JP6471785B1 - Management system for water treatment facilities for power generation boilers - Google Patents
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 50
- 239000000126 substance Substances 0.000 claims description 7
- 238000010248 power generation Methods 0.000 claims description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 16
- 229910021529 ammonia Inorganic materials 0.000 description 8
- 230000000052 comparative effect Effects 0.000 description 5
- 238000002347 injection Methods 0.000 description 5
- 239000007924 injection Substances 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- 150000001412 amines Chemical class 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 239000003002 pH adjusting agent Substances 0.000 description 3
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 2
- PAFZNILMFXTMIY-UHFFFAOYSA-N cyclohexylamine Chemical compound NC1CCCCC1 PAFZNILMFXTMIY-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000001139 pH measurement Methods 0.000 description 2
- FAXDZWQIWUSWJH-UHFFFAOYSA-N 3-methoxypropan-1-amine Chemical compound COCCCN FAXDZWQIWUSWJH-UHFFFAOYSA-N 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000007405 data analysis Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001647 drug administration Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000012795 verification Methods 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
- F22D11/00—Feed-water supply not provided for in other main groups
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N27/00—Investigating or analysing materials by the use of electric, electrochemical, or magnetic means
- G01N27/02—Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance
- G01N27/04—Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance by investigating resistance
- G01N27/06—Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance by investigating resistance of a liquid
- G01N27/08—Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance by investigating resistance of a liquid which is flowing continuously
- G01N27/10—Investigation or analysis specially adapted for controlling or monitoring operations or for signalling
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N27/00—Investigating or analysing materials by the use of electric, electrochemical, or magnetic means
- G01N27/26—Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating electrochemical variables; by using electrolysis or electrophoresis
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N27/00—Investigating or analysing materials by the use of electric, electrochemical, or magnetic means
- G01N27/26—Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating electrochemical variables; by using electrolysis or electrophoresis
- G01N27/28—Electrolytic cell components
- G01N27/30—Electrodes, e.g. test electrodes; Half-cells
- G01N27/302—Electrodes, e.g. test electrodes; Half-cells pH sensitive, e.g. quinhydron, antimony or hydrogen electrodes
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N27/00—Investigating or analysing materials by the use of electric, electrochemical, or magnetic means
- G01N27/26—Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating electrochemical variables; by using electrolysis or electrophoresis
- G01N27/416—Systems
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
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Abstract
【課題】pH計のドリフトや校正のずれが解消されないまま、水処理管理をすることが防止され、安定した水処理管理を行うことができる水処理設備の管理システムを提供する。【解決手段】水処理設備の管理システムは、電気伝導率とpHとの相関関係を記憶する第1の記憶手段と、電気伝導率計で測定された電気伝導率と第1の記憶手段に記憶された相関関係とに基づいて理論pH値を求め、理論pH値とpH計の検出pH測定値とが所定値以上乖離した場合にpH計の校正を促す信号を発信する管理手段とを備える。【選択図】図1Provided is a water treatment facility management system capable of preventing water treatment management and eliminating stable water treatment management without eliminating a drift of pH meter and calibration deviation. A water treatment facility management system stores a first storage means for storing a correlation between electrical conductivity and pH, and an electrical conductivity measured by an electrical conductivity meter and stored in the first storage means. And a management means for obtaining a theoretical pH value based on the calculated correlation and transmitting a signal prompting calibration of the pH meter when the theoretical pH value and the detected pH measurement value of the pH meter deviate by a predetermined value or more. [Selection] Figure 1
Description
本発明は、ボイラの給水系など、pHが重要な水質管理項目となる水処理設備の管理システムに係り、詳しくは、予め設定した任意の規定温度における電気伝導率とpHとの相関関係を利用して管理を行う水処理設備の管理システムに関する。 The present invention relates to a water treatment facility management system in which pH is an important water quality management item, such as a water supply system of a boiler, and more specifically, utilizing a correlation between electrical conductivity and pH at a predetermined specified temperature. It is related with the management system of the water treatment facility which performs management.
