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JP5736607B2 - Chemical injection control method and chemical injection control device - Google Patents

Chemical injection control method and chemical injection control device Download PDF

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JP5736607B2
JP5736607B2 JP2010118151A JP2010118151A JP5736607B2 JP 5736607 B2 JP5736607 B2 JP 5736607B2 JP 2010118151 A JP2010118151 A JP 2010118151A JP 2010118151 A JP2010118151 A JP 2010118151A JP 5736607 B2 JP5736607 B2 JP 5736607B2
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chemical injection
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JP2011247447A (en
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祐一 高堀
祐一 高堀
啓一 大友
啓一 大友
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Iwaki Co Ltd
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Description

この発明は、開放循環冷却水系の循環冷却水への水処理薬剤の薬注制御方法及び薬注制御装置に関する。   The present invention relates to a chemical injection control method and a chemical injection control device for a water treatment chemical to circulating cooling water in an open circulating cooling water system.

いわゆる開放循環冷却水系のシステムでは、冷却塔内に空気を強制的に取り込んで、冷凍機等の熱交換器から送られて来た循環冷却水とこの空気とを気液接触させることで、循環冷却水の一部を蒸発させて冷却することが行われている。循環冷却水は、熱交換器と冷却塔との間を循環利用されるため、腐食、スケール、スライムなどの障害が発生しやすく、これらの障害を防ぐために、種々の水処理薬剤が添加された上で使用される。   In a so-called open circulating cooling water system, air is forced into the cooling tower and the air is brought into gas-liquid contact with the circulating cooling water sent from a heat exchanger such as a refrigerator. Cooling is performed by evaporating a part of the cooling water. Since the circulating cooling water is circulated between the heat exchanger and the cooling tower, corrosion, scale, slime and other obstacles are likely to occur, and various water treatment chemicals have been added to prevent these obstacles. Used above.

水処理薬剤は、その効果を最大限に発揮するために、循環冷却水中において常時一定濃度以上を保つように管理される必要があり、そのために種々の方法により水処理薬剤を循環冷却水に注入する(薬注する)ことが行われている。例えば、下記特許文献1の薬注制御方法では、冷却塔内へ入る循環冷却水と冷却塔外へ出る循環冷却水との温度差から冷却塔の負荷を求め、この求められた負荷に基づいて水処理薬剤の薬注量を制御することが行われている。   In order to maximize the effects of water treatment chemicals, it is necessary to manage the water treatment chemicals at a constant concentration or higher at all times in the circulating cooling water. For this purpose, water treatment chemicals are injected into the circulating cooling water by various methods. To do (medicine) is done. For example, in the chemical injection control method of Patent Document 1 below, the load of the cooling tower is obtained from the temperature difference between the circulating cooling water entering the cooling tower and the circulating cooling water exiting the cooling tower, and based on the obtained load. Controlling the dose of water treatment chemicals has been carried out.

特開2009−30936号公報JP 2009-30936 A

しかしながら、上述した従来技術の薬注制御方法では、循環冷却水の蒸発損失の場合は求めた負荷に基づいてブロー水量を算出し、このブロー水量に基づき薬注量を求めるようにすると共に、飛散損失の場合は飛散損失量とブロー水量との合計量と設定薬品濃度とから薬注量を求めるようにしている。このため、水処理薬剤の薬注に関する制御が複雑になると共にシステム全体が高価になるという問題がある。また、従来の一般的な制御では、薬注動作がタイマー制御となっており、ブロー動作と薬注動作とが連動していないため、有効な薬剤濃度を維持することが困難であった。そこで、例えば循環冷却水中の薬剤濃度を直接計測して薬注を制御するものも知られているが、この場合には、システム全体が高価なものとなってしまう。   However, in the above-described conventional chemical injection control method, in the case of the evaporation loss of the circulating cooling water, the blow water amount is calculated based on the obtained load, and the chemical injection amount is obtained based on the blow water amount and scattered. In the case of loss, the chemical injection amount is obtained from the total amount of the scattering loss amount and the blow water amount and the set chemical concentration. For this reason, there are problems that the control related to the chemical injection of the water treatment chemical is complicated and the entire system is expensive. Further, in the conventional general control, the medicine injection operation is a timer control, and since the blow operation and the medicine injection operation are not interlocked, it is difficult to maintain an effective medicine concentration. Thus, for example, there is known a method that directly measures the drug concentration in the circulating cooling water to control the drug injection, but in this case, the entire system becomes expensive.

