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JP3080228B2 - Power plant control method - Google Patents
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JP3080228B2 - Power plant control method - Google Patents

Power plant control method

Info

Publication number
JP3080228B2
JP3080228B2 JP10370755A JP37075598A JP3080228B2 JP 3080228 B2 JP3080228 B2 JP 3080228B2 JP 10370755 A JP10370755 A JP 10370755A JP 37075598 A JP37075598 A JP 37075598A JP 3080228 B2 JP3080228 B2 JP 3080228B2
Authority
JP
Japan
Prior art keywords
boiler
steam
pressure
power plant
boilers
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 - Fee Related
Application number
JP10370755A
Other languages
Japanese (ja)
Other versions
JP2000193201A (en
Inventor
徹夫 寺本
成昭 東
貢 足利
俊郎 伊藤
憲彦 和佐田
光俊 羽鳥
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.)
Kawasaki Motors Ltd
Original Assignee
Kawasaki Jukogyo KK
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 Kawasaki Jukogyo KK filed Critical Kawasaki Jukogyo KK
Priority to JP10370755A priority Critical patent/JP3080228B2/en
Publication of JP2000193201A publication Critical patent/JP2000193201A/en
Application granted granted Critical
Publication of JP3080228B2 publication Critical patent/JP3080228B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Control Of Turbines (AREA)
  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)

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】本発明は発電プラントの制御
方法に関する。さらに詳しくは、複数のボイラと複数の
蒸気タービンとを有する発電プラントにおいて、各ボイ
ラを最適な状態で稼働させることができる発電プラント
の制御方法に関する。
The present invention relates to a method for controlling a power plant. More specifically, the present invention relates to a power plant control method capable of operating each boiler in an optimal state in a power plant having a plurality of boilers and a plurality of steam turbines.

【0002】[0002]

【従来の技術】従来より、発電プラントにおいては複数
のボイラと複数の蒸気タービンとを組合せた構成が採用
されている。そして、かかる構成とされている発電プラ
ントの制御方法についても種々提案されているが、その
多くはボイラBと蒸気タービンTとが隣接して配置され
ているところから、図7に示すように、共通母管の圧力
によりボイラBのフィードバック制御をなすというもの
である(例えば、特開平3ー158601号公報、特開
平4ー55601号公報、実開平4ー229312号公
報等)。
2. Description of the Related Art Conventionally, a power plant has a configuration in which a plurality of boilers and a plurality of steam turbines are combined. Various methods of controlling a power plant having such a configuration have been proposed, but most of them have a boiler B and a steam turbine T arranged adjacent to each other, as shown in FIG. The feedback control of the boiler B is performed by the pressure of the common main pipe (for example, JP-A-3-158601, JP-A-4-55601, JP-A-4-229212, etc.).

【0003】しかるに、最近では新規発電プラントの建
設が、適当な立地条件の場所がないなどの問題のために
困難なところから、既設発電プラントにボイラBや蒸気
タービンTを増設することが多くなされている。この場
合、既設備との関係から増設されるボイラBや蒸気ター
ビンTが、既設のボイラBおよび蒸気タービンTと離れ
た場所に設置されることがしばしは起こる。そのため、
図7に示すような、共通母管の圧力によりボイラBのフ
ィードバック制御をなした場合、すなわち母管によりボ
イラBの代表圧力を計測し、その圧力を所定値に維持す
るために必要な燃料量(発熱量ベース)を算出し、その
燃料量を各ボイラBに分配することにより各ボイラBの
負荷配分をなすような方式を取った場合、蒸気管におけ
る圧力降下のために既設設備から離れた個所に設置され
たボイラBの圧力を所定圧力に維持できないことがあ
る。
[0003] However, recently, construction of a new power plant is difficult due to a problem such as lack of a suitable location, and therefore, a boiler B and a steam turbine T are often added to an existing power plant. ing. In this case, the boiler B and the steam turbine T that are added due to the relationship with the existing equipment are often installed at a location separated from the existing boiler B and the steam turbine T. for that reason,
When the feedback control of the boiler B is performed by the pressure of the common main pipe as shown in FIG. 7, that is, the representative pressure of the boiler B is measured by the main pipe, and the amount of fuel required to maintain the pressure at a predetermined value. When calculating the (heat generation base) and distributing the fuel amount to each of the boilers B, the load distribution of each of the boilers B is performed. In some cases, the pressure of the boiler B installed at the location cannot be maintained at a predetermined pressure.

【0004】[0004]

【発明が解決しようとする課題】本発明はかかる従来技
術の課題に鑑みなされたものであって、複数のボイラと
複数の蒸気タービンとがそれぞれ離れた場所に設置され
ていても、各ボイラの圧力を所定圧力に維持できる発電
プラントの制御方法を提供することを目的としている。
SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned problems of the prior art, and is intended to solve the problems of each of the boilers even if the plurality of boilers and the plurality of steam turbines are installed at separate places. It is an object of the present invention to provide a power plant control method capable of maintaining a pressure at a predetermined pressure.

