JPH11132674A - Pressure control device of high-pressure steam condenser - Google Patents

Pressure control device of high-pressure steam condenser

Info

Publication number
JPH11132674A
JPH11132674A JP29801597A JP29801597A JPH11132674A JP H11132674 A JPH11132674 A JP H11132674A JP 29801597 A JP29801597 A JP 29801597A JP 29801597 A JP29801597 A JP 29801597A JP H11132674 A JPH11132674 A JP H11132674A
Authority
JP
Japan
Prior art keywords
steam
pressure
condenser
output
pressure control
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
JP29801597A
Other languages
Japanese (ja)
Inventor
Takayuki Tanabe
隆之 田邊
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.)
Meidensha Corp
Meidensha Electric Manufacturing Co Ltd
Original Assignee
Meidensha Corp
Meidensha Electric Manufacturing Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Meidensha Corp, Meidensha Electric Manufacturing Co Ltd filed Critical Meidensha Corp
Priority to JP29801597A priority Critical patent/JPH11132674A/en
Publication of JPH11132674A publication Critical patent/JPH11132674A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To control pressure stably and at the same time reduce the deterioration of control performance. SOLUTION: Steam generated by a boiler 31 for generating steam by burning rubbish is accumulated in a high-pressure steam accumulation tank 32. The high-pressure steam of the tank 32 is supplied to a steam turbine 33 and at the same time is supplied to a high-pressure steam condenser 34 via a flowmeter 35. The steam condenser 34 is constituted by combining steam condenser single substances (bundle) A, B, and C, and pressure control valves 36a, 36b, and 36c are provided at the outer side of the bundles A, B, and C. The pressure control valves 36a, 36b, and 36c are controlled by a drive signal from a control valve drive signal generation part 37. A selector 38 selects whether the operation of the pressure control valves 36a, 36b, and 36c is right or wrong according to a signal from the flowmeter 35. The signal of a pressure sensor 39 is compared with a pressure setting value by a deviation equipment 40, and the deviation output is fed to a controller 41. The output of the controller 41 is supplied to the drive signal generation part 37.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】この発明は、ゴミ焼却施設の
余熱利用発電設備における高圧蒸気復水器の圧力制御装
置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a pressure control device for a high-pressure steam condenser in a power generation facility utilizing waste heat in a refuse incineration plant.

【0002】[0002]

【従来の技術】図3は、ゴミ焼却施設の余熱利用発電設
備における主要な機器構成図で、図3において、11は
燃料であるゴミを燃焼させて蒸気を発生させるボイラ
で、このボイラ11で発生された蒸気は高圧蒸気蓄積タ
ンク12に蓄積される。タンク12の高圧蒸気は蒸気タ
ービン13に供給されるとともに、高圧蒸気復水器14
に供給される。高圧蒸気復水器14は、ゴミの発熱量の
変動に起因したボイラ11の発生蒸気量の変動を吸収す
るためのもので、余剰蒸気の廃熱を高圧蒸気復水器14
で行う。また、高圧蒸気復水器14は、蒸気タービン1
3の1次側圧力を安定させるために、高圧蒸気復水器1
4との流路にある制御弁15で圧力制御される。16は
制御弁である。
2. Description of the Related Art FIG. 3 is a diagram showing the main components of a power generation facility utilizing waste heat in a refuse incineration facility. In FIG. 3, reference numeral 11 denotes a boiler for burning refuse as fuel to generate steam. The generated steam is stored in the high-pressure steam storage tank 12. The high-pressure steam in the tank 12 is supplied to a steam turbine 13 and a high-pressure steam condenser 14.
Supplied to The high-pressure steam condenser 14 is for absorbing fluctuations in the amount of steam generated by the boiler 11 due to fluctuations in the amount of heat generated by the garbage.
Do with. The high-pressure steam condenser 14 is a steam turbine 1
3 to stabilize the primary pressure of the high pressure steam condenser 1
The pressure is controlled by a control valve 15 in the flow path with the control valve 4. 16 is a control valve.

