について説明する。比例注入動作に
関しては、検出器11で検出された冷却水の導電率に基づ
き予め設定されたブロー必要量に応じてブロー動作制御
装置10からブロー装置の水供給手段7へブロー開始制御
信号が送られ、水供給手段7は作動され、下部水槽内の
冷却水をサイホンパイプ6へ送り込んでサイホン現象を
生じさせる。この場合サイホンパイプ6内にサイホン現
象が生じるや否や水供給手段7は停止するようにされて
いる。こうしてサイホンパイプ6を介して冷却水のブロ
ーが開始され、ブローが予定量に達するとブロー動作制
御装置10からブロー終了制御信号により空気供給管8の
開閉弁9が開放され、空気供給管8を介してサイホンパ
イプ6内に空気が供給され、サイホン現象を停止させ、
ブロー操作は終了する。この間タイマー装置13は実際の
ブロー時間を計測し、そのブロー時間はブロー動作制御
装置10に送られる。ブロー動作制御装置10では実際に計
測したブロー時間に応じて水処理剤注入装置12へ水処理
剤注入命令信号を供給し、水処理剤注入装置12を作動さ
せそれにより実際に計測したブロー時間に比例した水処
理剤を冷却水中に注入させる。この場合、継続投入量
は、冷却水配管循環冷却水中の濃度が薬剤効果を発揮す
る下限濃度以上例えば200PPMとなるように設定され得
る。また、当然ブロー量に相応して水補給管4を介して
必要量の補給水が供給される。
The operation of actually managing the cooling water by using the apparatus configured as described above will be described. Regarding the proportional injection operation, a blow start control signal is sent from the blow operation control device 10 to the water supply means 7 of the blow device in accordance with a preset required blow amount based on the conductivity of the cooling water detected by the detector 11. Then, the water supply means 7 is operated and the cooling water in the lower water tank is sent to the siphon pipe 6 to cause the siphon phenomenon. In this case, the water supply means 7 is stopped as soon as the siphon phenomenon occurs in the siphon pipe 6. In this way, the blowing of the cooling water is started via the siphon pipe 6, and when the blowing reaches the predetermined amount, the opening / closing valve 9 of the air supply pipe 8 is opened by the blow end control signal from the blow operation control device 10, and the air supply pipe 8 is opened. Air is supplied to the inside of the siphon pipe 6 to stop the siphon phenomenon,
The blow operation ends. During this time, the timer device 13 measures the actual blow time, and the blow time is sent to the blow operation control device 10. In the blow operation control device 10, the water treatment agent injection command signal is supplied to the water treatment agent injection device 12 according to the actually measured blow time, and the water treatment agent injection device 12 is operated, whereby the blow time actually measured is set. A proportional water treatment agent is injected into the cooling water. In this case, the continuous injection amount can be set so that the concentration in the cooling water circulating the cooling water is equal to or higher than the lower limit concentration for exerting the drug effect, for example, 200 PPM. Naturally, the required amount of makeup water is supplied through the water supplement pipe 4 in accordance with the blow amount.

【0009】次に飛散補充動作に関しては、検出器11で
検出した導電率が水処理剤の初期注入時の導電率より高
い時にのみ飛散補充動作制御装置14が作動される。飛散
補充動作制御装置14においては、使用する冷却塔の形状
や設置場所の気象状況(例えば比較的強い風が常時吹い
ている等)に基づき予め計算した運転中の飛散水の量に
応じて例えば10%、20%、30%と補充すべき水処理剤の
量が設定されており、従って飛散補充動作制御装置14は
設定した補充すべき水処理剤の量に対応した動作信号を
水処理剤注入装置12に供給する。それにより水処理剤注
入装置12は予定の時間間隔で設定された量の水処理剤を
冷却水中へ補充する。
Next, regarding the splash replenishment operation, the splash replenishment operation control device 14 is operated only when the conductivity detected by the detector 11 is higher than the conductivity at the time of the initial injection of the water treatment agent. In the splash replenishment operation control device 14, for example, according to the amount of splash water during operation calculated in advance based on the shape of the cooling tower to be used and the weather condition of the installation location (for example, a relatively strong wind constantly blows) The amount of the water treatment agent to be replenished is set to 10%, 20%, 30%, and accordingly, the scattering replenishment operation control device 14 outputs an operation signal corresponding to the set amount of the water treatment agent to be replenished. Supply to the injection device 12. Thereby, the water treatment agent injecting device 12 replenishes the cooling water with a set amount of the water treatment agent at predetermined time intervals.