【0005】[0005]

【課題を解決するための手段】本発明の発電プラントの
制御方法は、所要数のボイラと所要数の蒸気タービンと
を備える発電プラントの制御方法であって、電力デマン
ドに基づいて各蒸気タービンへの供給蒸気配分比および
各ボイラの発生蒸気配分比を設定し、ついで基準ボイラ
の設定蒸圧力を設定ししかるのち供給蒸気配分比
生蒸気配分比およびボイラ間流量に基づいて管路に発生
する管路抵抗と、前記設定蒸気圧力とを用いて基準ボイ
ラ以外の各ボイラの必要圧力を算出し、前記設定蒸気圧
力により前記基準ボイラを制御し、前記算出された各ボ
イラの必要圧力により各ボイラを制御することを特徴と
する。
A method for controlling a power plant according to the present invention is a method for controlling a power plant including a required number of boilers and a required number of steam turbines. steam supplies distribution ratio and sets the generated steam distribution ratio for each boiler, then set the configuration蒸圧force reference boiler, accordingly later steam supply distribution ratio, generating the conduit on the basis of the steam generated distribution ratio and the boiler between flow rate
The required line pressure of each boiler other than the reference boiler is calculated using the pipeline resistance to be set and the set steam pressure, and the set steam pressure is set.
The reference boiler is controlled by force , and each boiler is controlled by the calculated required pressure of each boiler.

【0006】本発明の発電プラントの制御方法において
は、例えば、各ボイラの必要圧力が下記式により算出さ
れる。
In the power plant control method of the present invention, for example, the required pressure of each boiler is calculated by the following equation.

【0007】[0007]

【数2】 (Equation 2)

【0008】本発明の発電プラントの制御方法において
は、隣接する各ボイラの管路抵抗が無視し得る場合、前
記各ボイラを接続する蒸気ラインの圧力を同ボイラの必
要圧力として制御がなされる。その場合、管路抵抗が無
視し得るとされたボイラ群の燃料量を発生蒸気配分比に
より制御することがなされる。
In the power plant control method of the present invention, when the line resistance of each adjacent boiler is negligible, the control is performed with the pressure of the steam line connecting each of the boilers as the required pressure of the same boiler. In this case, the amount of fuel in the boiler group for which the pipeline resistance is considered negligible is controlled by the generated steam distribution ratio.

【0009】また、蒸気タービンにおいて抽気がなされ
ている場合、蒸気タービン入口における蒸気量を計測
し、その計測値に基づいて供給蒸気配分比の設定がなさ
れる。
Further, when bleeding is performed in the steam turbine, the amount of steam at the inlet of the steam turbine is measured, and the supply steam distribution ratio is set based on the measured value.

【0010】[0010]

【作用】本発明は前記の如く構成されているので、複数
のボイラと複数の蒸気タービンとから構成される発電プ
ラントにおいて、管路抵抗が無視し得ない場合であって
も各ボイラの圧力を発生蒸気量配分に対応した圧力に制
御できる。
According to the present invention, as described above, in a power plant including a plurality of boilers and a plurality of steam turbines, the pressure of each boiler can be reduced even if the pipeline resistance cannot be ignored. The pressure can be controlled to correspond to the generated steam distribution.

【0011】[0011]

【発明の実施の形態】以下、添付図面を参照しながら本
発明を実施形態に基づいて説明するが、本発明はかかる
実施形態のみに限定されるものではない。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described based on embodiments with reference to the accompanying drawings, but the present invention is not limited to only such embodiments.

【0012】実施形態1 本発明の実施形態1の発電プラントの制御方法が適用さ
れている発電プラントを図1にブロック図で示す。な
お、図1中、符号Pはボイラ出口圧力、Bはボイラ、T
は蒸気タービン、fFは燃料量、fBはボイラ発生蒸気
量、fTはタービン供給蒸気量、fPは抽気量、CBはボ
イラマスター制御器、CTは発電量制御器、Wは電力、
Rは管路抵抗、矢符は流れの順方向(正方向)をそれぞ
れ示す。
Embodiment 1 FIG. 1 is a block diagram showing a power plant to which a method for controlling a power plant according to Embodiment 1 of the present invention is applied. In FIG. 1, reference symbol P denotes a boiler outlet pressure, B denotes a boiler, T
Amount of fuel steam turbine, f F is, f B is a boiler generating steam amount, f T is the turbine supply steam amount, f P is extracted amount, C B boiler master controller, C T is the power generation amount controlling unit, W is Power,
R indicates the pipeline resistance, and the arrows indicate the forward direction (positive direction) of the flow, respectively.

