JPH06129604A - Method for water supplying processing of heat power plant - Google Patents

Method for water supplying processing of heat power plant

Info

Publication number
JPH06129604A
JPH06129604A JP27583292A JP27583292A JPH06129604A JP H06129604 A JPH06129604 A JP H06129604A JP 27583292 A JP27583292 A JP 27583292A JP 27583292 A JP27583292 A JP 27583292A JP H06129604 A JPH06129604 A JP H06129604A
Authority
JP
Japan
Prior art keywords
oxygen
deaerator
water
concentration
resolved
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
JP27583292A
Other languages
Japanese (ja)
Inventor
Shinji Tsunoda
伸爾 角田
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP27583292A priority Critical patent/JPH06129604A/en
Publication of JPH06129604A publication Critical patent/JPH06129604A/en
Pending legal-status Critical Current

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  • Physical Water Treatments (AREA)

Abstract

PURPOSE:To prevent a concentration of resolved oxygen kept within boiler supplied water from being increased in a water supplying and processing method for feeding oxygen in the boiler supplied water and processing oxygen processing. CONSTITUTION:A lower part of a deaerator 7 to which condensed water got from a condenser 1 is provided with a deaerator water storing tank 9. Oxygen for use in oxygen processing is fed from an oxygen feeding device 17 into the condensed water at a location where oxygen is out of a desalting device 4. A resolved oxygen meter 21 is connected to a water supplying pipe 10 at an outlet port of the exhausting device water storing tank 9 by a sample collecting pipe 20. Concentration of resolved oxygen measured by the meter is converted into an electrical signal by a converter 22 and sent to a system for controlling a degree of opening of a vent valve 8 of the deaerator 7. The vent valve 8 of the deaerator 7 is opened when the concentration of resolved oxygen measured by the resolved oxygen meter 21 is increased more than a certain predetermined value and in tune the vent valve 8 is closed when the concentration of the resolved oxygen is decreased lower than the predetermined value by a predetermined value. With such an arrangement as above, the concentration of the resolved oxygen in the supplied water is kept at the desired value.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は火力発電プラントにおい
て給水を酸素処理する給水処理方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a feed water treatment method for treating feed water with oxygen in a thermal power plant.

【0002】[0002]

【従来の技術】火力発電プラントの給水処理の一手法と
して行われる酸素処理においては、系統を構成する機器
・配管類を防食し、ボイラに搬入される腐食生成物を低
減するため酸素を注入している。酸素処理による従来の
給水処理法を図2によって説明する。
2. Description of the Related Art In oxygen treatment, which is one of the methods of water supply treatment for thermal power plants, oxygen is injected in order to protect the equipment and pipes that make up the system from corrosion and to reduce the corrosion products carried into the boiler. ing. A conventional water supply treatment method using oxygen treatment will be described with reference to FIG.

【0003】図2において、1は復水器で、その上部に
は図示しないタービンが設置されている。復水器1の低
部には、復水管2の一側が接続され、この復水管2に
は、復水器1の側から順に復水ポンプ3、脱塩装置4、
復水ブースタポンプ5、低圧ヒータ6が配置され、復水
管2の他側が脱気器7に接続されている。
In FIG. 2, reference numeral 1 is a condenser, and a turbine (not shown) is installed above the condenser. One side of the condenser pipe 2 is connected to the lower part of the condenser 1, and the condenser pipe 3 is connected to the condenser pipe 2 in this order from the condenser 1 side.
The condensate booster pump 5 and the low-pressure heater 6 are arranged, and the other side of the condensate pipe 2 is connected to the deaerator 7.

【0004】脱気器7の上部には脱気ガスを大気中に放
出するための脱気器ベント弁8が設置されている。脱気
器7の下方には脱気器貯水槽9が連結されている。脱気
器貯水槽9の低部には、給水管10の一側が接続され、
この給水管10に給水ポンプ11、高圧ヒータ12が配
置され、それから給水管10の他側が節炭器13を経て
ボイラ14に接続されている。
A deaerator vent valve 8 for releasing the deaerated gas into the atmosphere is installed above the deaerator 7. A deaerator water storage tank 9 is connected below the deaerator 7. One side of the water supply pipe 10 is connected to the lower part of the deaerator water tank 9,
A water supply pump 11 and a high-pressure heater 12 are arranged in the water supply pipe 10, and the other side of the water supply pipe 10 is connected to a boiler 14 via a economizer 13.