この発明は、上述した従来技術による問題点を解消するため、安価に構成可能で複雑な制御を行うことなく循環冷却水中の薬剤濃度を有効な状態に維持することができる薬注制御方法及び薬注制御装置を提供することを目的とする。   The present invention eliminates the problems caused by the prior art described above, and a chemical injection control method and a medicine capable of maintaining the chemical concentration in the circulating cooling water in an effective state without complicated control that can be configured at low cost. Note To provide a control device.

本発明に係る薬注制御方法は、開放循環冷却水系の循環冷却水に水処理薬剤を注入する薬注制御方法であって、冷却塔における前記循環冷却水のブロー動作中に、前記循環冷却水への前記水処理薬剤の薬注動作を行わないように制御することを特徴とする。   The chemical injection control method according to the present invention is a chemical injection control method for injecting a water treatment chemical into the circulating cooling water of an open circulating cooling water system, wherein the circulating cooling water is blown during the circulating cooling water blowing operation in a cooling tower. Control is performed so as not to perform the medicine pouring operation of the water treatment chemical into the water.

なお、例えば前記ブロー動作が行われた後に、前記ブロー弁の開いた時間に比例した前記薬注動作を行うように制御したり、例えば前記ブロー弁が所定時間動作していない場合に、前記循環冷却水に前記水処理薬剤を所定量注入する補助薬注動作を行うように制御したりしても良い。   For example, after the blow operation is performed, the circulation operation is controlled so as to perform the medicine injection operation proportional to the opening time of the blow valve, or when the blow valve is not operated for a predetermined time, for example, You may control to perform the auxiliary | assistant medicine injection | pouring operation | movement which inject | pours the predetermined amount of said water treatment chemical | medical agents into cooling water.

本発明に係る薬注制御装置は、開放循環冷却水系の循環冷却水への水処理薬剤の注入を制御する薬注制御装置であって、冷却塔におけるブロー弁の動作を制御するブロー弁動作制御手段と、前記循環冷却水に前記水処理薬剤を注入する薬注装置を制御する薬注制御手段とを備え、前記薬注制御手段は、前記ブロー弁動作制御手段からの信号に基づいて、前記循環冷却水のブロー動作中に、前記薬注装置に薬注動作を行わせないように制御することを特徴とする。   A chemical injection control device according to the present invention is a chemical injection control device that controls injection of a water treatment chemical into circulating cooling water in an open circulating cooling water system, and controls blow valve operation control that controls the operation of a blow valve in a cooling tower. Means and a chemical injection control means for controlling a chemical injection device for injecting the water treatment chemical into the circulating cooling water, the chemical injection control means based on the signal from the blow valve operation control means, Control is performed so that the medicine injection device does not perform the medicine injection operation during the operation of blowing the circulating cooling water.

なお、薬注制御手段は、例えば前記ブロー動作が行われた後に、前記ブロー弁の開いた時間に比例して前記薬注装置に前記薬注動作を行わせるように制御したり、例えば前記ブロー弁が所定時間動作していない場合に、前記循環冷却水に前記水処理薬剤を所定量注入する補助薬注動作を前記薬注装置に行わせるように制御したりする。   The chemical injection control means controls the chemical injection device to perform the chemical injection operation in proportion to the opening time of the blow valve after the blow operation is performed, for example, When the valve has not been operated for a predetermined time, it is controlled to cause the chemical injection device to perform an auxiliary chemical injection operation for injecting a predetermined amount of the water treatment chemical into the circulating cooling water.