【0013】この発電プラントは、図1に示すように、
m缶のボイラBと、m台の蒸気タービンTと、これらの
ボイラBと蒸気タービンTとを連絡している蒸気ライン
と、燃料ラインとを主要構成要素として備えてなる。こ
の発電プラントにおいては、電力要求(電力デマンド)
に応じた電力負荷配分に基づいて各蒸気タービンTへの
供給蒸気量が決定され、ついでその供給蒸気量に応じて
ボイラBの負荷配分、すなわち発生蒸気量が決定され、
しかるのちその発生蒸気量を確保するための各ボイラB
の圧力(必要圧力)が算出される。
[0013] As shown in FIG.
It comprises m boilers B, m steam turbines T, a steam line connecting these boilers B and the steam turbine T, and a fuel line as main components. In this power plant, power demand (power demand)
The amount of steam to be supplied to each steam turbine T is determined based on the power load distribution according to the following, and then the load distribution of the boiler B, that is, the amount of generated steam, is determined according to the supplied steam amount.
After that, each boiler B to secure the generated steam amount
(Required pressure) is calculated.

【0014】次に、各ボイラBの必要圧力の算出につい
て説明する。
Next, the calculation of the required pressure of each boiler B will be described.

【0015】図1に示す発電プラントにおいて、電力負
荷配分から決定される蒸気タービンTの供給蒸気量配
分:fT(i)=αT(i)・fall、およびボイラ負荷配分と
して発生蒸気量配分:fB(i)=αB(i)・fallを設定す
る。
In the power plant shown in FIG. 1, the distribution of the amount of steam supplied to the steam turbine T determined from the distribution of electric power: f T (i) = α T (i) · f all , and the amount of generated steam as the boiler load distribution Allocation: fB (i) = αB (i) · fall is set.

【0016】ここに、 fall:全蒸気量 αT(i):供給蒸気配分比(ΣαT(i)=1 (i=1〜
m)) αB(i):発生蒸気配分比(ΣαB(i)=1 (i=1〜
m))
Where, f all : total steam amount α T (i) : supply steam distribution ratio (Σα T (i) = 1 (i = 1 to
m)) α B (i) : generated steam distribution ratio (Σα B (i) = 1 (i = 1 to
m))

【0017】前記関係を利用すると各ボイラB,B間の
流量f (i)(i+1)は、よく知られている代数的関係から
下記式(1)により表される。なお、添字(i)(i+
1)は(i)番目のボイラB(i)から(i+1)番目
のボイラB(i+1)へ蒸気が流れていることを示す。 f (i)(i+1)=(Σ(αB(k)−αT(k)))・fall (i
=1〜m−1) (1) また、前記式(1)を利用
すると各ボイラBの必要圧力PB(i)は、例えば第1ボイ
ラ(i=1)を基準とし、また圧力損失ΔPが2乗特性
(ΔP=sgn(f)・R・f 2)に従うとすると下記式(2)によ
り表される。
Using the above relationship, each boiler B, B
Flow rate f(i) (i + 1)Is from a well-known algebraic relationship
It is represented by the following equation (1). Note that the subscript (i) (i +
1) is from the (i) th boiler B (i) to the (i + 1) th boiler
Indicates that steam is flowing to boiler B (i + 1). f(i) (i + 1)= (Σ (αB (k)−αT (k))) ・ Fall (I
= 1 to m-1) (1) In addition, the above equation (1) is used.
Then, the required pressure P of each boiler BB (i)Is, for example, the first boy
(I = 1), and the pressure loss ΔP is squared.
(ΔP = sgn (f) ・ R ・ f Two) Is given by the following equation (2).
Is represented.

【0018】[0018]

【数3】 (Equation 3)

【0019】そして、前記式(2)において管路抵抗R
B(i),R (i)(i+1)は種々の公知の方法により算出可能
であるから、供給蒸気配分比:αT(i)、および発生蒸気
配分比:αB(i)を用いて各ボイラBにおける必要圧力P
B(i)が算出できる。ここで、管路抵抗Rの添字(i)
(i+1)は(i)番目のボイラB(i)と(i+1)
番目のボイラB(i+1)間の管路抵抗Rであることを
示す。なお、前記式(2)においては、基準ボイラBと
して第1ボイラB(1)が用いられているが、基準ボイ
ラBは任意のボイラとすることができる。
In the equation (2), the pipe resistance R
Since B (i) and R (i) (i + 1) can be calculated by various known methods, the supply steam distribution ratio: α T (i) and the generated steam distribution ratio: α B (i) Required pressure P in each boiler B
B (i) can be calculated. Here, the subscript (i) of the pipe resistance R
(I + 1) is the (i) th boiler B (i) and (i + 1)
This indicates that the pipeline resistance R is between the boilers B (i + 1). In the above equation (2), the first boiler B (1) is used as the reference boiler B, but the reference boiler B can be any boiler.

【0020】このように、この実施形態1によれば、複
数のボイラBがそれぞれ離れた場所に設置され、また複
数の蒸気タービンTもそれぞれ離れた場所に設置されて
いるため、蒸気ラインにおける圧力損失が無視できない
場合であっても各ボイラBの必要圧力が算出できるの
で、その圧力になるようボイラBを制御する、例えば燃
料量fFを制御することにより、所定の負荷配分に応じ
た発生蒸気量を確保できる。
As described above, according to the first embodiment, the plurality of boilers B are installed at distant locations, and the plurality of steam turbines T are also installed at distant locations. Even if the loss is not negligible, the required pressure of each boiler B can be calculated. Therefore, by controlling the boiler B so that the pressure becomes equal to the required pressure, for example, by controlling the fuel amount f F , the generation according to the predetermined load distribution The amount of steam can be secured.

