JPH0323637B2 - - Google Patents

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Publication number
JPH0323637B2
JPH0323637B2 JP58207373A JP20737383A JPH0323637B2 JP H0323637 B2 JPH0323637 B2 JP H0323637B2 JP 58207373 A JP58207373 A JP 58207373A JP 20737383 A JP20737383 A JP 20737383A JP H0323637 B2 JPH0323637 B2 JP H0323637B2
Authority
JP
Japan
Prior art keywords
thermal power
feed water
inlet
ultra
power plant
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
Application number
JP58207373A
Other languages
Japanese (ja)
Other versions
JPS60100688A (en
Inventor
Mamoru Suzuki
Katsumi Suzuki
Kazutoshi Ito
Akira Minato
Takeshi Kanbayashi
Shigetoshi Ono
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.)
Hitachi Ltd
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
Hitachi 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 Babcock Hitachi KK, Hitachi Ltd filed Critical Babcock Hitachi KK
Priority to JP58207373A priority Critical patent/JPS60100688A/en
Publication of JPS60100688A publication Critical patent/JPS60100688A/en
Publication of JPH0323637B2 publication Critical patent/JPH0323637B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

〔発明の利用分野〕 本発明は超々臨界圧火力発電プラントの水処理
方法に係り、特に超々臨界圧火力発電プラントの
給水系統機器及び配管等に腐食生成物の付着を防
止する方法に関する。 〔発明の背景〕 近年、火力発電プラントの効率向上の要請は最
近の化石燃料の高騰(石油は1970項頃20倍以上の
高値)と石油資源の枯渇問題からますます強まつ
ている。このことより効率の向上のため現有の超
臨界圧火力発電プラント(蒸気条件:538℃、246
Kg/cm2)よりも蒸気条件が高温高圧化した超々臨
界圧火力発電プラントの開発が急務となつてい
る。 従来の超臨界圧火力発電プラント及びその他の
発電プラントにおける系統機器及び配管等は大部
分が鉄鋼材で構成されている。また循環媒体には
高純度水を使用する。しかし、更に構成材料を防
食するために、給水のPH及びFe量を節炭器入口
で分析・測定し、その測定値に基づいて低圧給水
加熱器入口にある薬剤注入装置により微量の薬剤
(NaOH、Na3PO4、Na2HPO4、NH4OH、
N2H2)を注入することにより、給水をアルカリ
性にして系統機器及び配管等の腐食を防止してい
る。しかし、発電プラントは長年の使用により鉄
鋼材から溶出した腐食生成物(Fe3O4、γ−
Fe2O3等)がボイラ水壁管内面、タービン、高圧
給水加熱器、及び給水流量計等に付着する。付着
すると、(1)管のオーバーヒート、(2)タービン出力
の低下、(3)差圧上昇によるポンプの過負荷、(4)流
量計指示の不適等の種々の障害の原因となるの
で、定期的に腐食生成物を酸洗及びジエツト洗浄
等で除去しなければならないというような欠点が
ある。 第1図は超臨界圧火力発電プラントにおける給
水温度と腐食生成物の付着量との関係を示すもの
である。第1図より腐食生成物の付着量は給水温
度の上昇と共に増加し、特に250℃以上において
は著しく増大している、また、第2図は実験室に
おいて、Fe濃度を一定にした場合、温度とFe付
着量との関係を示す。実験は試料回転式オーバー
クレーブ中に炭素鋼を入れ、Fe濃度100ppm、溶
存酸素10ppb以下、流速2.4m/s、PH9.3、温度
50〜280℃の範囲で行ない、炭素鋼に付着したFe
量を測定した。第2図よりFeは150℃付近から付
着し始め、200℃以上になると急激に増加してい
る。この傾向は第1図に示した実機のプラントと
同様である。なお、超々臨界圧火力発電プラント
では超臨界圧火力発電プラントよりも温度、圧力
が大幅に上昇している為、超臨界圧火力発電プラ
ントでの給水の温度は高圧給水器入口で150℃前
後、節炭器入口で280℃前後であるが、超々臨界
圧火力発電プラントでの給水の温度は高圧給水器
入口で200℃以上、節炭器入口でも超臨界圧火力
発電プラントの場合よりも高い。従つて超々臨界
圧火力発電プラントでは、給水中に鉄鋼材から溶
出する腐食生成物が多くなりFe量が増加するの
で、給水系統中にある各種機器及び配管等に腐食
生成物が大量に付着し、種々の問題が発生するも
のと懸念されている。 〔発明の目的〕 本発明の目的は、前記した超々臨界圧火力発電
プラントの蒸気条件が高温高圧化するために生ず
る問題点を解決し、超々臨界圧火力発電プラント
の給水系統において腐食生成物の付着を防止する
為に効果的な水処理方法を提供することにある。 〔発明の概要〕 本発明は、超々臨界圧火力発電プラントの水処
理方法において、給水系統中に設置されている高
圧給水加熱器入口の給水のPH及びFe量を測定し、
これらの測定値に基づいて給水系統中に注入する
薬剤の注入量を制御し給水のPHを調整することを
特徴とする超々臨界圧火力発電プラントの水処理
方法にある。 本発明者等は、超々臨界圧火力発電プラントの
給水系統において、給水中のFe量の増加の抑制、
系統機器及び配管等への腐食生成物の付着の防止
を種々検討した。給水のPH、Fe量の分析・測定
は超臨界圧火力発電プラントでは器炭節入口で行
なわれるが、超々臨界圧火力発電プラントでは給
水が非常に高温高圧になるので測定が困難である
が、しかし高圧給水加熱器入口では節炭器入口よ
りも温度、圧力が低いので給水の測定を容易に行
なうことができ、この測定値に基づいて良質の水
質に調整できることを見い出した。即ちプラント
給水系統のボイラ給水ポンプと高圧給水加熱器入
口との間にある給水配管において給水のPH及び
Fe量を分析・測定し、その測定値に基づいて給
水系統中への薬剤(アンモニヤ水NH4OH、ヒド
ラジンN2H2、NaOH、Na3PO4、Na2HPO4等、
これらの中で好ましくはアンモニア水、ヒドラジ
ン)の注入量を増減することにより給水中のFe
量の増加を抑制し、系統機器及び配管等への腐食
生成物の付着を防止する方法が最も効果的である
ことを見い出して本発明を達成したものである。 次に本発明を添付図面に基づいて具体的に説明
する。第3図は超々臨界圧火力発電プラントの系
統図である。第3図において、1はタービン、2
は復水器、3は復水器ホツトウエル、4は復水配
管、5は復水ポンプ、6は復水脱塩装置、7は復
水昇圧ポンプ、8A〜8Cは低圧給水加熱器、9
は脱気器脱気室、10は脱気器貯水槽、11は給
水配管、12はボイラ給水ポンプ、13A〜13
Cは高圧給水加熱器、14は節炭器、15はボイ
ラ、16は蒸気配管、17A〜17Cは低圧給水
加熱器ドレン配管、18A〜18Cは高圧給水加
熱器ドレン配管、19はドレンポンプ、20A〜
20Fは抽気配管、21A,21Bは薬剤注入装
置を示す。 第3図における工程を説明すると、給水は復水
器2、復水器ホツトウエル3、復水配管4、復水
ポンプ5、復水脱塩装置6、復水昇圧ポンプ7、
低圧給水加熱器8A〜8C、脱気器脱気室9、脱
気器貯水槽10、給水配管11、給水ポンプ1
2、高圧給水加熱器13A〜13C、節炭器14
を経てボイラ15に入り、ここで蒸気に変換され
た後、蒸気配管16を通り、タービン1に流入し
て仕事をし、再び復水器2に戻る。 本発明者等は、実験室においてPHと腐食量の比
の関係、及びFe濃度を一定とした場合のPHとFe
付着量の比の関係を実験した。PHと腐食量の比の
関係を求める実験は、オートクレーブ中に炭素鋼
を入れ、温度280℃、溶存酸素10ppb以下、PH9.3
〜10.0の範囲で行なつた。またPHとFe付着量の比
の関係を求める実験は、試料回転式オークレーブ