本発明によれば、安価に構成可能で複雑な制御を行うことなく循環冷却水の薬剤濃度を有効な状態に維持することが可能となる。   According to the present invention, the chemical concentration of the circulating cooling water can be maintained in an effective state without complicated control that can be configured at low cost.

本発明の一実施形態に係る薬注制御方法及び薬注制御装置が適用された開放循環冷却水系の冷却設備を示す系統図である。It is a distribution diagram showing cooling equipment of an open circulation cooling water system to which a medicine injection control method and medicine injection control device concerning one embodiment of the present invention are applied. 同薬注制御装置の内部構成を示すブロック図である。It is a block diagram which shows the internal structure of the same medicine injection control apparatus. 同薬注制御方法による薬注制御処理手順の一例を示すフローチャートである。It is a flowchart which shows an example of the chemical injection control processing procedure by the chemical injection control method. 同冷却設備の動作を示す波形図である。It is a wave form diagram which shows operation | movement of the cooling equipment.

以下に、添付の図面を参照して、この発明に係る薬注制御方法及び薬注制御装置の実施の形態を詳細に説明する。   Embodiments of a chemical injection control method and a chemical injection control device according to the present invention will be described below in detail with reference to the accompanying drawings.

図1は、本発明の一実施形態に係る薬注制御方法及び薬注制御装置が適用された開放循環冷却水系の冷却設備を示す系統図、図2は同薬注制御装置の内部構成を示すブロック図である。図1に示すように、開放循環冷却水系の冷却設備は、例えば冷却塔1と、冷凍機2と、循環ポンプ3と、制御装置10と、薬注装置20とを備えて構成されている。   FIG. 1 is a system diagram showing a cooling facility of an open circulating cooling water system to which a chemical injection control method and a chemical injection control device according to an embodiment of the present invention are applied, and FIG. 2 shows an internal configuration of the chemical injection control device. It is a block diagram. As shown in FIG. 1, the cooling system of the open circulation cooling water system is configured to include, for example, a cooling tower 1, a refrigerator 2, a circulation pump 3, a control device 10, and a chemical injection device 20.

冷凍機2で昇温された循環冷却水は、冷却塔1内の散水装置4から散水されて、下部水槽6に溜まる。下部水槽6に溜まった循環冷却水は、循環ポンプ3によって冷凍機2に循環される。   The circulating cooling water heated by the refrigerator 2 is sprinkled from the sprinkler 4 in the cooling tower 1 and collected in the lower water tank 6. The circulating cooling water accumulated in the lower water tank 6 is circulated to the refrigerator 2 by the circulation pump 3.

この循環冷却水は、冷凍機2及び冷却塔1の間を循環利用されるうちに蒸発や飛散により損失される。このため、冷却塔1内における循環冷却水の蒸発損失量及びブロー弁7の動作によるブロー動作に伴うブロー水量を含む飛散損失量に相当する量の補給水が、補給弁8を通って冷却塔1内に供給される。   This circulating cooling water is lost due to evaporation and scattering while being circulated between the refrigerator 2 and the cooling tower 1. For this reason, an amount of makeup water corresponding to the amount of splash loss including the evaporation loss amount of the circulating cooling water in the cooling tower 1 and the blow water amount accompanying the blow operation by the operation of the blow valve 7 passes through the replenishment valve 8 to the 1 is supplied.

なお、下部水槽6に溜まった循環冷却水は、下部水槽6における水面が一定となるようにそのオーバーフロー分が排出管9aを通って外部に排出されると共に、排出弁9を動作させることにより強制的に外部に排出されたりする。冷却塔1内に供給される補給水は、下部水槽6の水面を一定とするように供給される。このため、上記蒸発損失量や飛散損失量が変動したり、ブロー動作が行われたりしても、冷却設備の循環冷却水の水量はほぼ一定に保たれる構造となっている。   Note that the circulating cooling water accumulated in the lower water tank 6 is discharged by operating the discharge valve 9 while the overflow is discharged to the outside through the discharge pipe 9a so that the water surface in the lower water tank 6 is constant. May be discharged to the outside. The makeup water supplied into the cooling tower 1 is supplied so that the water surface of the lower water tank 6 is kept constant. For this reason, even if the evaporation loss amount and the scattering loss amount fluctuate or the blow operation is performed, the amount of the circulating cooling water in the cooling facility is kept substantially constant.