【0021】実施形態2 本発明の実施形態2の発電プラントの制御方法が適用さ
れている発電プラントを図2にブロック図で示す。前記
式(2)を用いて各ボイラBの発生蒸発量を決定するた
めには、隣接するボイラB,B間の蒸気ラインに直列の
管路抵抗Rが存在するという条件(R (i-1)(i)+R
B(i-1)+RB(i)>0)が必要であるため、隣接するボイ
ラB,Bが近接し、その間の管路抵抗Rが無視し得るよ
うな場合(図2に示す例では、第1ボイラB(1)の管
路抵抗R (1)と第2ボイラB(2)の管路抵抗R (2)
よび第1ボイラB(1)と第2ボイラB(2)との間の
管路抵抗R (1)(2)が無視し得るとされている。)に
は、それらのボイラBの必要圧力は算出することができ
ても、それらのボイラBの発生蒸発量を決定し得ない。
そこで、この実施形態2では、その間の蒸気ラインを部
分的な母管と考えて処理するものである。すなわち、隣
接する各ボイラ(図示例では第1ボイラと第2ボイラ)
Bの必要圧力を、母管の圧力により代表させて実施形態
1と同様にして算出してその圧力によりボイラBの圧力
を制御するとともに、発生蒸気配分比:α B(i)に応じて
管路抵抗Rが無視し得るとされている各ボイラ(ボイラ
群)Bの燃料量fFを発生蒸気量配分比αB(i)により制
御するものである。
Embodiment 2 The control method of a power plant according to Embodiment 2 of the present invention is applied.
FIG. 2 is a block diagram showing the power plant that is being used. Said
Equation (2) is used to determine the amount of generated evaporation of each boiler B.
For this purpose, the steam line between the adjacent boilers B
The condition that the pipeline resistance R exists (R(i-1) (i)+ R
B (i-1)+ RB (i)> 0) is required, so that adjacent
La and B are close to each other, and the pipeline resistance R between them is negligible.
(In the example shown in FIG. 2, the pipe of the first boiler B (1)
Road resistance R(1)And the pipeline resistance R of the second boiler B (2)(2)You
And between the first boiler B (1) and the second boiler B (2)
Pipe resistance R(1) (2)Is ignorable. )
Can calculate the required pressure of those boilers B
However, the amount of generated evaporation of the boiler B cannot be determined.
Therefore, in the second embodiment, the steam line between
It is treated as a separate mother tube. That is, next to
Each boiler in contact (first boiler and second boiler in the example shown)
The embodiment in which the required pressure of B is represented by the pressure of the main pipe
Calculate in the same way as 1 and calculate the pressure of boiler B by the pressure.
And the generated steam distribution ratio: α B (i)In response to the
Each boiler (boiler) whose pipeline resistance R is considered negligible
Group) fuel amount f of BFGenerated steam distribution ratio αB (i)Controlled by
Control.

【0022】このように、この実施形態2によれば隣接
するボイラBが近接し、その間の管路抵抗Rが無視し得
るような場合であっても、各ボイラBの必要圧力および
管路抵抗Rが無視し得るとされているボイラ群の発生蒸
気量が算出できるので、その圧力になるようボイラBを
制御する、例えば燃料量fFを制御することにより、負
荷配分に応じた発生蒸気量を確保できる。
As described above, according to the second embodiment, even if the adjacent boilers B are close to each other and the pipeline resistance R therebetween is negligible, the required pressure and the pipeline resistance of each boiler B the generation amount of steam boilers group R is a negligible can be calculated, and controls the boiler B so that its pressure, for example by controlling the fuel amount f F, generating steam amount according to the load distribution Can be secured.

【0023】実施形態3 本発明の実施形態3の発電プラントの制御方法が適用さ
れている発電プラントを図3にブロック図で示す。この
実施形態3は実施形態1を改変したものであって、蒸気
タービンTにおいて抽気がなされているものである。こ
の場合は電力負荷配分と供給蒸気量配分が一意には決定
できないため、蒸気タービンT入口における蒸気量を計
測し、その計測により得られた蒸気量に基づいて供給蒸
気配分を決定するようにしてなるものである。すなわ
ち、 αT(i)=fT(i)/fall ここに、fall=ΣfT(i) (i=1,2,3,…,
m)
Third Embodiment FIG. 3 is a block diagram showing a power plant to which a power plant control method according to a third embodiment of the present invention is applied. The third embodiment is a modification of the first embodiment, in which bleeding is performed in the steam turbine T. In this case, since the power load distribution and the supply steam amount distribution cannot be uniquely determined, the steam amount at the inlet of the steam turbine T is measured, and the supply steam distribution is determined based on the steam amount obtained by the measurement. It becomes. That is, α T (i) = f T (i) / f all where f all = Σf T (i) (i = 1, 2, 3,...,
m)