に炭素鋼を組み込み、温度280℃、溶存酸素
10ppb以下、流速2.4m/s、PH9.3〜10.0の範囲で
行なつた。なお、試料液としては実機より採取し
た腐食生成物(主成分Fe3O4)を乳鉢で微粉砕し
たものを100ppm加えた。その結果、PHと腐食量
の比の関係、及びFe濃度一定とした場合のPHと
Fe付着量の比の関係は夫々第4図の曲線a、曲
線bのようになる。ここで腐食量の比はPH9.3の
腐食量の値を、Fe付着量の比はPH10.0のFe付着
量の値を夫々1.0として表わした。第4図より、
曲線aに示されるようにPHが高くなると腐食量の
比は減少し、一方曲線bに示されるようにFe付
着量の比は逆に多くなることがわかる。第4図の
点線cは前記した腐食量の比とFe付着量の比の
関係より試算したFe付着量の比であり、PHが9.5
以上9.8以上において試算したFe付着量の比が非
常に少ないことが明らかになつた。 本発明の特徴とするところは、上記の検討結果
に基づいてなされたものであり、超々臨界圧火力
発電プラント給水系統の給水中のFe量を大幅に
減少し、各種機器及び配管等への腐食生成物の付
着を防止することができるので、前記した問題点
を解決し、更に(1)プラントの性能及び効率の向
上、(2)腐食生成物除去のための酸洗間隔の延長、
(3)排水処理費の削減、(4)復水脱塩樹脂再生及び補
給費の削減効果がある。 〔発明の実施例〕 実施例 1 本発明の実施例を第3図により説明する。超々
臨界圧火力発電プラントにおいて、給水のPH及び
Fe量の分析・測定を高圧給水加熱器13A入口
で行ない、給水中のFe濃度が少なくなるように、
その測定値に基づいて高圧給水加熱器13A入口
に設けた薬剤注入装置21Bより薬剤
(NH4OH、N2H2等)を注入し給水のPHを9.5〜
9.8の範囲に調整する。本実施例によれば高圧給
水加熱器13A〜13Cに於いてFe濃度を減少
させ腐食生成物の付着量を減少させることがで
き、良質の給水を得ることができる。尚、高圧給
水加熱器13A入口及び節炭器14入口でのFe
濃度を第1表に示す。 実施例 2 超々臨界圧火力発電プラントに於いて、給水の
PH及びFe量の分析・測定を高圧給水加熱器13
A入口で行ない、その測定値に基づいて低圧給水
加熱器8A入口にある薬剤注入装置21Aより薬
剤(NH4OH、N2H2等)を注入し給水のPHを9.5
〜9.8の範囲に調整する。本実施例によれば、節
炭器14入口より下流側の給水のPHを調整するば
かりでなく、腐食生成物の付着量が多くなる高圧
給水加熱器13A〜13Cの給水のPHを調整でき
ることにより、Fe濃度を減少させ腐食生成物の
付着量を抑止でき、良質の給水を得ることができ
る。尚、第1表に高圧給水加熱器13A入口及び
炭節器14入口でのFe濃度を示す。 実施例 3 超々臨界圧火力発電プラントに於いて、給水の
PH及びFe量の分析・測定を高圧給水加熱器13
A入口で行ない、給水中のFe量が極力少なくな
るように低圧給水加熱器8A入口にある薬剤注入
装置21A及び高圧給水加熱器13A入口にある
薬剤注入装置21Bの2々所より、測定値に基づ
いて薬剤(NH4OH、N2H2等)の注入量を増減
してPHを9.5〜9.8の範囲に調整する。本実施例に
よれば、給水中のFe量を少なくすると共に、高
圧給水加熱器13A〜13Bへの腐食生成物の付
着量を大幅に減少させることができるように良質
の給水を得ることができる。尚、第1表に高圧給
水加熱器13A入口及び節炭器14入口でのFe
濃度を示す。 また、比較の為に超臨界圧火力発電プラントの
場合について述べる。節炭入口でPH及びFe量を
分析・測定し、その測定値に基づいて低圧給水加
熱器入口より薬剤(NH4OH、N2H2等)を注入
し、PHを9.4になるように調整した。尚、第1表
に高圧給水加熱器入口及び節炭器入口でのFe濃
度を示す。 第1表に示すように、本発明の実施例1、2、
3は比較例と比べると、高圧給水加熱器入口及び
節炭器入口で給水中のFe濃度が大幅に減少して
おり、従つて給水系統機器及び配管等への腐食生
成物の付着が防止される。
[Field of Application of the Invention] The present invention relates to a water treatment method for an ultra-supercritical thermal power plant, and particularly to a method for preventing corrosion products from adhering to water supply system equipment, piping, etc. of an ultra-supercritical thermal power plant. [Background of the Invention] In recent years, demands for improving the efficiency of thermal power plants have become stronger due to the recent soaring price of fossil fuels (the price of oil was more than 20 times higher around the 1970s) and the problem of depletion of oil resources. For this reason, in order to improve efficiency, the existing supercritical pressure thermal power plant (steam conditions: 538℃, 246℃
There is an urgent need to develop an ultra-supercritical thermal power plant with steam conditions that are higher in temperature and pressure than those in Japan (Kg/cm 2 ). Most of the system equipment, piping, etc. in conventional supercritical pressure thermal power plants and other power plants are made of steel. Also, high purity water is used as the circulating medium. However, in order to further prevent corrosion of the constituent materials, the PH and Fe content of the feed water is analyzed and measured at the inlet of the economizer, and based on the measured values, a trace amount of a chemical (NaOH , Na 3 PO 4 , Na 2 HPO 4 , NH 4 OH,
By injecting N 2 H 2 ), the water supply is made alkaline to prevent corrosion of system equipment and piping. However, power plants are exposed to corrosion products (Fe 3 O 4 , γ-
Fe 2 O 3 , etc.) adheres to the inner surface of boiler water wall tubes, turbines, high-pressure feed water heaters, feed water flow meters, etc. If it adheres, it can cause various problems such as (1) pipe overheating, (2) reduced turbine output, (3) pump overload due to increased differential pressure, and (4) inappropriate flowmeter indication. However, there are drawbacks such as the fact that corrosion products must be removed by pickling, jet cleaning, etc. FIG. 1 shows the relationship between the feed water temperature and the amount of corrosion products deposited in a supercritical pressure thermal power plant. Figure 1 shows that the amount of corrosion products deposited increases as the feed water temperature increases, especially at temperatures above 250°C. Figure 2 shows that when the Fe concentration is kept constant in the laboratory, The relationship between and the amount of Fe deposited is shown. In the experiment, carbon steel was placed in a sample rotating overclave, Fe concentration was 100 ppm, dissolved oxygen was 10 ppb or less, flow rate was 2.4 m/s, pH was 9.3, and temperature was