このような冷却塔1内における水面制御は、例えば補給弁8としてボールタップ弁等を用いることで自動的に行うことができ、ブロー動作は循環冷却水の水質が劣化した際に適宜行われる。循環冷却水の水質が劣化したか否かは、公知の技術にあるように、循環冷却水の電導度を測定することにより判定することができる。   Such water level control in the cooling tower 1 can be automatically performed by using a ball tap valve or the like as the replenishment valve 8, for example, and the blow operation is appropriately performed when the quality of the circulating cooling water is deteriorated. Whether or not the quality of the circulating cooling water has deteriorated can be determined by measuring the electrical conductivity of the circulating cooling water, as is known in the art.

循環冷却水には、設備における腐食、スケール、スライム等の障害の発生を防止するために、各種の水処理薬剤が予め添加されているが、循環冷却水はこのような補給や損失を繰り返すため、循環冷却水中の薬剤濃度が有効な状態を維持できるように、薬注装置20の薬液タンク22から薬注ポンプ21によって水処理薬剤が適宜注入される。これにより、腐食、スケール、スライム等の障害の発生の防止が図られている。   Circulating cooling water is pre-added with various water treatment chemicals to prevent the occurrence of failures such as corrosion, scale, and slime in the equipment, but circulating cooling water repeats such replenishment and loss. The water treatment chemical is appropriately injected from the chemical liquid tank 22 of the chemical injection device 20 by the chemical injection pump 21 so that the chemical concentration in the circulating cooling water can be maintained. This prevents the occurrence of troubles such as corrosion, scale, slime and the like.

一方、これらの冷却設備の動作を制御する制御装置10は、例えば冷却設備全体の制御を司ると共に、内部にブロー動作制御部11、薬注動作制御部12、及び電導度測定部13を備えて構成されている。   On the other hand, the control device 10 that controls the operation of these cooling facilities controls, for example, the entire cooling facility, and includes a blow operation control unit 11, a chemical injection operation control unit 12, and an electrical conductivity measurement unit 13 therein. It is configured.

ブロー動作制御部11は、後述する電導度測定部13からの情報に基づき、ブロー弁7の動作を制御する。   The blow operation control unit 11 controls the operation of the blow valve 7 based on information from the conductivity measurement unit 13 described later.

薬注動作制御部12は、薬注装置20全体の制御を司ると共に、ブロー動作制御部11からのブロー動作に関する情報に基づいて、薬注ポンプ21の動作を制御し、薬液タンク22から水処理薬剤を循環冷却水中に注入する薬注動作を薬注装置20に行わせる。この薬注動作制御部12が制御する薬注動作の詳細は後述する。   The medicinal operation control unit 12 controls the entire medicinal injection device 20 and controls the operation of the medicinal pump 21 based on the information related to the blow operation from the blow operation control unit 11 to perform water treatment from the medicinal solution tank 22. The medicine injection device 20 is caused to perform a medicine injection operation for injecting the medicine into the circulating cooling water. Details of the drug injection operation controlled by the drug injection operation control unit 12 will be described later.

電導度測定部13は、例えば下部水槽6に取り付けられた投げ込み型の電導度センサ15a或いは循環管路に設けられた流通型の電導度センサ15bからの情報に基づいて循環冷却水の電導度を測定する。   The conductivity measuring unit 13 determines the conductivity of the circulating cooling water based on information from, for example, a throw-type conductivity sensor 15a attached to the lower water tank 6 or a flow-type conductivity sensor 15b provided in the circulation line. taking measurement.