【0005】高圧ヒータ12には、図示しないタービン
系統から抽気された蒸気が高圧抽気管15によって導入
され、高圧ヒータ12で給水管10を流れる給水と熱交
換された蒸気はドレン化し、高圧ヒータ12と脱気器貯
水槽9の間に接続された高圧ヒータドレン管16によっ
て脱気器貯水槽9に回収される。
The steam extracted from a turbine system (not shown) is introduced into the high-pressure heater 12 by a high-pressure extraction pipe 15, and the steam heat-exchanged with the feed water flowing through the water supply pipe 10 in the high-pressure heater 12 is drained, and the high-pressure heater 12 is discharged. Is collected in the deaerator water storage tank 9 by the high-pressure heater drain pipe 16 connected between the deaeration water storage tank 9.

【0006】また、給水処理設備として、酸素注入装置
17から脱塩装置4の出口側の復水管2に酸素注入管1
8が接続されている。酸素注入管18からの酸素注入量
の調整は、この管路に設けられた酸素注入調節弁19に
よって制御され、系統に所定量の酸素が供給される。
As the water supply treatment facility, the oxygen injection pipe 1 is connected to the condensate pipe 2 on the outlet side of the desalination device 4 from the oxygen injection device 17.
8 is connected. The adjustment of the oxygen injection amount from the oxygen injection pipe 18 is controlled by the oxygen injection control valve 19 provided in this pipe line, and a predetermined amount of oxygen is supplied to the system.

【0007】[0007]

【発明が解決しようとする課題】以上のように構成され
た給水処理装置において、給水処理として酸素処理によ
る給水処理を行う場合、注入する酸素量は、本水処理法
の効果を発揮させる上で、節炭器13の入口給水で溶存
酸素濃度を基準値の20〜200μg/リットルの範囲内に
保持する必要がある。このため、酸素注入量の調節手段
として、給水流量比例で酸素注入調節弁19の開度を調
節する制御方式が通常採用されている。
In the water supply treatment apparatus configured as described above, when the water supply treatment by oxygen treatment is performed as the water supply treatment, the amount of oxygen to be injected depends on the effect of the present water treatment method. It is necessary to keep the dissolved oxygen concentration in the inlet water supply of the economizer 13 within the range of 20 to 200 μg / liter of the reference value. For this reason, a control method of adjusting the opening of the oxygen injection control valve 19 in proportion to the feed water flow rate is usually adopted as a means for adjusting the oxygen injection amount.

【0008】また脱気器7の使用方法としては、酸素処
理のために注入された酸素が、脱気器7で脱気されて脱
気器ベント弁8から大気に放出されない様に脱気器ベン
ト弁7を全閉として運用し、脱気器貯水槽9から下流側
の給水及びボイラ水に上述した適量の溶存酸素が存在す
る様に水質管理が行われている。
As a method of using the deaerator 7, the deaerator is used so that the oxygen injected for the oxygen treatment is not deaerated by the deaerator 7 and released from the deaerator vent valve 8 to the atmosphere. The vent valve 7 is fully closed and the water quality is controlled so that the appropriate amount of dissolved oxygen described above exists in the feed water and the boiler water on the downstream side from the deaerator water storage tank 9.

【0009】しかしながら、この酸素注入量調節方式に
おいては、プラントの運転状態が定格負荷運転から低負
荷運転に変化する状態において、脱気器7及び脱気器貯
水槽9の器内圧力、温度が低下し、その影響により器内
の酸素分圧が変化し、液相側すなわち脱気器貯水槽9の
出口給水の溶存酸素濃度が上昇し、基準値の範囲内に保
持することが不可能となる。
However, in this oxygen injection amount adjusting system, the internal pressure and temperature of the deaerator 7 and the deaerator water tank 9 are changed when the operating state of the plant changes from the rated load operation to the low load operation. The oxygen partial pressure in the vessel changes due to the decrease, and the dissolved oxygen concentration in the liquid phase side, that is, the outlet feed water of the deaerator water storage tank 9 rises, and it becomes impossible to maintain it within the range of the reference value. Become.