【0003】[0003]

【発明が解決しようとする課題】図3に示すゴミ焼却施
設発電設備においては、燃料であるゴミの発熱量の変動
に起因したボイラの発生蒸気量の変動が大きい。この発
生蒸気量の変動は主たる余熱利用設備である蒸気タービ
ン発電機の安定な運転を妨げるものである。このため、
発生蒸気量変動を吸収せしめるためには、高圧蒸気復水
器による余剰蒸気の廃熱が必要となる。
In the garbage incineration facility power generation equipment shown in FIG. 3, the amount of steam generated by the boiler greatly fluctuates due to the change in the amount of heat generated by the garbage as fuel. This fluctuation in the amount of generated steam hinders stable operation of the steam turbine generator, which is the main equipment for utilizing residual heat. For this reason,
In order to absorb the generated steam fluctuation, waste heat of excess steam by the high-pressure steam condenser is required.

【0004】通常の運転時においては、余剰蒸気量は低
く押さえることが望まれるために、高圧蒸気復水器への
発生蒸気量は非常に低い値で変動する。しかし、高圧蒸
気復水器は蒸気タービンの非運転時においては、ボイラ
の発生する大半の蒸気量を復水せしめる必要がある。こ
のため、高圧蒸気復水器の処理能力は、負荷最大時に対
して設計されてある。これにより、蒸気タービンの運転
時と非運転時において、高圧蒸気復水器に対する負荷は
大きく分けて、2つの状態を持つこととなる。この状態
において、蒸気タービンの安定な運転のために、蒸気タ
ービンの1、2次側圧力を一定に保つ必要がある。
[0004] During normal operation, since it is desired that the amount of surplus steam be kept low, the amount of steam generated in the high-pressure steam condenser fluctuates at a very low value. However, when the steam turbine is not operating, the high-pressure steam condenser needs to condense most of the steam generated by the boiler. For this reason, the processing capacity of the high-pressure steam condenser is designed for maximum load. As a result, the load on the high-pressure steam condenser is largely divided into two states during operation and non-operation of the steam turbine. In this state, it is necessary to keep the primary and secondary pressures of the steam turbine constant for stable operation of the steam turbine.

【0005】上記圧力制御のために、高圧蒸気蓄積タン
ク12と高圧蒸気復水器14は図4に示すように制御弁
15、16により制御される。図4において、高圧蒸気
蓄積タンク12の圧力は、圧力センサ17により検出さ
れる。この検出圧力と設定値圧力は偏差器18で比較さ
れ、偏差出力に応じて制御器19から制御弁15に制御
出力が送出される。
For controlling the pressure, the high-pressure steam storage tank 12 and the high-pressure steam condenser 14 are controlled by control valves 15 and 16 as shown in FIG. In FIG. 4, the pressure of the high-pressure vapor storage tank 12 is detected by a pressure sensor 17. The detected pressure and the set value pressure are compared by the deviation device 18, and a control output is sent from the controller 19 to the control valve 15 according to the deviation output.

【0006】また、高圧蒸気復水器14の圧力は、圧力
センサ20により検出される。この検出圧力と設定値圧
力は偏差器21で比較され、偏差出力に応じて制御器2
2から制御弁16に制御出力が送出される。
The pressure of the high-pressure steam condenser 14 is detected by a pressure sensor 20. The detected pressure and the set pressure are compared by the deviation device 21 and the controller 2 according to the deviation output.
2 outputs a control output to the control valve 16.