このように構成された冷却設備における薬注制御は、例えば次のように行われる。図3は、本発明の一実施形態に係る薬注制御方法による薬注制御処理手順の一例を示すフローチャート、図4は冷却設備の動作を示す波形図である。本実施形態に係る薬注制御方法による薬注制御処理は、次の点を特徴とする。   The chemical injection control in the cooling equipment configured as described above is performed, for example, as follows. FIG. 3 is a flowchart showing an example of a chemical injection control processing procedure by the chemical injection control method according to the embodiment of the present invention, and FIG. 4 is a waveform diagram showing the operation of the cooling facility. The chemical injection control process by the chemical injection control method according to the present embodiment is characterized by the following points.

すなわち、一般的にはタイマーで行われる薬注動作を、(1)ブロー動作中には行わない、(2)ブロー動作が行われた後に、ブロー弁7の開いた時間に比例して行う、(3)ブロー弁7が所定時間動作していない場合に、水処理薬剤を所定量注入するように補助的に行うようにした点を特徴としている。   That is, the medicine injection operation generally performed by a timer is (1) not performed during the blow operation, (2) performed in proportion to the time when the blow valve 7 is opened after the blow operation is performed, (3) It is characterized in that when the blow valve 7 has not been operated for a predetermined period of time, a supplementary amount of water treatment chemical is injected.

まず、電導度測定部13によって循環冷却水の電導度が測定され、ブロー動作制御部11は、この電導度測定部13からの情報に基づいて、図4に示すように、電導度が高くなって制御開始点以上となったか否かを判定する(ステップS100)。電導度が制御開始点以上となったと判定した場合(ステップS100のY)は、ブロー動作制御部11は、ブロー弁7の動作を制御してブロー動作を行う(ステップS102)。   First, the electrical conductivity measurement unit 13 measures the electrical conductivity of the circulating cooling water, and the blow operation control unit 11 increases the electrical conductivity based on the information from the electrical conductivity measurement unit 13 as shown in FIG. It is then determined whether or not the control start point has been reached (step S100). If it is determined that the electrical conductivity is equal to or higher than the control start point (Y in step S100), the blow operation control unit 11 controls the operation of the blow valve 7 to perform the blow operation (step S102).

すなわち、公知のように循環冷却水の水質が劣化すると電導度が高くなるという性質を利用することで、ブロー動作制御部12は、この電導度が所定の制御開始点以上となった場合にブロー弁7を開けてブロー動作を行う。こうしてブロー動作が行われると、循環冷却水の水質は改善され、電導度が低下する。   That is, as is well known, by utilizing the property that the electrical conductivity increases when the water quality of the circulating cooling water deteriorates, the blow operation control unit 12 allows the blow operation control unit 12 to blow when the electrical conductivity exceeds a predetermined control start point. The valve 7 is opened and a blow operation is performed. When the blow operation is performed in this way, the quality of the circulating cooling water is improved and the electrical conductivity is lowered.

そして、ブロー動作制御部11は、電導度測定部13からの情報に基づき電導度が低くなって制御停止点以下となったか否かを判定する(ステップS104)。電導度が制御停止点以下となったと判定した場合(ステップS104のY)は、ブロー動作制御部11は、ブロー弁7の動作を制御してブロー動作を停止する(ステップS106)。   Then, the blow operation control unit 11 determines whether or not the conductivity has become lower than the control stop point based on the information from the conductivity measuring unit 13 (step S104). When it is determined that the electrical conductivity is equal to or lower than the control stop point (Y in Step S104), the blow operation control unit 11 controls the operation of the blow valve 7 and stops the blow operation (Step S106).

すなわち、公知のように循環冷却水の水質が劣化状態から改善すると電導度が低くなるため、ブロー動作制御部11は、この電導度が所定の制御停止点以下となった場合に、ブロー弁7を閉めてブロー動作を停止する。こうしてブロー動作を停止すると、循環冷却水の水質は再び劣化し始め、電導度が高くなる。   That is, as is well known, when the water quality of the circulating cooling water is improved from the deteriorated state, the conductivity is lowered. Therefore, the blow operation control unit 11 causes the blow valve 7 when the conductivity falls below a predetermined control stop point. To stop the blow operation. When the blow operation is stopped in this way, the quality of the circulating cooling water begins to deteriorate again, and the conductivity increases.