【0010】更に各負荷運転においては、脱気器貯水槽
9に回収される高圧ヒータドレンの量が変化するため、
この流量が低下する低負荷運転では脱気器貯水槽9の出
口給水の溶存酸素濃度上昇現象を加速し溶存酸素濃度上
昇を顕著にする要因となっている。
Further, in each load operation, the amount of high-pressure heater drain collected in the deaerator water storage tank 9 changes,
In the low load operation in which the flow rate decreases, this is a factor that accelerates the phenomenon of increasing the dissolved oxygen concentration of the outlet feed water of the deaerator water storage tank 9 and makes the dissolved oxygen concentration increase remarkable.

【0011】また、この溶存酸素濃度の上昇現象を防止
するため、注入点の酸素量を調節する方法は、酸素注入
が間欠となったり、復水系統の溶存酸素が下限値を下回
わる等の不具合が生じ、従来の酸素注入制御方式におい
ては、プラントの負荷変動に応答した適性な酸素注入は
不可能であった。
In order to prevent the phenomenon of rising dissolved oxygen concentration, the method of adjusting the amount of oxygen at the injection point is such that the oxygen injection is intermittent or the dissolved oxygen in the condensate system falls below the lower limit value. However, in the conventional oxygen injection control system, it is impossible to properly inject oxygen in response to load fluctuations in the plant.

【0012】本発明は、従来のやり方にみられた前述の
ような問題点のない火力発電プラントの給水処理方法を
提供することを課題としている。
It is an object of the present invention to provide a feed water treatment method for a thermal power plant that does not have the above-mentioned problems found in conventional methods.

【0013】[0013]

【課題を解決するための手段】本発明は、脱気器及び脱
気器貯水槽を含む給水系統を流れるボイラ給水中に酸素
を注入して酸素処理を行う火力発電プラントの給水処理
方法における前記した課題を解決するため、前記脱気器
貯水槽を出る給水中の溶存酸素濃度を検出し同検出濃度
に応じて前記脱気器のベント弁を開閉させることによっ
て前記検出濃度を所定値に保持する方法を採用する。
SUMMARY OF THE INVENTION The present invention relates to a water treatment method for a thermal power plant for injecting oxygen into a boiler feedwater flowing through a water supply system including a deaerator and a deaerator water storage tank to perform oxygen treatment. In order to solve the above problem, the dissolved oxygen concentration in the feed water exiting the deaerator water storage tank is detected, and the vent valve of the deaerator is opened and closed according to the detected concentration to maintain the detected concentration at a predetermined value. Adopt the method of doing.

【0014】[0014]

【作用】本発明の酸素処理においては前記した方法を採
用するので、脱気器貯水槽の出口側の給水管に設置した
溶存酸素計で検出した溶存酸素濃度によって、脱気器の
ベント弁の開度を自動制御して、給水の溶存酸素濃度を
所定値幅に調節することができる。
Since the method described above is adopted in the oxygen treatment of the present invention, the vent valve of the deaerator is controlled by the dissolved oxygen concentration detected by the dissolved oxygen meter installed in the water supply pipe on the outlet side of the deaerator water tank. The dissolved oxygen concentration of the feed water can be adjusted within a predetermined range by automatically controlling the opening.

【0015】脱気器ベント弁の自動制御のやり方の1つ
として、溶存酸素計で検出された酸素濃度が予じめ定め
た第1の値を越えたとき前記脱気器のベント弁を開き、
検出濃度が前記第1の値より小さい予じめ定めた第2の
値に達したときに前記ベント弁を閉じるように制御す
る。
As one of the automatic control methods of the deaerator vent valve, the vent valve of the deaerator is opened when the oxygen concentration detected by the dissolved oxygen meter exceeds a predetermined first value. ,
The vent valve is controlled to close when the detected concentration reaches a predetermined second value smaller than the first value.