【0007】上記のように構成された高圧蒸気蓄積タン
ク12と高圧蒸気復水器14の圧力制御において、高圧
蒸気復水器14は1次側圧力である高圧蒸気蓄積タンク
12の圧力制御操作端の下流に位置する。このため、高
圧蒸気復水器14の圧力変動は、高圧蒸気蓄積タンク1
2の圧力制御の外乱となって、安定な1次側圧力を阻害
することとなる。
In the pressure control of the high-pressure steam storage tank 12 and the high-pressure steam condenser 14 configured as described above, the high-pressure steam condenser 14 is a pressure control operation terminal of the high-pressure steam storage tank 12 which is the primary pressure. Located downstream of. For this reason, the pressure fluctuation of the high-pressure steam condenser 14 depends on the high-pressure steam storage tank 1.
As a disturbance in the pressure control of No. 2, the stable primary side pressure is hindered.

【0008】上記のことから、高圧蒸気復水器14は、
最大負荷状態と最小負荷状態の2つの状態で安定な圧力
制御が要求される。このため、最大負荷時に対して、設
計される高圧蒸気復水器14では最小負荷時において、
安定な圧力制御が困難となる問題がある。この問題は、
高圧蒸気復水器14の構成が、高圧蒸気蓄積タンク12
からの蒸気で蒸気タービン13を運転中、すなわち最大
負荷時に対して設計されているため、最小負荷時では、
高圧蒸気復水器14の動特性の非線形性の強い状態での
運転が要求されることによって、制御性能の悪化が生じ
るからである。また、最大負荷時において設計される高
圧蒸気復水器の構造は、最小負荷時においては、操作端
である調節弁の非線形性の強い全閉付近での運転が行わ
れるのも、制御性能が悪化する問題にもなっている。
From the above, the high-pressure steam condenser 14 is
Stable pressure control is required in two states, a maximum load state and a minimum load state. For this reason, at the time of the minimum load, the designed high-pressure steam condenser 14 has the
There is a problem that stable pressure control becomes difficult. This problem,
The configuration of the high-pressure steam condenser 14 is different from that of the high-pressure steam storage tank 12.
During operation of the steam turbine 13 with steam from, that is, at the time of maximum load, at the time of minimum load,
This is because the control performance is deteriorated when the high-pressure steam condenser 14 is required to be operated in a state where the dynamic characteristics are highly nonlinear. In addition, the structure of the high-pressure steam condenser designed at the time of maximum load has the control performance that, at the time of minimum load, the operation is performed near the fully closed state where the control valve, which is the operating end, has strong nonlinearity. It is also a problem that gets worse.

【0009】この発明は上記の事情に鑑みてなされたも
ので、安定な圧力制御を可能とするとともに、制御性能
の悪化を低減する高圧蒸気復水器の圧力制御装置を提供
することを課題とする。
The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a pressure control device for a high-pressure steam condenser that enables stable pressure control and reduces deterioration of control performance. I do.

【0010】[0010]

【課題を解決するための手段】この発明は、上記の課題
を達成するために、第1発明は、燃料を燃焼させて蒸気
を発生させ、その蒸気を高圧蒸気蓄積タンクを介して蒸
気タービンに供給して蒸気タービンを運転させる発電設
備であって、前記高圧蒸気蓄積タンクに連結され、蒸気
流量変動を吸収させる高圧蒸気復水器と、この復水器の
蒸気流入側の圧力を検出するセンサと、このセンサの出
力信号と圧力設定値とを比較し、その偏差出力を送出す
る偏差器と、前記復水器の蒸気流出側に設けられる圧力
制御弁と、前記偏差器の偏差出力が供給され、出力に前
記圧力制御弁の調節量が送出される制御器と、前記タン
クと復水器との蒸気流路に設けられた流量計と、この流
量計からの流量信号が与えられ、その流量信号に応じて
選択信号を送出する選択器と、この選択器から送出され
る選択信号が与えられ、選択信号の有無により前記圧力
制御弁を開閉させるとともに、前記制御器からの調節量
に応じて前記圧力制御弁を調節する制御弁駆動信号発生
部とを備えたことを特徴とするものである。
SUMMARY OF THE INVENTION In order to achieve the above-mentioned object, a first aspect of the present invention is to generate steam by burning fuel, and the steam is supplied to a steam turbine via a high-pressure steam storage tank. A power generator for supplying and operating a steam turbine, comprising a high-pressure steam condenser connected to the high-pressure steam storage tank for absorbing fluctuations in steam flow rate, and a sensor for detecting a pressure on a steam inlet side of the condenser. The output signal of this sensor is compared with a pressure set value, a deviation device for sending out a deviation output, a pressure control valve provided on the steam outflow side of the condenser, and a deviation output of the deviation device are supplied. A controller that outputs an adjustment amount of the pressure control valve to an output, a flow meter provided in a steam flow path between the tank and the condenser, and a flow signal from the flow meter are given. Send selection signal according to flow signal A selector, provided with a selection signal sent from the selector, for opening and closing the pressure control valve according to the presence or absence of the selection signal, and for controlling the pressure control valve according to an adjustment amount from the controller. And a drive signal generator.