このように、冷却設備における循環冷却水の電導度の高低を判断してブロー動作が行われる場合において、従来の薬注制御方法のようにブロー動作とは無関係に水処理薬剤の薬注動作が行われると、水処理薬剤のロスが出てしまったり、循環冷却水中の薬剤濃度が過剰に上昇してしまったりして好ましくない。   As described above, when the blow operation is performed by determining the level of the electrical conductivity of the circulating cooling water in the cooling facility, the water treatment chemical injection operation is performed independently of the blow operation as in the conventional chemical injection control method. If it is carried out, loss of water treatment chemicals will occur, or the chemical concentration in the circulating cooling water will increase excessively, which is not preferable.

そこで、本実施形態に係る薬注制御処理では、上記(1)のようにブロー動作に同期して薬注動作を行わない(すなわち、ブロー動作中に薬注動作を行わない)ようにしている。具体的には、ブロー動作制御部11からの情報に基づいて、ブロー動作が停止されたら(ステップS106)、薬注動作制御部12は、図4に示すように、薬注ポンプ21を動作させて薬注動作を行う(ステップS108)。   Therefore, in the chemical injection control process according to the present embodiment, the chemical injection operation is not performed in synchronization with the blow operation as described in (1) above (that is, the chemical injection operation is not performed during the blow operation). . Specifically, based on information from the blow operation control unit 11, when the blow operation is stopped (step S106), the medicinal operation control unit 12 operates the medicinal pump 21 as shown in FIG. Then, a medicine injection operation is performed (step S108).

この時の薬注動作は、水処理薬剤を予め決められた量注入するようにしても良いし、上記(2)のようにブロー弁7の開いた時間に比例して薬注量や薬注時間を決めて行うようにしても良い。薬注動作が行われると、図4に示すように、循環冷却水中の薬剤濃度は高くなる。   The chemical injection operation at this time may be performed by injecting a predetermined amount of the water treatment chemical, or as shown in the above (2), the chemical injection amount or chemical injection is proportional to the time when the blow valve 7 is opened. You may make it decide at time. When the chemical injection operation is performed, as shown in FIG. 4, the chemical concentration in the circulating cooling water increases.

そして、薬注動作制御部12は、ブロー動作制御部11からの情報に基づき、ブロー弁7が動作しておらずブロー動作が停止している時間が所定時間Tよりも長いか否か(所定時間T以上であるか否か)を判定する(ステップS110)。図4に示すように、例えばブロー動作が行われていない場合は、冷却設備の低負荷時における循環運転が行われている場合などが相当し、ブロー動作が頻繁に行われている場合は、高負荷運転が行われている場合などが相当する。   Then, based on the information from the blow operation control unit 11, the medicine injection operation control unit 12 determines whether or not the time during which the blow valve 7 is not operating and the blow operation is stopped is longer than the predetermined time T (predetermined) It is determined whether or not it is equal to or longer than time T (step S110). As shown in FIG. 4, for example, when the blow operation is not performed, it corresponds to the case where the circulation operation is performed at a low load of the cooling facility, and when the blow operation is frequently performed, This corresponds to the case where high-load operation is performed.

ブロー動作が停止している時間が所定時間Tよりも長いと判定した場合(ステップS110のY)は、循環冷却水中の薬剤濃度が低下し続けてしまい悪影響となるため、薬注動作制御部12は、上記(3)のように水処理薬剤を循環冷却水に所定量注入するように補助的な薬注動作(補助薬注動作)を行い(ステップS112)、上記ステップS100に移行して処理を繰り返す。なお、補助薬注動作の薬注量や薬注時間は、冷却設備の各種条件によって適宜設定される。この補助薬中動作は、上記薬注動作と同様の薬注量や薬注時間であっても、異なる薬注量や薬注時間であっても良い。   If it is determined that the time during which the blow operation is stopped is longer than the predetermined time T (Y in step S110), the drug concentration in the circulating cooling water continues to decrease, resulting in an adverse effect. Performs an auxiliary medicine injection operation (auxiliary medicine injection operation) so as to inject a predetermined amount of the water treatment chemical into the circulating cooling water as in (3) above (step S112), and the process proceeds to step S100. repeat. Note that the amount and time of the auxiliary drug injection operation are appropriately set according to various conditions of the cooling facility. This auxiliary medicine operation may be the same amount or time as the above-mentioned medicine operation, or may be a different amount or time.