The Fe adhering to carbon steel was
The amount was measured. As shown in Figure 2, Fe begins to adhere at around 150°C, and increases rapidly above 200°C. This tendency is similar to that of the actual plant shown in FIG. Furthermore, since the temperature and pressure in ultra-supercritical thermal power plants are significantly higher than in supercritical thermal power plants, the temperature of the feed water in supercritical thermal power plants is around 150℃ at the high-pressure water supply inlet. The temperature of the feed water at the inlet of the economizer is around 280°C, but the temperature of the feed water in an ultra-supercritical thermal power plant is over 200°C at the inlet of the high-pressure water supply, which is higher than that in a supercritical thermal power plant even at the inlet of the economizer. Therefore, in ultra-supercritical thermal power plants, a large amount of corrosion products are leached from steel materials in the water supply, increasing the amount of Fe, resulting in a large amount of corrosion products adhering to various equipment and piping in the water supply system. , there are concerns that various problems will occur. [Object of the Invention] The object of the present invention is to solve the problems that arise due to the high temperature and high pressure of the steam conditions in the ultra-supercritical thermal power plant described above, and to eliminate corrosion products in the water supply system of the ultra-supercritical thermal power plant. The object of the present invention is to provide an effective water treatment method to prevent fouling. [Summary of the Invention] The present invention is a water treatment method for an ultra-supercritical thermal power plant, in which the PH and Fe content of the feed water at the inlet of a high-pressure feed water heater installed in the water supply system are measured,
The present invention provides a water treatment method for an ultra-supercritical thermal power plant, which is characterized by controlling the amount of chemicals injected into the water supply system based on these measured values and adjusting the pH of the water supply. The present inventors have developed a system for suppressing the increase in the amount of Fe in the water supply in the water supply system of an ultra-supercritical thermal power plant.
Various methods of preventing corrosion products from adhering to system equipment and piping were investigated. Analysis and measurement of the PH and Fe content of the feed water is carried out at the coal-fired inlet in supercritical pressure thermal power plants, but measurement is difficult in ultrasupercritical pressure thermal power plants because the feed water is at extremely high temperature and pressure. However, since the temperature and pressure at the inlet of the high-pressure feed water heater are lower than at the inlet of the energy saver, it has been found that the feed water can be easily measured and the water quality can be adjusted to a good quality based on the measured values. In other words, the PH and
The amount of Fe is analyzed and measured, and based on the measured value, chemicals (ammonium water NH 4 OH, hydrazine N 2 H 2 , NaOH, Na 3 PO 4 , Na 2 HPO 4 , etc.) are added to the water supply system.
Among these, Fe in the water supply can be reduced by increasing or decreasing the injection amount of aqueous ammonia or hydrazine.