【0024】このように、この実施形態3によれば、蒸
気タービンTにおいて抽気がなされている場合であって
も、その場合における各ボイラBの必要圧力が算出でき
るので、その圧力になるようボイラBを制御する、例え
ば燃料量fFを制御することにより負荷配分に応じた発
生蒸気量を確保できる。
As described above, according to the third embodiment, even when bleeding is performed in the steam turbine T, the required pressure of each boiler B in that case can be calculated. controlling the B, it can ensure the generation amount of steam in accordance with the load distribution by controlling, for example, fuel quantity f F.

【0025】なお、この実施形態1〜3ではボイラBの
缶数と蒸気タービンTの台数とは一致させられている
が、ボイラBの缶数と蒸気タービンTの台数とは必ずし
も一致させる必要はない。例えば、ボイラBの缶数が蒸
気タービンTの台数よりも多い場合には、適当な個所の
蒸気タービンTへの供給蒸気量配分比:αT(i)をゼロと
することにより対処でき、その逆にボイラBの缶数が蒸
気タービンTの台数よりも少ない場合には、適当な個所
のボイラBへの発生蒸気配分比:αB(i)をゼロとするこ
とにより対処できる。また、いわゆる台数制御を行う場
合には、稼働させないボイラBの発生蒸気配分比:α
B(i)をゼロとするとともに、稼働させない蒸気タービン
Tの供給蒸気量配分比:αT(i)をゼロとすることにより
対処できる。
In the first to third embodiments, the number of boilers B and the number of steam turbines T are matched, but the number of boilers B and the number of steam turbines T need not necessarily match. Absent. For example, when the number of cans of the boiler B is larger than the number of steam turbines T, it can be dealt with by setting the supply steam amount distribution ratio αT (i) to the steam turbine T at an appropriate location to zero. Conversely, when the number of cans in the boiler B is smaller than the number of steam turbines T, it can be dealt with by setting the generated steam distribution ratio αB (i) to the boiler B at an appropriate location to zero. When so-called unit control is performed, the generated steam distribution ratio of the boiler B that is not operated: α
This can be dealt with by setting B (i) to zero and setting the supply steam distribution ratio α T (i) of the steam turbine T that is not operated to zero.

【0026】[0026]

【実施例】以下、本発明をより具体的な実施例に基づい
てより具体的に説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described more specifically based on more specific embodiments.

【0027】実施例1 この実施例1は実施形態1を具体化したものであって、
図4に示すように、4缶のボイラBと4台の蒸気タービ
ンTとにより発電プラントを構成してなるものである。
この発電プラントの電力デマンドは48MWとされ、そ
れに対応した電力負荷配分から決定される第1〜第4蒸
気タービンT(1)〜T(4)の供給蒸気配分比:α
T(1)〜αT(4)はそれぞれ0.19,0.23,0.2
7,0.31とされ、またボイラ負荷配分から決定され
る第1〜第4ボイラB(1)〜B(4)の発生蒸気配分
比:αB(1)〜αB(4)はそれぞれ0.2,0.3,0.
3,0.2とされている。したがって、第1〜第4ボイ
ラB(1)〜B(4)の発生蒸気配分:fB(1)〜fB(4)
はそれぞれ80t/h,120t/h,120t/h,
80t/hとなり、また第1〜第4蒸気タービンT
(1)〜T(4)の供給蒸気配分:76t/h,92t
/h,108t/h,124t/hとなり、また各ボイ
ラB,B間の流量:f (i)(i+1)は、前記式(1)よ
り、第1ボイラB(1)および第2ボイラB(2)間の
流量:f (1)(2)が4t/hとなり、第2ボイラB
(2)および第3ボイラB(3)間の流量:f (2)(3)
は32t/hとなり、第3ボイラB(3)および第4ボ
イラB(4)間の流量:f (3)(4)は44t/hとな
る。そして、第1ボイラB(1)の管路抵抗:RB(1)
0.043kPa/(t/h)2、第2ボイラB(2)
の管路抵抗:RB(2)を0.035kPa/(t/
h)2、第3ボイラB(3)の管路抵抗:RB(3)を0.
035kPa/(t/h)2、第4ボイラB(4)の管
路抵抗:RB(4)を0.043kPa/(t/h)2、第
1ボイラB(1)および第2ボイラB(2)間の管路抵
抗:R (1)(2)を0.112kPa/(t/h)2、第2
ボイラB(2)および第3ボイラB(3)間の管路抵
抗:R (2)(3)を0.092kPa/(t/h)2、第3
ボイラB(3)および第4ボイラB(4)間の管路抵
抗:R (3)(4)を0.092kPa/(t/h)2とす
る。また、前記式(2)における基準圧力を第1ボイラ
B(1)において11.7MPaとする。
Example 1 Example 1 is an embodiment of the first embodiment.
As shown in FIG. 4, a power plant is constituted by four boilers B and four steam turbines T.
The power demand of this power plant is 48 MW, and the supply steam distribution ratio of the first to fourth steam turbines T (1) to T (4) determined from the corresponding power load distribution: α
T (1) to αT (4) are 0.19, 0.23, 0.2, respectively.
Is a 7,0.31, also the first to fourth boiler B (1) ~B (4) generating steam distribution ratio determined from boiler load allocation: α B (1) ~α B (4) , respectively 0.2, 0.3, 0.
3, 0.2. Therefore, the generated steam distribution of the first to fourth boilers B (1) to B (4): fB (1) to fB (4)
Are 80t / h, 120t / h, 120t / h,
80 t / h, and the first to fourth steam turbines T
(1) -T (4) supply steam distribution: 76 t / h, 92 t
/ H, 108 t / h, 124 t / h, and the flow rate f (i) (i + 1) between the boilers B, B is obtained from the first boiler B (1) and the second boiler B (1) according to the equation (1). The flow rate between the boilers B (2): f (1) (2) becomes 4 t / h, and the second boiler B
Flow rate between (2) and third boiler B (3): f (2) (3)
Is 32 t / h, and the flow rate f (3) (4) between the third boiler B (3) and the fourth boiler B (4) is 44 t / h. The pipeline resistance of the first boiler B (1): R B (1) is set to 0.043 kPa / (t / h) 2 , and the second boiler B (2)
Pipe resistance of RB (2) is 0.035 kPa / (t /
h) 2 , the pipeline resistance of the third boiler B (3): R B (3) is set to 0.
035 kPa / (t / h) 2 , pipeline resistance of the fourth boiler B (4): RB (4) is 0.043 kPa / (t / h) 2 , the first boiler B (1) and the second boiler B Pipe resistance between (2): R (1) (2) is 0.112 kPa / (t / h) 2 , second
Pipe resistance between the boiler B (2) and the third boiler B (3): R (2) (3) is set to 0.092 kPa / (t / h) 2 ,
The pipe resistance between the boiler B (3) and the fourth boiler B (4): R (3) (4) is set to 0.092 kPa / (t / h) 2 . The reference pressure in the above equation (2) is set to 11.7 MPa in the first boiler B (1).