特許文献1に示すように、設備管理システムの管理センタが、水処理設備の設備稼働情報を定期的に収集して稼動状態を管理するとともに、データベースに蓄積された参照情報を参照しながら、設備稼働情報や被処理水の分析結果に基づいて水処理設備の稼動状態を詳細に分析し、水処理設備を稼動するに有用な運転条件に関するアドバイス情報やメンテナンス情報等を作成して水処理設備側に提示することが行われている。
As shown in
現場計器の確からしさを担保できていることの検証が、水処理効果の向上に対する大きな課題となっている。例えば、発電ボイラの水処理設備の場合、pHは重要な管理項目であり、JIS B8223:2015にもその適用範囲が記載されている。特許文献2には、複数のpH計を用いて相互に校正を実施したり、電気伝導率計より換算したpH値での相関を見たりすることが記載されている。この特許文献2の場合、複数のpH計を用意してそれらの値を比較する必要があったり、サンプル温度によりpH値そのものが変動してpH値がドリフトしたりする問題がある。なお、現場のサンプル水温が常に一定になるよう冷却水量の調整等を実施するのは非常に困難である。
Verification that the certainty of field instruments can be assured is a major issue for improving the water treatment effect. For example, in the case of a water treatment facility for a power generation boiler, pH is an important management item, and its applicable range is also described in JIS B8223: 2015.
本発明は、pH計のドリフトや校正のずれが解消されないまま水処理管理をすることが防止され、安定した水処理管理を行うことができる水処理設備の管理システムを提供することを課題とする。 It is an object of the present invention to provide a water treatment facility management system capable of performing stable water treatment management by preventing water treatment management without eliminating drift and calibration deviation of a pH meter. .
本発明一態様の水処理設備の管理システムは、pH計及び電気伝導率計を有する水処理設備の管理システムにおいて、電気伝導率とpHとの相関関係を記憶する第1の記憶手段と、pHと水温との相関関係を記憶する第2の記憶手段と、電気伝導率計で測定された電気伝導率と該第1の記憶手段に記憶された該相関関係とに基づいて理論pH値を求め、前記pH計の検出pH値を、該第2の記憶手段に記憶された相関関係と水温とに基づいて規定温度のpH値に換算し、理論pH値と換算pH値とが所定値以上乖離した場合にpH計の校正を促す信号を発信する管理手段とを備えたことを特徴とする。 The water treatment facility management system according to one aspect of the present invention is a water treatment facility management system having a pH meter and an electrical conductivity meter, wherein the first storage means stores the correlation between the electrical conductivity and the pH, and the pH The theoretical pH value is obtained based on the second storage means for storing the correlation between the water temperature and the water temperature, the electrical conductivity measured by the electrical conductivity meter, and the correlation stored in the first storage means. The detected pH value of the pH meter is converted into a pH value of a specified temperature based on the correlation stored in the second storage means and the water temperature, and the theoretical pH value and the converted pH value are different from each other by a predetermined value or more. And a management means for transmitting a signal for prompting calibration of the pH meter.
本発明の一態様の水処理設備の管理システムは、電気伝導率計を有する水処理設備の管理システムにおいて、規定温度における電気伝導率とpHとの相関関係を記憶する記憶手段と、電気伝導率計で測定された電気伝導率と該記憶手段に記憶された該相関関係とに基づいてpH値を求める手段とを備えたことを特徴とする。 A water treatment facility management system according to one aspect of the present invention is a water treatment facility management system having an electrical conductivity meter, a storage unit that stores a correlation between electrical conductivity at a specified temperature and pH, and electrical conductivity. And a means for obtaining a pH value based on the electrical conductivity measured by the meter and the correlation stored in the storage means.
本発明の一態様では、前記規定温度が25℃である。 In one embodiment of the present invention, the specified temperature is 25 ° C.
本発明の一態様では、前記水処理設備はボイラ給水を対象とする。 In one aspect of the present invention, the water treatment facility is intended for boiler water supply.
本発明の一態様では、前記管理手段は、薬注量の調整又はブロー量の調整を含むアドバイス信号を発信する。 In one aspect of the present invention, the management means transmits an advice signal including adjustment of a chemical injection amount or adjustment of a blow amount.