The present invention was achieved by discovering that the most effective method is to suppress the increase in corrosion products and prevent the adhesion of corrosion products to system equipment, piping, etc. Next, the present invention will be specifically explained based on the accompanying drawings. Figure 3 is a system diagram of an ultra-supercritical thermal power plant. In Fig. 3, 1 is a turbine, 2
is a condenser, 3 is a condenser hot well, 4 is a condensate pipe, 5 is a condensate pump, 6 is a condensate desalination device, 7 is a condensate boost pump, 8A to 8C are low pressure feed water heaters, 9
10 is a deaerator deaeration chamber, 10 is a deaerator water tank, 11 is a water supply pipe, 12 is a boiler water supply pump, 13A to 13
C is a high pressure feed water heater, 14 is a energy saver, 15 is a boiler, 16 is a steam pipe, 17A to 17C is a low pressure feed water heater drain pipe, 18A to 18C is a high pressure feed water heater drain pipe, 19 is a drain pump, 20A ~
20F is an air bleed pipe, and 21A and 21B are drug injection devices. To explain the steps in FIG. 3, water is supplied to the condenser 2, condenser hot well 3, condensate piping 4, condensate pump 5, condensate desalination device 6, condensate boost pump 7,
Low-pressure feed water heaters 8A to 8C, deaerator deaeration chamber 9, deaerator water tank 10, water supply piping 11, water supply pump 1
2. High-pressure water heaters 13A to 13C, energy saver 14
The steam enters the boiler 15, where it is converted into steam, passes through the steam pipe 16, flows into the turbine 1, does work, and returns to the condenser 2 again. The present inventors investigated the relationship between PH and the ratio of corrosion amount in the laboratory, and the relationship between PH and Fe when the Fe concentration is constant.
An experiment was conducted to examine the relationship between the adhesion weight ratio. In an experiment to determine the relationship between PH and the ratio of corrosion amount, carbon steel was placed in an autoclave at a temperature of 280°C, dissolved oxygen of 10 ppb or less, and PH of 9.3.
~10.0. In addition, an experiment to determine the relationship between PH and the ratio of Fe adhesion was carried out using carbon steel installed in a sample rotating oaklave at a temperature of 280°C and dissolved oxygen.
The test was performed at a flow rate of 2.4 m/s at a flow rate of 10 ppb or less, and a pH range of 9.3 to 10.0. As a sample solution, 100 ppm of a corrosion product (main component Fe 3 O 4 ) collected from an actual machine was pulverized in a mortar. As a result, the relationship between PH and the ratio of corrosion amount, and the PH and
The relationship between the ratios of Fe adhesion amounts is as shown by curves a and b in FIG. 4, respectively. Here, the corrosion amount ratio is expressed as the corrosion amount value at PH9.3, and the Fe deposition amount ratio is expressed with the Fe deposition amount value at PH10.0 as 1.0. From Figure 4,
It can be seen that as the PH increases, as shown by curve a, the ratio of corrosion amount decreases, while as shown by curve b, the ratio of Fe deposition amount increases. The dotted line c in Fig. 4 is the ratio of the amount of Fe adhesion calculated from the relationship between the ratio of the amount of corrosion and the ratio of the amount of Fe adhesion described above, and the PH is 9.5.
It is clear that the ratio of Fe adhesion amount calculated above is very small for 9.8 or higher. The feature of the present invention is that it was made based on the above study results, and it significantly reduces the amount of Fe in the water supply of the ultra-supercritical thermal power plant water supply system, and prevents corrosion of various equipment and piping. Since the adhesion of products can be prevented, the above-mentioned problems can be solved, and furthermore, (1) the performance and efficiency of the plant can be improved, (2) the pickling interval for removing corrosion products can be extended,