【0028】したがって、前記式(2)より、第2ボイ
ラB(2)の圧力PB(2)は11.93MPa、第3ボイ
ラB(3)の圧力PB(3)は11.84MPa、第4ボイ
ラB(4)の圧力PB(4)は11.43MPaとなる。す
なわち、第1ボイラB(1)の圧力PB(1)を11.7M
Pa、第2ボイラB(2)の圧力PB(2)を11.93M
Pa、第3ボイラB(3)の圧力PB(3)を11.84M
Pa、第4ボイラB(4)の圧力PB(4)を11.43M
Paとなるように制御すれば、第1ボイラB(1)〜第
4ボイラB(4)において所望の発生蒸気量が得られ
る。
Therefore, from the above equation (2), the pressure P B (2) of the second boiler B (2) is 11.93 MPa, the pressure P B (3) of the third boiler B (3) is 11.84 MPa, The pressure P B (4) of the fourth boiler B (4) becomes 11.43 MPa. That is, the pressure P B (1) of the first boiler B (1) is increased to 11.7M.
Pa, the pressure P B (2) of the second boiler B (2) is set to 11.93M.
Pa, the pressure P B (3) of the third boiler B (3) is set to 11.84M.
Pa, the pressure P B (4) of the fourth boiler B (4) is set to 11.43M.
By controlling to be Pa, a desired amount of generated steam can be obtained in the first to fourth boilers B (1) to B (4).