【0011】第2発明は、前記高圧蒸気復水器が、複数
の復水器単体から構成され、その復水器単体の蒸気流入
側は一括接続され、蒸気流出側には復水器単体毎に圧力
制御弁が設けられ、それら圧力制御弁の開閉は選択器か
らの選択信号により選択されるようにしたことを特徴と
するものである。
In a second aspect of the present invention, the high-pressure steam condenser is constituted by a plurality of condensers alone, the steam inflow sides of the condensers are connected collectively, and the condenser outflow side is connected to each of the condensers. Are provided with pressure control valves, and the opening and closing of these pressure control valves are selected by a selection signal from a selector.

【0012】第3発明は、燃料を燃焼させて蒸気を発生
させ、その蒸気を高圧蒸気蓄積タンクを介して蒸気ター
ビンに供給して蒸気タービンを運転させる発電設備であ
って、 前記高圧蒸気蓄積タンクに連結され、蒸気流量
変動を吸収させる高圧蒸気復水器と、この復水器の蒸気
流入側の圧力を検出するセンサと、このセンサの出力信
号と圧力設定値とを比較し、その偏差出力を送出する偏
差器と、前記復水器の蒸気流出側に設けられる圧力制御
弁と、前記偏差器の偏差出力が供給され、出力に前記圧
力制御弁の調節量が送出される制御器と、前記タンクと
復水器との蒸気流路に設けられた流量計と、この流量計
からの流量信号が与えられると、出力に非線形出力を送
出する非線形発生部と、この非線形発生部からの非線形
出力と前記制御器からの調節量を乗算し、その乗算出力
により前記圧力制御弁を制御する乗算器とを備えたこと
を特徴とするものである。
[0012] A third invention is a power generation facility for operating a steam turbine by burning fuel to generate steam and supplying the steam to a steam turbine via a high-pressure steam storage tank, wherein the high-pressure steam storage tank is provided. A high-pressure steam condenser that absorbs fluctuations in steam flow rate, a sensor that detects the pressure on the steam inflow side of the condenser, and compares the output signal of this sensor with a pressure set value and outputs a deviation output thereof. And a pressure control valve provided on the steam outflow side of the condenser, a deviation output of the deviation device is supplied, and a controller that outputs an adjustment amount of the pressure control valve to the output, A flow meter provided in a steam flow path between the tank and the condenser, a flow rate signal from the flow meter being supplied, a non-linear generation unit for sending a non-linear output to an output, and a non-linear generation unit from the non-linear generation unit Output and the controller A multiplier that multiplies the adjustment amounts and controls the pressure control valve with the multiplied output.