(3) Reduces wastewater treatment costs; (4) Reduces condensate desalination resin regeneration and replenishment costs. [Embodiments of the Invention] Example 1 An embodiment of the present invention will be described with reference to FIG. In ultra-supercritical thermal power plants, the PH and
Analyze and measure the amount of Fe at the high-pressure feed water heater 13A inlet to reduce the Fe concentration in the feed water.
Based on the measured value, chemicals (NH 4 OH, N 2 H 2, etc.) are injected from the medicine injection device 21B installed at the inlet of the high-pressure feed water heater 13A to raise the pH of the water supply to 9.5 or more.
Adjust to a range of 9.8. According to this embodiment, it is possible to reduce the Fe concentration in the high-pressure feed water heaters 13A to 13C, thereby reducing the amount of corrosion products attached, and it is possible to obtain high-quality feed water. In addition, Fe at the high-pressure feed water heater 13A inlet and the energy saver 14 inlet
The concentrations are shown in Table 1. Example 2 Water supply in an ultra-supercritical thermal power plant
High-pressure feed water heater 13 for analysis and measurement of PH and Fe content
Based on the measured value, chemicals (NH 4 OH, N 2 H 2, etc.) are injected from the chemical injection device 21A at the inlet of the low-pressure feed water heater 8A to raise the pH of the feed water to 9.5.
Adjust to a range of ~9.8. According to this embodiment, it is possible to not only adjust the PH of the feed water downstream from the inlet of the energy saver 14, but also adjust the PH of the feed water of the high-pressure feed water heaters 13A to 13C, where a large amount of corrosion products adhere. , Fe concentration can be reduced, the amount of corrosion products attached can be suppressed, and high quality water supply can be obtained. Table 1 shows the Fe concentrations at the inlet of the high-pressure feed water heater 13A and the inlet of the carbon saver 14. Example 3 Water supply in an ultra-supercritical thermal power plant
High-pressure feed water heater 13 for analysis and measurement of PH and Fe content
In order to minimize the amount of Fe in the water supply, the measurement value was measured from two locations: the drug injection device 21A at the inlet of the low-pressure feed water heater 8A and the drug injection device 21B at the inlet of the high-pressure feed water heater 13A. Adjust the PH to a range of 9.5 to 9.8 by increasing or decreasing the injection amount of drugs (NH 4 OH, N 2 H 2, etc.) based on the results. According to this embodiment, it is possible to obtain high-quality feed water by reducing the amount of Fe in the feed water and by significantly reducing the amount of corrosion products adhering to the high-pressure feed water heaters 13A to 13B. . In addition, Table 1 shows Fe at the inlet of the high-pressure feed water heater 13A and the inlet of the energy saver 14.
Indicates concentration. Also, for comparison, we will discuss the case of a supercritical pressure thermal power plant. Analyze and measure the PH and Fe amount at the coal-saving inlet, and based on the measured values, inject chemicals (NH 4 OH, N 2 H 2, etc.) from the low-pressure feed water heater inlet to adjust the PH to 9.4. did. Table 1 shows the Fe concentration at the inlet of the high-pressure feed water heater and the inlet of the economizer. As shown in Table 1, Examples 1 and 2 of the present invention,
In case 3, compared to the comparative example, the Fe concentration in the feed water at the inlet of the high-pressure feed water heater and the inlet of the energy saver was significantly reduced, and therefore the adhesion of corrosion products to water supply system equipment and piping was prevented. Ru.