本発明によれば、規定温度下のpHに換算されたpHが、電気伝導率から求められたpH値から所定値以上乖離した際に校正を促す表示がなされたり、電気伝導率からpHを推定したりすることにより、誤差の大きなpH測定値に基づいた水処理管理が防止され、安定した水処理管理が行われるようになる。 According to the present invention, when the pH converted to the pH at the specified temperature deviates by a predetermined value or more from the pH value obtained from the electrical conductivity, a display prompting calibration is made, or the pH is estimated from the electrical conductivity. By doing so, water treatment management based on a pH measurement value having a large error is prevented, and stable water treatment management is performed.
以下、図面を参照して実施の形態について説明する。図1は本発明の水処理設備の管理システムの一例を示している。水処理設備(例えば発電ボイラ用水処理設備)1では、薬注装置2によって、アンモニア、中和性アミン、ヒドラジンなどのアルカリ性の薬剤が添加注入されている。
Hereinafter, embodiments will be described with reference to the drawings. FIG. 1 shows an example of a water treatment facility management system of the present invention. In a water treatment facility (for example, a water treatment facility for a power generation boiler) 1, an alkaline agent such as ammonia, neutralizing amine, hydrazine is added and injected by a
水処理設備1の水質を管理する現場計器3の一部として、pH計、電気伝導率計、水温計等が設置されており、これらのデータが判定装置(例えばPLC)4に伝送される。判定装置4には判定部、表示部及び送信部が設けられており、pH計で測定されたpH値を規定温度のpH値に換算し、この換算pH値が、電気伝導率から求められた理論pH値から乖離していないことを確認しながら、管理センタ5にデータを伝送する。管理センタ5ではこれらの情報を蓄積し、従来と異なる場合には、予めデータ解析部に登録していた現象と比較し、薬液注入量の調整や、ボイラ水のブロー量の調整等のアドバイスをアドバイス表示部6で表示するものとなっている。アドバイス表示部6としては、パソコンや携帯端末などが用いられる。
A pH meter, an electric conductivity meter, a water temperature meter, and the like are installed as part of the on-site meter 3 that manages the water quality of the
判定装置4は、例えば後述の図4に示すpH−温度関係線を記憶手段で記憶しており、pH計で測定されたpH値を規定温度(好ましくは25℃)のpH値に換算した換算pH値が、電気伝導率計の電気伝導率から求めた理論pH値から乖離した場合に、校正を促すアドバイス表示を表示部に表示させるとともに、管理センタ5にも同内容を伝送する。これにより、管理センタ5経由で、アドバイス表示部6にも同様のアドバイス表示が行われる。この表示はメール送信されるものであってもよいし、特定のWEB画面に表示させ、このWEB画面へアクセスして知得するものであってもよい。
The
現場のpH計が、劣化・破損等によってpH測定値の誤差(電気伝導率計の電気伝導率に基づいて演算された理論pH値からの乖離)が大きくなっている場合には、判定装置4の判定表示部で電気伝導率から換算した理論pH値を表示するとともに、管理センタ5に伝送する構成としてもよい。
When the on-site pH meter has a large error in the measured pH value (deviation from the theoretical pH value calculated based on the electrical conductivity of the electrical conductivity meter) due to deterioration, damage, etc., the
pH値と電気伝導率との相関関係線は、20℃や30℃などの温度におけるものでもよいが、ボイラの水管理を念頭に置いた場合は、例えばJIS B8223(2015)に準拠できるよう25℃における相関関係線とするのが好ましい。 The correlation line between the pH value and the electrical conductivity may be at a temperature such as 20 ° C. or 30 ° C. However, when the water management of the boiler is taken into consideration, for example, 25 in order to comply with JIS B8223 (2015). It is preferable to use a correlation line at ° C.
電気伝導率計によって測定される電気伝導率は、pH値と比較して温度(水温)の影響が小さいので、温度換算しなくても良いが、より正確に測定するためには電極付属の温度換算機能等で補正することが好ましい。 The electrical conductivity measured by the electrical conductivity meter is less affected by the temperature (water temperature) compared to the pH value, so it is not necessary to convert the temperature, but for more accurate measurement, the temperature attached to the electrode It is preferable to correct by a conversion function or the like.