【0013】[0013]

【発明の実施の形態】以下この発明の実施の形態を図面
に基づいて説明する。図1はこの発明の実施の第1形態
を示す構成説明図で、図1において、31は燃料である
ゴミを燃焼させて蒸気を発生させるボイラで、このボイ
ラ31で発生された蒸気は高圧蒸気蓄積タンク32に蓄
積される。タンク32の高圧蒸気は蒸気タービン33に
供給されるとともに、高圧蒸気復水器34に流量計35
を介して供給される。高圧蒸気復水器34は、ゴミの発
熱量の変動に起因したボイラ31の発生蒸気量の変動を
吸収するためのもので、この高圧蒸気復水器34は復水
器単体(バンドル)A,B,Cを組み合わせて構成され
ている。なお、余剰蒸気の廃熱は高圧蒸気復水器14で
行われる。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a structural explanatory view showing a first embodiment of the present invention. In FIG. 1, reference numeral 31 denotes a boiler which burns refuse as fuel to generate steam, and the steam generated by the boiler 31 is high-pressure steam. It is stored in the storage tank 32. The high-pressure steam in the tank 32 is supplied to a steam turbine 33 and a high-pressure steam condenser 34 is connected to a flow meter 35.
Is supplied via The high-pressure steam condenser 34 is for absorbing fluctuations in the amount of steam generated by the boiler 31 due to fluctuations in the amount of heat generated by the garbage. B and C are combined. In addition, the waste heat of the surplus steam is performed by the high-pressure steam condenser 14.

【0014】高圧蒸気復水器34を構成するバンドル
A,B,Cの蒸気流出側には、圧力制御弁36a,36
b,36cが設けられる。この圧力制御弁36a,36
b,36cは制御弁駆動信号発生部37からの駆動信号
で制御される。38は選択器で、この選択器38は、前
記流量計35からの信号により圧力制御弁36a,36
b,36cの運転の可否を選択するものである。39は
高圧蒸気復水器34の入口圧力を検出する圧力センサ
で、この圧力センサ39の信号と圧力設定値とを偏差器
40にて比較し、その偏差出力を制御器41に与える。
制御器41の出力は駆動信号発生部37に供給される。
On the steam outflow side of the bundles A, B, C constituting the high-pressure steam condenser 34, pressure control valves 36a, 36
b, 36c are provided. These pressure control valves 36a, 36
b and 36c are controlled by a drive signal from the control valve drive signal generator 37. Reference numeral 38 denotes a selector, which is operated by a signal from the flow meter 35 to control the pressure control valves 36a, 36a.
b, 36c are selected. Reference numeral 39 denotes a pressure sensor for detecting the inlet pressure of the high-pressure steam condenser 34, and a signal from the pressure sensor 39 is compared with a set pressure value by a deviation device 40, and the deviation output is given to a controller 41.
The output of the controller 41 is supplied to the drive signal generator 37.

【0015】上記のように構成された高圧蒸気復水器の
圧力制御装置において、蒸気タービン33が運転状態か
ら非運転状態になると、高圧蒸気復水器34に流入する
蒸気流量が変動する。すると流量計35から流量に応じ
た信号が選択器38に与えられる。選択器38は、その
信号に応じて制御弁駆動信号発生部37に、どの圧力制
御弁36a〜36cを選択するかの選択信号を与える。
例えば、圧力制御弁36a,36bを選択した場合は、
これを制御状態にし、圧力制御弁36cを選択しない場
合は、非制御状態で弁を全閉する。これとともに、高圧
蒸気復水器34の蒸気入口の圧力を圧力センサ39で検
出し、偏差器40で設定値を比較し、その偏差量に応じ
て制御器41から圧力制御弁36a,36bの制御流量
を調節する。
In the pressure control device for a high-pressure steam condenser configured as described above, when the steam turbine 33 is changed from the operating state to the non-operating state, the flow rate of steam flowing into the high-pressure steam condenser 34 fluctuates. Then, a signal corresponding to the flow rate is provided from the flow meter 35 to the selector 38. The selector 38 supplies a selection signal indicating which of the pressure control valves 36a to 36c is to be selected to the control valve drive signal generator 37 according to the signal.
For example, when the pressure control valves 36a and 36b are selected,
When this is set to the control state and the pressure control valve 36c is not selected, the valve is fully closed in the non-control state. At the same time, the pressure at the steam inlet of the high-pressure steam condenser 34 is detected by the pressure sensor 39, the set value is compared by the deviation device 40, and the controller 41 controls the pressure control valves 36a and 36b according to the deviation amount. Adjust the flow rate.