なお、上記ステップS100において電導度が制御開始点以上となっていないと判定した場合(ステップS100のN)は、ステップS110に移行してブロー動作が停止している時間が所定時間Tよりも長いか否かを判定する。また、上記ステップS104において電導度が制御停止点以下となっていないと判定した場合(ステップS104のN)は、ステップS102に移行してブロー動作が続行される。更に、ブロー動作が停止している時間が所定時間Tよりも短い(所定時間T未満である)と判定した場合(ステップS110のN)は、上記ステップS100に移行して処理を繰り返す。   If it is determined in step S100 that the conductivity is not equal to or higher than the control start point (N in step S100), the process proceeds to step S110 and the time during which the blowing operation is stopped is longer than the predetermined time T. It is determined whether or not. If it is determined in step S104 that the conductivity is not equal to or lower than the control stop point (N in step S104), the process proceeds to step S102 and the blowing operation is continued. Further, when it is determined that the time during which the blow operation is stopped is shorter than the predetermined time T (less than the predetermined time T) (N in step S110), the process proceeds to step S100 and the process is repeated.

このような薬注制御処理を行った結果、図4に示すように、循環冷却水中の薬剤濃度は、冷却設備の高負荷運転或いは低負荷運転に関わりなく水処理薬剤が有効な状態となる濃度を維持することが可能となった。すなわち、本実施形態に係る薬注制御処理によれば、上記(1)〜(3)のように薬注動作が行われるので、タイマー運転による薬注動作と比べて水処理薬剤が注入過多となることもなく、別途ブロー水の流量を計測する流量計などが不要であると共に水処理薬剤のロスも少なくなるので、コスト低減を図ることができ安価に構成することができる。もちろん、流量計が既設のシステムにおいても本実施形態の効果が奏されることは言うまでもない。   As a result of performing such chemical injection control processing, as shown in FIG. 4, the chemical concentration in the circulating cooling water is such that the water treatment chemical is in an effective state regardless of the high load operation or low load operation of the cooling facility. It became possible to maintain. That is, according to the chemical injection control process according to the present embodiment, since the chemical injection operation is performed as in (1) to (3) above, the water treatment chemical is excessively injected compared to the chemical injection operation by the timer operation. In addition, since a separate flow meter for measuring the flow rate of blow water is unnecessary and the loss of the water treatment chemical is reduced, the cost can be reduced and the apparatus can be configured at low cost. Of course, it goes without saying that the effect of the present embodiment can be achieved even in a system in which a flow meter is already installed.

また、ブロー動作制御部11からのブロー動作に関する情報に基づいて薬注動作制御部14がブロー動作後、或いはブロー動作停止期間が所定時間よりも長い場合に薬注動作を行うように制御するため、複雑な演算処理や制御を行うことなく循環冷却水の水処理薬剤の薬剤濃度を有効な状態に維持することができる。   In addition, based on the information regarding the blow operation from the blow operation control unit 11, the drug injection operation control unit 14 performs control so that the drug injection operation is performed after the blow operation or when the blow operation stop period is longer than a predetermined time. Further, the chemical concentration of the water treatment chemical for the circulating cooling water can be maintained in an effective state without performing complicated arithmetic processing and control.