本実施形態では、上記の通り、pH計の測定pH値を規定温度のpH値に換算し、この換算pH値が、電気伝導率から求まる理論pH値から所定値以上乖離する場合に校正指示表示を行う。この乖離の所定値は、好ましくは0.1〜0.5の間から選択された値、例えば0.3好ましくは0.2程度とされる。 In the present embodiment, as described above, the measured pH value of the pH meter is converted into the pH value of the specified temperature, and when the converted pH value deviates from the theoretical pH value obtained from the electrical conductivity by a predetermined value or more, the calibration instruction display I do. The predetermined value of the deviation is preferably a value selected from 0.1 to 0.5, for example, 0.3 is preferably about 0.2.
アドバイス表示には、pH計や電気伝導率計に基づく表示だけでなく、より微量な測定計器を用いた結果を含めてもよい。 The advice display may include not only a display based on a pH meter and an electric conductivity meter but also a result using a smaller amount of measurement instrument.
pH計の校正を促すアドバイス表示のための信号は、例えば1時間おきの定期的なデータ転送と併せて送信するものであっても良いが、pH測定値が理論値から所定値以上乖離した際に遅滞なく送信されるのが好ましい。pH計の校正中に校正を促すアドバイスが発生しないように、校正中ボタンを設けるか、一定期間以内(例えば30分間)は校正を促す信号を発報しない仕組み等を設けても良い。 For example, the advice display signal that prompts the calibration of the pH meter may be transmitted together with periodic data transfer every hour, but when the measured pH value deviates from the theoretical value by a predetermined value or more. Is preferably transmitted without delay. A calibration button may be provided, or a mechanism that does not issue a signal prompting calibration within a certain period (for example, 30 minutes) may be provided so that advice for prompting calibration is not generated during calibration of the pH meter.
[測定例1]
ボイラ給水のpH調整剤として、アンモニアや各種アミンが使用されている。そこで、アンモニア、3−メトキシプロピルアミン又はシクロヘキシルアミンを種々の濃度で添加したボイラ給水の25℃におけるpHと電気伝導率を測定し、両者の関係(相関関係線)を図2に示した。図2の通り、pH調整剤の種類毎に、電気伝導率の対数値とpHとは直線関係にある。従って、pH計によるpH測定値のドリフト(実施例1で後述)や温度による誤差(実施例2で後述)が大きい場合、電気伝導率に基づいてpH計の測定値を補正することにより、誤差を解消したり小さくしたりすることができる。
[Measurement Example 1]
Ammonia and various amines are used as a pH adjuster for boiler feedwater. Therefore, the pH and electrical conductivity at 25 ° C. of boiler feed water to which ammonia, 3-methoxypropylamine or cyclohexylamine was added at various concentrations were measured, and the relationship between them (correlation line) is shown in FIG. As shown in FIG. 2, the logarithmic value of electrical conductivity and pH are in a linear relationship for each type of pH adjuster. Accordingly, when the pH measurement value drift by the pH meter (described later in Example 1) and the error due to temperature (described later in Example 2) are large, the error is obtained by correcting the measured value of the pH meter based on the electrical conductivity. Can be eliminated or reduced.
なお、図2は、各pH調整剤を1種類だけボイラ給水に添加した場合の相関関係線を示しているが、複数のアミンやアンモニアを組合わせて添加する場合にも同様にして相関関係線を求めておき、電気伝導率に基づく理論pH値をこの相関関係線に基づいて求めることができる。 FIG. 2 shows a correlation line when only one type of each pH adjuster is added to the boiler feed water. However, the correlation line is similarly applied when a plurality of amines and ammonia are added in combination. And the theoretical pH value based on the electrical conductivity can be obtained based on this correlation line.
[比較例1、実施例1]
ボイラ給水のpH調整にアンモニアを用いているボイラでの検討結果を図3に示す。
[Comparative Example 1, Example 1]
The examination result in the boiler which uses ammonia for pH adjustment of boiler feed water is shown in FIG.
この比較例1及び実施例1で用いたpH計は、pH測定値が負の方にドリフトする特性を有するものであった。 The pH meter used in Comparative Example 1 and Example 1 had a characteristic that the measured pH value drifted in the negative direction.