【0016】上記のようにして、高圧蒸気復水器34の
負荷変動(蒸気タービン運転時、非運転時の蒸気流量変
動)に応じて圧力制御弁36a〜36cを選択し、その
弁により制御量を調節することにより、負荷変動の割合
が減少し、安定した状態での高圧蒸気復水器34の運転
が可能となる。
As described above, the pressure control valves 36a to 36c are selected in accordance with the load fluctuation of the high-pressure steam condenser 34 (the steam flow rate fluctuation when the steam turbine is operating or not operating), and the control amount is controlled by the valve. Is adjusted, the rate of load fluctuation is reduced, and the high-pressure steam condenser 34 can be operated in a stable state.

【0017】図2はこの発明の実施の第2形態を示す構
成説明図で、この第2形態では、圧力制御弁を1台にし
て、コストの低減を図ったものである。このため、第2
形態では、負荷変動に対する圧力制御系の安定性の確保
を制御器のみで吸収するように構成した。図2におい
て、図1と同一部分には同一符号を付して示すに、流量
計35で得た流量信号は非線形発生部42に入力され
る。非線形発生部42は入力された流量信号に応じた出
力を送出し、その出力を制御器41の制御出力と乗算器
43で乗算する。この乗算器43で乗算した出力で圧力
制御弁36を調節する。
FIG. 2 is a structural explanatory view showing a second embodiment of the present invention. In the second embodiment, the cost is reduced by using one pressure control valve. Therefore, the second
In the embodiment, the stability of the pressure control system with respect to the load fluctuation is ensured by only the controller. In FIG. 2, the same parts as those in FIG. 1 are denoted by the same reference numerals, and the flow signal obtained by the flow meter 35 is input to the nonlinear generation unit 42. The nonlinear generator 42 outputs an output corresponding to the input flow signal, and multiplies the output by the multiplier 43 with the control output of the controller 41. The pressure control valve 36 is adjusted with the output multiplied by the multiplier 43.

【0018】上記のように、負荷変動に対する制御性能
の悪化の主たる原因は圧力制御弁36の非線形性にあ
る。このため、高圧蒸気復水器34への蒸気流量を検出
し、その検出信号を非線形発生部42に入力した後、制
御器41の制御出力と乗算器43で乗算して制御ゲイン
の補償を行って、圧力制御弁36の非線形性を制御する
ようにしたので、制御性能の向上を図ることができるよ
うになる。
As described above, the main cause of deterioration in control performance with respect to load fluctuation is the nonlinearity of the pressure control valve 36. Therefore, after detecting the steam flow rate to the high-pressure steam condenser 34 and inputting the detection signal to the non-linear generator 42, the control output of the controller 41 is multiplied by the multiplier 43 to compensate for the control gain. Since the non-linearity of the pressure control valve 36 is controlled, the control performance can be improved.

【0019】[0019]

【発明の効果】以上述べたように、この発明によれば、
高圧蒸気復水器に流入する蒸気流量と圧力とを用いて高
圧蒸気復水器の負荷変動を抑制することにより、高圧蒸
気復水器による制御性能の悪化を低減することができる
利点がある。
As described above, according to the present invention,
By suppressing the load fluctuation of the high-pressure steam condenser using the steam flow rate and the pressure flowing into the high-pressure steam condenser, there is an advantage that it is possible to reduce the deterioration of the control performance due to the high-pressure steam condenser.