1 冷却塔
2 冷凍機
3 循環ポンプ
4 散水装置
6 下部水槽
7 ブロー弁
8 補給弁
9 排出弁
9a 排出管
10 制御装置
11 ブロー動作制御部
12 薬注動作制御部
13 電導度測定部
15a 電導度センサ
15b 電導度センサ
20 薬注装置
21 薬注ポンプ
22 薬液タンク
DESCRIPTION OF SYMBOLS 1 Cooling tower 2 Refrigerator 3 Circulation pump 4 Sprinkling device 6 Lower water tank 7 Blow valve 8 Replenishment valve 9 Drain valve 9a Drain pipe 10 Controller 11 Blow operation control unit 12 Chemical injection operation control unit 13 Conductivity measurement unit 15a Conductivity sensor 15b Conductivity sensor 20 Chemical injection device 21 Chemical injection pump 22 Chemical solution tank

Claims (4)

開放循環冷却水系の循環冷却水に水処理薬剤を注入する薬注制御方法であって、
冷却塔におけるブロー弁の動作制御による前記循環冷却水のブロー動作中に、前記循環冷却水への前記水処理薬剤の薬注動作を行わないように制御するとともに、
前記ブロー弁が高負荷運転時における所定時間動作していない低負荷時における循環運転時に、前記循環冷却水に前記水処理薬剤を所定量注入する補助薬注動作を行うように制御する
ことを特徴とする薬注制御方法。
A chemical injection control method for injecting a water treatment chemical into circulating cooling water in an open circulating cooling water system,
During the blowing operation of the circulating cooling water by the operation control of the blow valve in the cooling tower, and controlling so as not to perform the chemical injection operation of the water treatment chemical to the circulating cooling water,
The blow valve is controlled not to operate for a predetermined time during a high load operation, and to perform an auxiliary medicine injection operation for injecting a predetermined amount of the water treatment chemical into the circulating cooling water during a low load circulation operation. A chemical injection control method characterized.
前記ブロー動作が行われた後に、前記ブロー弁の開いた時間に比例した前記薬注動作を行うように制御する
ことを特徴とする請求項1記載の薬注制御方法。
The method according to claim 1, wherein after the blow operation is performed, control is performed so as to perform the drug injection operation in proportion to a time during which the blow valve is opened.
開放循環冷却水系の循環冷却水への水処理薬剤の注入を制御する薬注制御装置であって、
冷却塔におけるブロー弁の動作を制御するブロー弁動作制御手段と、
前記循環冷却水に前記水処理薬剤を注入する薬注装置を制御する薬注制御手段とを備え、
前記薬注制御手段は、
前記ブロー弁動作制御手段からの信号に基づいて、前記循環冷却水のブロー動作中に、前記薬注装置に薬注動作を行わせないように制御するとともに、前記ブロー弁が高負荷運転時におけるブロー周期よりも長い所定時間動作していない低負荷時における循環運転時に、前記循環冷却水に前記水処理薬剤を所定量注入する補助薬注動作を前記薬注装置に行わせるように制御する
ことを特徴とする薬注制御装置。
A chemical injection control device that controls injection of a water treatment chemical into circulating cooling water in an open circulating cooling water system,
Blow valve operation control means for controlling the operation of the blow valve in the cooling tower;
A chemical injection control means for controlling a chemical injection device for injecting the water treatment chemical into the circulating cooling water,
The medicine injection control means includes
Based on the signal from the blow valve operation control means, during the blow operation of the circulating cooling water, the medicine injection device is controlled not to perform the medicine injection operation, and the blow valve is operated at the time of high load operation. Control to cause the chemical injection device to perform an auxiliary chemical injection operation for injecting a predetermined amount of the water treatment chemical into the circulating cooling water during a circulation operation at a low load that has not been operated for a predetermined time longer than a blow cycle. A chemical injection control device characterized by that.
前記薬注制御手段は、前記ブロー動作が行われた後に、前記ブロー弁の開いた時間に比例して前記薬注装置に前記薬注動作を行わせるように制御する
ことを特徴とする請求項3記載の薬注制御装置。
The said chemical injection control means controls the said chemical injection apparatus to perform the said chemical injection operation in proportion to the time when the said blow valve opened after the said blow operation was performed. 3. The chemical injection control device according to 3.
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