【0010】ところで、図示実施例では水処理剤の補充
注入は、検出器11で検出した導電率が水処理剤の初期注
入時の導電率より高い時にのみ行われるように構成され
ているが、水処理剤の初期注入時の導電率に関係なく、
飛散水量に応じて予定の割合で補充注入を行うようにし
てもよい。また、上記実施例では、実際のブロー時間に
比例して水処理剤注入を設定するようにしているが、代
わりに冷却水の実際のブロー流量を例えば積算流量計で
測定し、測定したブロー流量に比例して水処理剤注入装
置12の動作を制御し、必要量の水処理剤を注入するよう
に動作制御することもできる。さらに、図示実施例で
は、水処理剤注入は下部水槽内へ行なうように示されて
いるが、当然冷却水の循環管路へ注入することもでき
る。
In the illustrated embodiment, the replenishment injection of the water treatment agent is configured to be performed only when the conductivity detected by the detector 11 is higher than the conductivity at the time of the initial injection of the water treatment agent. Regardless of the conductivity at the time of initial injection of the water treatment agent,
Replenishment injection may be performed at a predetermined rate according to the amount of splashed water. Further, in the above embodiment, the water treatment agent injection is set in proportion to the actual blow time, but instead, the actual blow flow rate of the cooling water is measured by, for example, an integrating flow meter, and the measured blow flow rate is measured. It is also possible to control the operation of the water treatment agent injecting device 12 in proportion to, and to control the operation so as to inject a necessary amount of the water treatment agent. Furthermore, in the illustrated embodiment, the water treatment agent is shown to be injected into the lower water tank, but it is of course possible to inject it into the cooling water circulation line.

【0011】[0011]

【発明の効果】以上説明してきたように、本発明によれ
ば、ブロー装置の作動によるブローダウン量を計測し、
この計測したブローダウン量に応じて水処理剤を冷却塔
における循環冷却水中に注入すると共に、飛散水の量に
応じて補充注入するように構成しているので、飛散水か
らの水処理剤の逃げを自動的に補償することができ、そ
れにより冷却水中の薬剤濃度を実質的に一定に維持する
ことができ、しかも冷却塔おける循環冷却水の水質制御
を完全自動化ることができる。その結果、年間を通じて
の水処理剤の総体使用量を大幅に削減することができる
と共に、水管理を大幅に簡素化することができるので、
装置のランニングコストの大幅な低減が期待できる。
As described above, according to the present invention, the blowdown amount by the operation of the blower is measured,
The water treatment agent is injected into the circulating cooling water in the cooling tower in accordance with the measured blowdown amount, and is configured to be supplementally injected in accordance with the amount of scattered water. The escape can be automatically compensated, whereby the drug concentration in the cooling water can be maintained substantially constant, and the water quality control of the circulating cooling water in the cooling tower can be fully automated. As a result, it is possible to significantly reduce the total amount of water treatment agent used throughout the year, and it is possible to greatly simplify water management.
It is expected that the running cost of the equipment will be greatly reduced.

【図面の簡単な説明】[Brief description of drawings]

【図1】 本発明による冷却塔における循環冷却水の水
質制御方法を実施している冷却塔の一例を示す概略線図
である。
FIG. 1 is a schematic diagram showing an example of a cooling tower implementing a water quality control method for circulating cooling water in a cooling tower according to the present invention.

【符号の説明】[Explanation of symbols]

1:冷却塔 2:冷却水の循環管路 3:冷却水の循環管路 4:水補給管 5:オーバーフロー管 6:逆U字形のサイホンパイプ 7:水供給手段 8:空気供給管 9:開閉弁 10:ブロー動作制御装置 11:冷却水の導電率の検出器 12:水処理剤注入装置 13:タイマー装置 14:飛散補充動作制御装置 1: Cooling tower 2: Cooling water circulation pipe 3: Cooling water circulation pipe 4: Water supply pipe 5: Overflow pipe 6: Reverse U-shaped siphon pipe 7: Water supply means 8: Air supply pipe 9: Open / close Valve 10: Blow operation control device 11: Cooling water conductivity detector 12: Water treatment agent injection device 13: Timer device 14: Scattering replenishment operation control device