【0029】実施例2 この実施例2は実施形態2を具体化したものであって、
図5に示すように、4缶のボイラBと4台の蒸気タービ
ンTとにより発電プラントを構成し、かつ第1ボイラB
(1)の管路抵抗R (1)、第2ボイラB(2)の管路抵
抗R (2)および第1ボイラB(1)と第2ボイラB
(2)との間の管路抵抗R (1)(2)がそれぞれゼロとさ
れてなるものである。この発電プラントの電力デマンド
は48MWとされ、それに対応した電力負荷配分から決
定される第1〜第4蒸気タービンT(1)〜T(4)の
供給蒸気配分比:αT(1)〜αT(4)はそれぞれ0.19,
0.23,0.27,0.31とされ、またボイラ負荷
配分から決定される第1〜第4ボイラB(1)〜B
(4)の発生蒸気配分比:αB(1)〜αB(4)はそれぞれ
0.2,0.3,0.3,0.2とされている。したが
って、第1〜第4ボイラB(1)〜B(4)の発生蒸気
配分:fB(1)〜fB(4)はそれぞれ80t/h,120t
/h,120t/h,80t/hとなり、また第1〜第
4蒸気タービンT(1)〜T(4)の供給蒸気配分:7
6t/h,92t/h,108t/h,124t/hと
なり、また各ボイラB,B間の流量:f (i)(i+1)は、
前記式(1)より、第1ボイラB(1)および第2ボイ
ラB(2)間の流量:f (1)(2)が4t/hとなり、第
2ボイラB(2)および第3ボイラB(3)間の流量:
(2)(3)は32t/hとなり、第3ボイラB(3)お
よび第4ボイラB(4)間の流量:f (3)(4)は44t
/hとなる。そして、第1ボイラB(1)の管路抵抗:
B(1 )を0.0kPa/(t/h)2、第2ボイラB
(2)の管路抵抗:RB(2)を0.0kPa/(t/h)
2、第3ボイラB(3)の管路抵抗:RB(3)を0.03
5kPa/(t/h)2、第4ボイラB(4)の管路抵
抗:RB(4)を0.043kPa/(t/h)2、第1ボ
イラB(1)および第2ボイラB(2)間の管路抵抗:
(1)(2)を0.0kPa/(t/h)2、第2ボイラB
(2)および第3ボイラ間の管路抵抗:R (2)(3)
0.092kPa/(t/h)2、第3ボイラB(3)
および第4ボイラB(4)間の管路抵抗:R (3)(4)
0.092kPa/(t/h)2とする。また、前記式
(2)における基準圧力を第1ボイラB(1)および第
2ボイラB(2)の共通母管において11.7MPaと
する。
Example 2 This example 2 is a specific example of the second embodiment.
As shown in FIG. 5, a power plant is composed of four boilers B and four steam turbines T, and the first boiler B
The pipeline resistance R (1) of (1) , the pipeline resistance R (2) of the second boiler B (2), and the first boiler B (1) and the second boiler B
The line resistances R (1) and (2) between (2) and (2) are each made zero. The power demand of this power plant is set to 48 MW, and the supply steam distribution ratio of the first to fourth steam turbines T (1) to T (4) determined from the corresponding power load distribution: α T (1) to α T (4) is 0.19,
0.23, 0.27, 0.31 and the first to fourth boilers B (1) to B (1) to B determined from the boiler load distribution.
The generated steam distribution ratios of (4): α B (1) to α B (4) are 0.2, 0.3, 0.3, and 0.2, respectively. Therefore, the generated steam distributions of the first to fourth boilers B (1) to B (4): fB (1) to fB (4) are 80 t / h and 120 t, respectively.
/ H, 120 t / h, 80 t / h, and the supply steam distribution of the first to fourth steam turbines T (1) to T (4): 7
6t / h, 92t / h, 108t / h, 124t / h, and the flow rate between the boilers B, B: f (i) (i + 1) is
From the above equation (1), the flow rate f (1) (2) between the first boiler B (1) and the second boiler B (2) is 4 t / h, and the second boiler B (2) and the third boiler Flow rate between B (3):
f (2) (3) is 32 t / h, and the flow rate between the third boiler B (3) and the fourth boiler B (4): f (3) (4) is 44 t / h.
/ H. Then, the pipeline resistance of the first boiler B (1):
RB (1 ) is set to 0.0 kPa / (t / h) 2 and the second boiler B
Pipe resistance of (2) : RB (2) is 0.0 kPa / (t / h)
2. Pipe resistance of the third boiler B (3): RB (3) is 0.03
5 kPa / (t / h) 2 , pipeline resistance of the fourth boiler B (4): RB (4) is 0.043 kPa / (t / h) 2 , the first boiler B (1) and the second boiler B Pipe resistance between (2):
R (1) (2) is set to 0.0 kPa / (t / h) 2 , and the second boiler B
Pipe resistance between (2) and the third boiler: R (2) (3) is 0.092 kPa / (t / h) 2 , and the third boiler B (3)
And the pipeline resistance between the fourth boiler B (4): R (3) (4) is 0.092 kPa / (t / h) 2 . Further, the reference pressure in the above equation (2) is set to 11.7 MPa in the common mother pipe of the first boiler B (1) and the second boiler B (2).

【0030】したがって、前記式(2)より、第3ボイ
ラB(3)の圧力PB(3)は12.11MPa、第4ボイ
ラB(4)の圧力PB(4)は11.70MPaとなる。す
なわち、第1ボイラB(1)および第2ボイラB(2)
の共通母管の圧力PB(1)を11.73MPa、第3ボイ
ラB(3)の圧力PB(3)を11.84MPa、第4ボイ
ラB(4)の圧力PB(4)を11.43MPaになるよう
に制御し、かつ第1ボイラB(1)と第2ボイラB
(2)との燃料配分比(fF(1):fF(2))を2:3に制
御すれば、第1ボイラB(1)〜第4ボイラB(4)に
おいて所望の発生蒸気量が得られる。
Therefore, from the above equation (2), the pressure P B (3) of the third boiler B (3) is 12.11 MPa, and the pressure P B (4) of the fourth boiler B (4) is 11.70 MPa. Become. That is, the first boiler B (1) and the second boiler B (2)
The pressure PB (1) of the common main pipe is 11.73 MPa, the pressure PB (3) of the third boiler B (3) is 11.84 MPa, and the pressure PB (4) of the fourth boiler B (4) is The first boiler B (1) and the second boiler B are controlled to be 11.43 MPa.
If the fuel distribution ratio (f F (1) : f F (2) ) to (2) is controlled to 2: 3, desired steam generated in the first to fourth boilers B (1) to B (4) can be obtained. The amount is obtained.