図3の左半側に比較例1の結果を示す。比較例1では、pH計を従来通り1ヶ月に一度校正しているが、温度換算を実施していない。この比較例1では、pHが負の方向にドリフトしていたことに気づかず、アンモニアの添加量を増加させていたため、見かけ上のpH(pH計測定値)は一定値で推移していたが、実際には系内のアンモニア濃度が高くなっており、復水器でのアンモニアアタックの懸念が発生していた。 The result of Comparative Example 1 is shown on the left half side of FIG. In Comparative Example 1, the pH meter is calibrated once a month as usual, but temperature conversion is not performed. In Comparative Example 1, the pH was drifting in the negative direction, and the amount of ammonia added was increased, so that the apparent pH (pH meter measured value) was a constant value, Actually, the ammonia concentration in the system was high, and there was a concern about ammonia attack in the condenser.
図3の右半側に実施例1の結果を示す。図示の通り、本発明法を利用した場合は、電気伝導率から換算した25℃のpHで管理したため、2ヶ月を経過する間、実際のpHは一定に保たれ、適切な薬注管理が継続された。 The result of Example 1 is shown on the right half side of FIG. As shown in the figure, when using the method of the present invention, the pH was controlled at 25 ° C. converted from the electrical conductivity, so the actual pH was kept constant for 2 months, and appropriate drug administration management continued. It was done.
以上より、予め測定したpHと電気伝導率の相関関係線に基づいて、電気伝導率測定値からpH値を推定する方法の有用性が確認された。 From the above, the usefulness of the method for estimating the pH value from the measured value of electrical conductivity was confirmed based on the correlation line between pH and electrical conductivity measured in advance.
[実施例2]
ボイラ給水の温度を18〜35℃の範囲で変化させ、pH値を測定した。結果を図4に示す。図4の通り、温度とpHとの間には直線関係が存在する。従って、25℃以外の温度で測定したpH値であっても、換算式を用いることで25℃のpH値に換算できることが明らかになった。
[Example 2]
The temperature of the boiler feed water was changed in the range of 18 to 35 ° C., and the pH value was measured. The results are shown in FIG. As shown in FIG. 4, there is a linear relationship between temperature and pH. Therefore, it was revealed that even a pH value measured at a temperature other than 25 ° C. can be converted to a pH value of 25 ° C. by using a conversion formula.
25℃に換算したpH値に基づいて薬注制御することにより、より適正な薬品注入量の調整が可能となる。なお、図4の換算式は次の通りである。
pH[at25℃]=pH[atM℃]+(M−25)×0.035
By controlling the chemical injection based on the pH value converted to 25 ° C., it is possible to adjust the chemical injection amount more appropriately. In addition, the conversion formula of FIG. 4 is as follows.
pH [at 25 ° C.] = pH [at M ° C.] + (M−25) × 0.035
1 水処理設備
4 測定装置
5 管理センタ
6 アドバイス表示部
1
Claims (3)
電気伝導率とpHとの相関関係を記憶する第1の記憶手段と、
pHと水温との相関関係を記憶する第2の記憶手段と、
電気伝導率計で測定された電気伝導率と該第1の記憶手段に記憶された該相関関係とに基づいて理論pH値を求め、前記pH計の検出pH値を、該第2の記憶手段に記憶された相関関係と水温とに基づいて規定温度である25℃のpH値に換算し、理論pH値と換算pH値とが、0.1〜0.5の間から選択された所定値以上乖離した場合にpH計の校正を促す信号を発信する管理手段と
を備えたことを特徴とする発電ボイラ用水処理設備の管理システム。 In the management system of the power boiler water treatment facility with a pH meter and conductivity meter,
First storage means for storing a correlation between electrical conductivity and pH;
second storage means for storing the correlation between pH and water temperature;
A theoretical pH value is obtained based on the electrical conductivity measured by the electrical conductivity meter and the correlation stored in the first storage means, and the detected pH value of the pH meter is used as the second storage means. Is converted into a pH value of 25 ° C. , which is the specified temperature , based on the correlation stored in the water temperature and the water temperature , and the theoretical pH value and the converted pH value are selected from 0.1 to 0.5 management system water treatment facility for power generation boiler, characterized in that it comprises a managing means for transmitting a signal for prompting the calibration of the pH meter when deviation above.
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KR1020207004355A KR102603844B1 (en) | 2017-09-07 | 2018-07-31 | Management system for water treatment facilities |
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JP2007268397A (en) * | 2006-03-31 | 2007-10-18 | Kurita Water Ind Ltd | Pure water supply boiler water system treatment method and treatment apparatus |
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