【表】 〔発明の効果〕 本発明によれば、超々臨界圧火力発電プラント
系統水中のFe量を大幅に減少させ、給水系統機
器及び配管等への腐食生成物の付着を防止するこ
とにより、良質の給水を得ることができる為に超
臨界圧火力発電プラントの効率を高めることがで
きる。
[Table] [Effects of the Invention] According to the present invention, by significantly reducing the amount of Fe in ultra-supercritical pressure thermal power plant system water and preventing corrosion products from adhering to water supply system equipment and piping, etc. Since high-quality water can be obtained, the efficiency of supercritical pressure thermal power plants can be increased.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は超臨界圧火力発電プラントにおける給
水温度と腐食生成物の付着量の関係を示す線図、
第2図は温度とFe付着量の関係を示す線図、第
3図は超々臨界圧火力発電プラントの系統図、及
び第4図はPHと腐食量の比の関係を曲線a、PHと
Fe付着量の比の関係を曲線b、PHと試算したFe
付着量の比の関係を曲線cで示す線図である。 1……タービン、2……復水器、6……復水脱
塩装置、8A〜8C……低圧給水加熱器、13A
〜13C……高圧給水加熱器、14……節炭器、
15……ボイラ、21A,21B……薬剤注入装
置。
Figure 1 is a diagram showing the relationship between the feed water temperature and the amount of corrosion products deposited in a supercritical pressure thermal power plant.
Figure 2 is a diagram showing the relationship between temperature and Fe deposition amount, Figure 3 is a system diagram of an ultra-supercritical thermal power plant, and Figure 4 is a diagram showing the relationship between PH and the ratio of corrosion amount with curve a and PH.
Curve b shows the relationship between the ratio of Fe adhesion amount, PH and estimated Fe
It is a diagram showing the relationship between the ratio of adhesion amounts by curve c. 1... Turbine, 2... Condenser, 6... Condensate desalination device, 8A to 8C... Low pressure feed water heater, 13A
~13C...High pressure water heater, 14...Coal economizer,
15... Boiler, 21A, 21B... Drug injection device.