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

【図1】この発明の実施の第1形態を示す構成説明図。FIG. 1 is a configuration explanatory view showing a first embodiment of the present invention.

【図2】この発明の実施の第2形態を示す構成説明図。FIG. 2 is a configuration explanatory view showing a second embodiment of the present invention.

【図3】ゴミ焼却施設の余熱利用発電設備における主要
な機器構成図。
FIG. 3 is a main device configuration diagram of a power generation facility using residual heat in a garbage incineration facility.

【図4】従来の高圧蒸気蓄積タンク及び高圧蒸気復水器
の圧力制御装置の構成説明図。
FIG. 4 is a configuration explanatory view of a conventional pressure control device for a high-pressure steam storage tank and a high-pressure steam condenser.

【符号の説明】[Explanation of symbols]

31…ボイラ 32…高圧蒸気蓄積タンク 33…蒸気タービン 34…高圧蒸気復水器 35…流量計 36、36a〜36c…圧力制御弁 37…制御弁駆動信号発生部 38…選択器 39…圧力センサ 40…偏差器 41…制御器 42…非線形発生部 43…乗算器 Reference Signs List 31 boiler 32 high-pressure steam storage tank 33 steam turbine 34 high-pressure steam condenser 35 flow meter 36, 36a to 36c pressure control valve 37 control valve drive signal generator 38 selector 39 pressure sensor 40 … Deviation device 41… Controller 42… Non-linear generator 43… Multiplier