【0016】[0016]

【実施例】以下、本発明を図1に示す実施例を参照しつ
つ具体的に説明する。なお、図1において、従来の火力
発電プラントにおける給水処理方法を説明するのに用い
た図2に示すものと共通する機器、配管部分には同一符
号を付してありそれらの説明は省略する。図1におい
て、脱気器貯水槽9の出口側の給水管10には試料採取
管20が連結され、この試料採取管20には、溶存酸素
計21が接続されている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be specifically described below with reference to the embodiment shown in FIG. Note that, in FIG. 1, the same reference numerals are given to the equipment and piping portions common to those shown in FIG. 2 used to describe the conventional water supply treatment method in a thermal power plant, and the description thereof will be omitted. In FIG. 1, a sampling pipe 20 is connected to the water supply pipe 10 on the outlet side of the deaerator water storage tank 9, and a dissolved oxygen meter 21 is connected to the sampling pipe 20.

【0017】溶存酸素計21には、計測した溶存酸素濃
度を電気信号に変換する変換器22を内蔵している。こ
のようにして検出、変換された電気信号は、導線23に
よって脱気器ベント弁8の開度制御系に送られるように
構成されている。
The dissolved oxygen meter 21 contains a converter 22 for converting the measured dissolved oxygen concentration into an electric signal. The electrical signal thus detected and converted is sent to the opening control system of the deaerator vent valve 8 by the conductor 23.

【0018】すなわち、通常運転における脱気器ベント
弁8の開度は、全閉として酸素注入装置17から供給さ
れ脱気器7の内部で分離された酸素が大気に放出される
ことを防止しているが、負荷降下時に前述の要因から、
脱気器貯水槽9の出口給水の溶存酸素濃度が上昇した時
は、それを溶存酸素計21で検知し、変換器22を介し
て脱気器ベント弁8を自動操作で開として脱気器7の気
相部の酸素を大気に放出する。
That is, the opening degree of the deaerator vent valve 8 in the normal operation is fully closed to prevent the oxygen supplied from the oxygen injection device 17 and separated in the deaerator 7 from being released to the atmosphere. However, due to the above factors when the load drops,
When the dissolved oxygen concentration of the outlet feed water of the deaerator water storage tank 9 rises, it is detected by the dissolved oxygen meter 21, and the deaerator vent valve 8 is automatically opened via the converter 22 to open the deaerator. Oxygen in the gas phase portion 7 is released to the atmosphere.

【0019】この操作によって脱気器貯水槽9の出口給
水の溶存酸素濃度が低下した時は同様にして脱気器ベン
ト弁8を閉として給水中の溶存酸素濃度を基準値の範囲
内に調整する。
When the dissolved oxygen concentration of the outlet feed water of the deaerator water storage tank 9 is lowered by this operation, the deaerator vent valve 8 is closed in the same manner to adjust the dissolved oxygen concentration in the feed water within the range of the reference value. To do.

【0020】酸素処理における給水中の溶存酸素の基準
値は20〜200μg/リットルであるが、この範囲を逸脱
しないように本発明の適用時には、例えば溶存酸素濃度
100μg/リットルで脱気器ベント弁8を開とし、50μ
g/リットルで閉とする制御用設定値を溶存酸素計21に設
けて運転し、大幅な負荷変化に対しても、脱気器貯水槽
9の出口給水の溶存酸素濃度を基準値の範囲内に保持す
ることが可能となった。
The reference value of dissolved oxygen in the feed water in the oxygen treatment is 20 to 200 μg / liter, but when the present invention is applied so as not to deviate from this range, for example, a deaerator vent valve with a dissolved oxygen concentration of 100 μg / liter. Open 8 and 50μ
The dissolved oxygen meter 21 is operated with a set value for control that is closed at g / liter, and the dissolved oxygen concentration of the outlet feed water of the deaerator water storage tank 9 is within the standard value range even if the load changes significantly. It is now possible to hold.