Claims (1)

【特許請求の範囲】 1 超々臨界圧火力発電プラントの水処理方法に
おいて、給水系統中に設置されている高圧給水加
熱器入口の給水のPH及びFe量を測定し、これら
の測定値に基づいて給水系統中に注入する薬剤の
注入量を制御し給水のPHを調整することを特徴と
する超々臨界圧火力発電プラントの水処理方法。 2 特許請求の範囲第1項において、高圧給水加
熱器入口より薬剤を注入することを特徴とする
超々臨界圧火力発電プラントの水処理方法。 3 特許請求の範囲第1項において、低圧給水加
熱器入口より薬剤を注入することを特徴とする
超々臨界圧火力発電プラントの水処理方法。 4 特許請求の範囲第1項において、低圧給水加
熱器入口及び高圧給水加熱器入口より薬剤を注入
することを特徴とする超々臨界圧火力発電プラン
トの水処理方法。 5 特許請求の範囲第1項乃至第4項のいずれか
において、薬剤を注入して給水のPHを9.5〜9.8に
調整することを特徴とする超々臨界圧火力発電プ
ラントの水処理方法。 6 特許請求の範囲第1項乃至第5項のいずれか
において、薬剤がアンモニヤ水又はヒドラジンで
あることを特徴とする超々臨界圧火力発電プラン
トの水処理方法。
[Claims] 1. In a water treatment method for an ultra-supercritical thermal power plant, the PH and Fe content of the feed water at the inlet of a high-pressure feed water heater installed in the water supply system are measured, and based on these measured values, A water treatment method for an ultra-supercritical thermal power plant, characterized by controlling the amount of chemicals injected into the water supply system and adjusting the PH of the water supply. 2. A water treatment method for an ultra-supercritical thermal power plant according to claim 1, characterized in that a chemical is injected from the inlet of a high-pressure feed water heater. 3. A water treatment method for an ultra-supercritical thermal power plant according to claim 1, characterized in that the chemical is injected from the inlet of a low-pressure feed water heater. 4. A water treatment method for an ultra-supercritical thermal power plant according to claim 1, characterized in that the chemical is injected from the inlet of a low-pressure feedwater heater and the inlet of a high-pressure feedwater heater. 5. A water treatment method for an ultra-supercritical thermal power plant according to any one of claims 1 to 4, characterized in that the pH of the feed water is adjusted to 9.5 to 9.8 by injecting a chemical. 6. A water treatment method for an ultra-supercritical thermal power plant according to any one of claims 1 to 5, characterized in that the chemical is ammonia water or hydrazine.
JP58207373A 1983-11-07 1983-11-07 Water treatment of ultra-super critical thermal power plant Granted JPS60100688A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58207373A JPS60100688A (en) 1983-11-07 1983-11-07 Water treatment of ultra-super critical thermal power plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58207373A JPS60100688A (en) 1983-11-07 1983-11-07 Water treatment of ultra-super critical thermal power plant

Publications (2)

Publication Number Publication Date
JPS60100688A JPS60100688A (en) 1985-06-04
JPH0323637B2 true JPH0323637B2 (en) 1991-03-29

Family

ID=16538645

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58207373A Granted JPS60100688A (en) 1983-11-07 1983-11-07 Water treatment of ultra-super critical thermal power plant

Country Status (1)

Country Link
JP (1) JPS60100688A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5483408B2 (en) * 2009-06-26 2014-05-07 四国電力株式会社 Continuous concentration measuring apparatus and method

Also Published As

Publication number Publication date
JPS60100688A (en) 1985-06-04

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