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】ブロー装置及び水処理剤注入装置を備えた
冷却塔における循環冷却水の水質管理方法において、ブ
ロー装置の作動によるブローダウン量を計測し、この計
測したブローダウン量に応じて冷却水を補給すると共に
水処理剤注入装置を作動させ水処理剤を冷却塔における
循環冷却水中に注入し、またブローダウン量に応じた水
処理剤の比例注入とは別個に運転中に予定の時間間隔で
水処理剤を飛散水の量に応じて予定の量づつ補給して循
環冷却水中の水処理剤の濃度を常に所望のレベルに維持
することを特徴とする冷却塔における循環冷却水の水質
管理方法。
1. A method for controlling the quality of circulating cooling water in a cooling tower equipped with a blower and a water treatment agent injection device, in which the blowdown amount due to operation of the blow device is measured, and cooling is performed according to the measured blowdown amount. Water is replenished and the water treatment agent injection device is operated to inject the water treatment agent into the circulating cooling water in the cooling tower, and the scheduled time during the operation is independent from the proportional injection of the water treatment agent according to the blowdown amount. The water quality of the circulating cooling water in the cooling tower is characterized in that the concentration of the water treating agent in the circulating cooling water is constantly maintained at a desired level by replenishing the water treating agent at a predetermined amount according to the amount of scattered water at intervals. Management method.
【請求項2】ブロー装置及び水処理剤注入装置を備えた
冷却塔における循環冷却水の水質管理方法において、ブ
ロー装置の作動によるブローダウン量を計測し、この計
測したブローダウン量に応じて冷却水を補給すると共に
水処理剤注入装置を作動させ水処理剤を冷却塔における
循環冷却水中に注入し、またブローダウン量に応じた水
処理剤の比例注入とは別個に運転中に冷却水の導電率が
水処理剤の初期注入時の導電率より高い時に予定の時間
間隔で水処理剤を飛散水の量に応じて予定の量づつ補給
して循環冷却水中の水処理剤の濃度を常に所望のレベル
に維持することを特徴とする冷却塔における循環冷却水
の水質管理方法。
2. A water quality control method for circulating cooling water in a cooling tower equipped with a blower and a water treatment agent injection device, in which the blowdown amount due to the operation of the blow device is measured, and cooling is performed according to the measured blowdown amount. Water is replenished and the water treatment agent injection device is operated to inject the water treatment agent into the circulating cooling water in the cooling tower, and the cooling water during operation is separated from the proportional injection of the water treatment agent according to the blowdown amount. When the conductivity is higher than the conductivity at the time of initial injection of the water treatment agent, the water treatment agent is replenished at a predetermined time interval in accordance with the amount of scattered water at a predetermined amount to constantly maintain the concentration of the water treatment agent in the circulating cooling water. A water quality control method for circulating cooling water in a cooling tower, which is characterized by maintaining a desired level.
JP29446092A 1992-11-02 1992-11-02 Water quality control method for circulating cooling water in cooling tower Pending JPH06317393A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP29446092A JPH06317393A (en) 1992-11-02 1992-11-02 Water quality control method for circulating cooling water in cooling tower
US08/144,020 US5403521A (en) 1992-11-02 1993-11-01 Blow system and a method of use therefor in controlling the quality of recycle cooling water in a cooling tower
CN93112668A CN1094506A (en) 1992-11-02 1993-11-02 A kind of method of controlling recirculated cooling water amount in the cooling tower

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29446092A JPH06317393A (en) 1992-11-02 1992-11-02 Water quality control method for circulating cooling water in cooling tower

Publications (1)

Publication Number Publication Date
JPH06317393A true JPH06317393A (en) 1994-11-15

Family

ID=17808071

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29446092A Pending JPH06317393A (en) 1992-11-02 1992-11-02 Water quality control method for circulating cooling water in cooling tower

Country Status (1)

Country Link
JP (1) JPH06317393A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004025036A (en) * 2002-06-25 2004-01-29 Katayama Chem Works Co Ltd System and method for controlling concentration of water treating chemicals
JP2011247447A (en) * 2010-05-24 2011-12-08 Iwaki Co Ltd Chemical feed control method and chemical feed control device
JP2013015259A (en) * 2011-07-04 2013-01-24 Miura Co Ltd Water treatment system
JP2014070744A (en) * 2012-09-27 2014-04-21 Miura Co Ltd Water treatment system
JP2014185797A (en) * 2013-03-22 2014-10-02 Miura Co Ltd Medicine feeding device
JP2019015427A (en) * 2017-07-04 2019-01-31 オルガノ株式会社 cooling tower

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0245380B2 (en) * 1981-09-29 1990-10-09 Nippon Electric Co
JPH03114598A (en) * 1989-09-29 1991-05-15 Kurita Water Ind Ltd Method and apparatus for controlling water quality of cooling water apparatus

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0245380B2 (en) * 1981-09-29 1990-10-09 Nippon Electric Co
JPH03114598A (en) * 1989-09-29 1991-05-15 Kurita Water Ind Ltd Method and apparatus for controlling water quality of cooling water apparatus

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004025036A (en) * 2002-06-25 2004-01-29 Katayama Chem Works Co Ltd System and method for controlling concentration of water treating chemicals
JP2011247447A (en) * 2010-05-24 2011-12-08 Iwaki Co Ltd Chemical feed control method and chemical feed control device
JP2013015259A (en) * 2011-07-04 2013-01-24 Miura Co Ltd Water treatment system
JP2014070744A (en) * 2012-09-27 2014-04-21 Miura Co Ltd Water treatment system
JP2014185797A (en) * 2013-03-22 2014-10-02 Miura Co Ltd Medicine feeding device
JP2019015427A (en) * 2017-07-04 2019-01-31 オルガノ株式会社 cooling tower

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