【0021】以上本発明による給水処理方法を具体的に
説明したが本発明がこれに限定されないことはいうまで
もない。要は、脱気器貯水槽を出る給水中の溶存酸素濃
度を検出しその濃度が所定値に収まるように脱気器のベ
ント弁を開閉制御すればよい。
Although the water supply treatment method according to the present invention has been specifically described above, it goes without saying that the present invention is not limited to this. The point is to detect the dissolved oxygen concentration in the feed water leaving the deaerator water storage tank and control the opening / closing of the vent valve of the deaerator so that the concentration falls within a predetermined value.

【0022】[0022]

【発明の効果】以上述べたように、本発明の酸素処理に
おける給水の溶存酸素濃度の制御方法は、負荷変動が頻
繁で、かつ変動幅が大きい火力発電プラントの給水の溶
存酸素を調節する方法において、脱気器貯水槽出口給水
の溶存酸素濃度を溶存酸素計で連続的に検出監視し、そ
の検出濃度に応じて脱気器ベント弁の開度を自動調整す
ることによって、常時給水の溶存酸素濃度を適性な範囲
内に保持することを可能とし、所期の目的を達成するこ
とができる。
As described above, the method for controlling the dissolved oxygen concentration of feed water in the oxygen treatment of the present invention is a method for adjusting the dissolved oxygen of feed water of a thermal power plant in which load fluctuations are frequent and whose fluctuation range is large. , The dissolved oxygen concentration of the feedwater at the outlet of the deaerator water tank is continuously detected and monitored by a dissolved oxygen meter, and the opening of the deaerator vent valve is automatically adjusted according to the detected concentration, so that the feedwater is always dissolved It is possible to keep the oxygen concentration within an appropriate range and achieve the intended purpose.

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

【図1】本発明による火力発電プラントの給水処理方法
を示すフローシート図。
FIG. 1 is a flow sheet diagram showing a water supply treatment method for a thermal power plant according to the present invention.

【図2】従来の火力発電プラントにおける給水処理方法
を示すフローシート図。
FIG. 2 is a flow sheet diagram showing a water supply treatment method in a conventional thermal power plant.

【符号の説明】[Explanation of symbols]

1 復水器 2 復水管 7 脱気器 8 脱気器ベント弁 9 脱気器貯水槽 10 給水管 17 酸素注入装置 18 酸素注入管 20 試料採取管 21 溶存酸素計 22 変換器 1 Condenser 2 Condensate Pipe 7 Deaerator 8 Deaerator Vent Valve 9 Deaerator Water Tank 10 Water Supply Pipe 17 Oxygen Injector 18 Oxygen Injector 20 Sampling Pipe 21 Dissolved Oxygen Meter 22 Converter

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 脱気器及び脱気器貯水槽を含む給水系統
に流れるボイラ給水中に酸素を注入して酸素処理を行う
火力発電プラントの給水処理方法において、前記脱気器
貯水槽を出る給水中の溶存酸素濃度を検出し同検出濃度
に応じて前記脱気器のベント弁を開閉させることによっ
て前記検出濃度を所定値に保持することを特徴とする火
力発電プラントの給水処理方法。
1. A feedwater treatment method for a thermal power plant that injects oxygen into a boiler feedwater flowing in a water supply system including a deaerator and a deaerator water storage tank to perform oxygen treatment, and exits the deaerator water storage tank. A method for treating feedwater in a thermal power plant, which detects a dissolved oxygen concentration in feedwater and holds the detected concentration at a predetermined value by opening and closing a vent valve of the deaerator according to the detected concentration.
JP27583292A 1992-10-14 1992-10-14 Method for water supplying processing of heat power plant Pending JPH06129604A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27583292A JPH06129604A (en) 1992-10-14 1992-10-14 Method for water supplying processing of heat power plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27583292A JPH06129604A (en) 1992-10-14 1992-10-14 Method for water supplying processing of heat power plant

Publications (1)

Publication Number Publication Date
JPH06129604A true JPH06129604A (en) 1994-05-13

Family

ID=17561054

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27583292A Pending JPH06129604A (en) 1992-10-14 1992-10-14 Method for water supplying processing of heat power plant

Country Status (1)

Country Link
JP (1) JPH06129604A (en)

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