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 燃料を燃焼させて蒸気を発生させ、その
蒸気を高圧蒸気蓄積タンクを介して蒸気タービンに供給
して蒸気タービンを運転させる発電設備であって、 前記高圧蒸気蓄積タンクに連結され、蒸気流量変動を吸
収させる高圧蒸気復水器と、この復水器の蒸気流入側の
圧力を検出するセンサと、このセンサの出力信号と圧力
設定値とを比較し、その偏差出力を送出する偏差器と、
前記復水器の蒸気流出側に設けられる圧力制御弁と、前
記偏差器の偏差出力が供給され、出力に前記圧力制御弁
の調節量が送出される制御器と、前記タンクと復水器と
の蒸気流路に設けられた流量計と、この流量計からの流
量信号が与えられ、その流量信号に応じて選択信号を送
出する選択器と、この選択器から送出される選択信号が
与えられ、選択信号の有無により前記圧力制御弁を開閉
させるとともに、前記制御器からの調節量に応じて前記
圧力制御弁を調節する制御弁駆動信号発生部とを備えた
ことを特徴とする高圧蒸気復水器の圧力制御装置。
1. A power generation facility for operating a steam turbine by burning fuel to generate steam and supplying the steam to a steam turbine via a high-pressure steam storage tank, wherein the power generation facility is connected to the high-pressure steam storage tank. , A high-pressure steam condenser that absorbs steam flow rate fluctuations, a sensor that detects the pressure on the steam inflow side of the condenser, a comparison between an output signal of the sensor and a pressure set value, and transmission of a deviation output thereof. A deviator,
A pressure control valve provided on the steam outflow side of the condenser, a deviation output of the deviation device is supplied, and a controller that outputs an adjustment amount of the pressure control valve to an output; the tank and the condenser; A flow meter provided in the steam flow path, a flow signal from the flow meter is given, and a selector that sends a selection signal in accordance with the flow signal, and a selection signal that is sent from the selector are given. A control valve drive signal generator for opening and closing the pressure control valve according to the presence or absence of a selection signal and adjusting the pressure control valve in accordance with an adjustment amount from the controller. Water pressure control device.
【請求項2】 前記高圧蒸気復水器は、複数の復水器単
体から構成され、その復水器単体の蒸気流入側は一括接
続され、蒸気流出側には復水器単体毎に圧力制御弁が設
けられ、それら圧力制御弁の開閉は選択器からの選択信
号により選択されるようにしたことを特徴とする請求項
1記載の高圧蒸気復水器の圧力制御装置。
2. The high-pressure steam condenser is composed of a plurality of condensers alone, the steam inlet side of the condensers is connected collectively, and the steam outlet side is pressure-controlled for each condenser alone. 2. A pressure control device for a high-pressure steam condenser according to claim 1, wherein valves are provided, and opening and closing of the pressure control valves are selected by a selection signal from a selector.
【請求項3】 燃料を燃焼させて蒸気を発生させ、その
蒸気を高圧蒸気蓄積タンクを介して蒸気タービンに供給
して蒸気タービンを運転させる発電設備であって、 前記高圧蒸気蓄積タンクに連結され、蒸気流量変動を吸
収させる高圧蒸気復水器と、この復水器の蒸気流入側の
圧力を検出するセンサと、このセンサの出力信号と圧力
設定値とを比較し、その偏差出力を送出する偏差器と、
前記復水器の蒸気流出側に設けられる圧力制御弁と、前
記偏差器の偏差出力が供給され、出力に前記圧力制御弁
の調節量が送出される制御器と、前記タンクと復水器と
の蒸気流路に設けられた流量計と、この流量計からの流
量信号が与えられると、出力に非線形出力を送出する非
線形発生部と、この非線形発生部からの非線形出力と前
記制御器からの調節量を乗算し、その乗算出力により前
記圧力制御弁を制御する乗算器とを備えたことを特徴と
する高圧蒸気復水器の圧力制御装置。
3. A power generation facility for operating a steam turbine by burning fuel to generate steam and supplying the steam to a steam turbine via a high-pressure steam storage tank, wherein the power plant is connected to the high-pressure steam storage tank. , A high-pressure steam condenser that absorbs steam flow rate fluctuations, a sensor that detects the pressure on the steam inflow side of the condenser, a comparison between an output signal of the sensor and a pressure set value, and transmission of a deviation output thereof. A deviator,
A pressure control valve provided on the steam outflow side of the condenser, a deviation output of the deviation device is supplied, and a controller that outputs an adjustment amount of the pressure control valve to an output; the tank and the condenser; A flow meter provided in the steam flow path, a non-linear generator for sending a non-linear output to an output when a flow signal from the flow meter is provided, a non-linear output from the non-linear generator, and a non-linear output from the controller. A multiplier for multiplying the control amount and controlling the pressure control valve by the multiplied output.
JP29801597A 1997-10-30 1997-10-30 Pressure control device of high-pressure steam condenser Pending JPH11132674A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29801597A JPH11132674A (en) 1997-10-30 1997-10-30 Pressure control device of high-pressure steam condenser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29801597A JPH11132674A (en) 1997-10-30 1997-10-30 Pressure control device of high-pressure steam condenser

Publications (1)

Publication Number Publication Date
JPH11132674A true JPH11132674A (en) 1999-05-21

Family

ID=17854026

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29801597A Pending JPH11132674A (en) 1997-10-30 1997-10-30 Pressure control device of high-pressure steam condenser

Country Status (1)

Country Link
JP (1) JPH11132674A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003024633A1 (en) * 2001-09-20 2003-03-27 Thermsave Engineering Uk Limited Improved waste treatment
WO2013111577A1 (en) * 2012-01-23 2013-08-01 富士電機株式会社 Air-cooling condenser and power generation device equipped with same

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003024633A1 (en) * 2001-09-20 2003-03-27 Thermsave Engineering Uk Limited Improved waste treatment
WO2013111577A1 (en) * 2012-01-23 2013-08-01 富士電機株式会社 Air-cooling condenser and power generation device equipped with same
JPWO2013111577A1 (en) * 2012-01-23 2015-05-11 富士電機株式会社 Air-cooled condenser and power generator equipped with the same
US9920998B2 (en) 2012-01-23 2018-03-20 Fuji Electric Co., Ltd. Air cooled condenser and power generating apparatus provided with the same

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