【0031】実施例3 この実施例3は実施形態3を具体化したものであって、
図6に示すように、4缶のボイラBと4台の蒸気タービ
ンTにより発電プラントを構成してなるものである。こ
の発電プラントの電力デマンドは24MWとされ、それ
に対応した電力負荷配分および蒸気タービンの抽気量:
P(i)は、第1蒸気タービンT(1)では抽気量:f
P(1)は38t/h、第2蒸気タービンT(2)では抽気
量:fP(2)は46t/h、第3蒸気タービンT(3)で
は抽気量:fP(3)は54t/h、第4蒸気タービンT
(4)では抽気量:fP(3)は62t/hから決定される
第1〜第4蒸気タービンT(1)〜T(4)への供給蒸
気量、すなわち第1〜第4蒸気タービンT(1)〜T
(4)の供給蒸気配分:76t/h,92t/h,10
8t/h,124t/hから、第1〜第4蒸気タービン
T(1)〜T(4)の供給蒸気量配分比:αT(1)〜α
T(4)はそれぞれ0.19,0.23,0.27,0.3
1とされ、またボイラ負荷配分から決定される第1〜第
4ボイラB(1)〜B(4)の発生蒸気配分比:αB(1)
〜αB(4)はそれぞれ0.2,0.3,0.3,0.2と
されている。したがって、第1〜第4ボイラB(1)〜
B(4)の発生蒸気配分:fB(1)〜fB(4)はそれぞれ8
0t/h,120t/h,120t/h,80t/hと
なり、また各ボイラB,B間の流量:f (i)(i+1)は、
前記式(1)より、第1ボイラB(1)および第2ボイ
ラB(2)間の流量:f (1)(2)が4t/hとなり、第
2ボイラB(2)および第3ボイラB(3)間の流量:
(2)(3)は32t/hとなり、第3ボイラB(3)およ
び第4ボイラB(4)間の流量:f (3)(4)は44t/
hとなる。そして、第1ボイラB(1)の管路抵抗:R
B(1)を0.043kPa/(t/h)2、第2ボイラB
(2)の管路抵抗:RB(2)を0.035kPa/(t/
h)2、第3ボイラB(3)の管路抵抗:RB(3)を0.
035kPa/(t/h)2、第4ボイラB(4)の管
路抵抗:RB (4)を0.043kPa/(t/h)2、第
1ボイラB(1)および第2ボイラB(2)間の管路抵
抗:R (1)(2)を0.112kPa/(t/h)2、第2
ボイラB(2)および第3ボイラB(3)間の管路抵
抗:R (2)(3)を0.092kPa/(t/h)2、第3
ボイラB(3)および第4ボイラB(4)間の管路抵
抗:R (3)(4)を0.092kPa/(t/h)2
し、、そして前記式(2)における基準圧力を第1ボイ
ラB(1)において11.7MPaとする。
Example 3 Example 3 is an embodiment of the third embodiment.
As shown in FIG. 6, a power plant is configured by four boilers B and four steam turbines T. The power demand of this power plant is assumed to be 24 MW, the corresponding power load distribution and the amount of bleed air of the steam turbine:
f P (i) is the amount of extracted air: f in the first steam turbine T (1).
P (1) is 38 t / h, the amount of bleed air in the second steam turbine T (2): f P (2) is 46 t / h, and the amount of bleed air in the third steam turbine T (3): f P (3) is 54 t. / H, fourth steam turbine T
In (4), the amount of extracted air: f P (3) is determined from 62 t / h, and is the amount of steam supplied to the first to fourth steam turbines T (1) to T (4), that is, the first to fourth steam turbines. T (1)-T
(4) Supply steam distribution: 76 t / h, 92 t / h, 10
From 8 t / h and 124 t / h, the supply steam amount distribution ratio of the first to fourth steam turbines T (1) to T (4): α T (1) to α
T (4) is 0.19, 0.23, 0.27, 0.3, respectively.
1, and the generated steam distribution ratio of the first to fourth boilers B (1) to B (4) determined from the boiler load distribution: α B (1)
To α B (4) are 0.2, 0.3, 0.3, and 0.2, respectively. Therefore, the first to fourth boilers B (1) to
Distribution of generated steam of B (4): f B (1) to f B (4) are each 8
0 t / h, 120 t / h, 120 t / h, 80 t / h, and the flow rate between the boilers B, B: f (i) (i + 1) is
From the above equation (1), the flow rate f (1) (2) between the first boiler B (1) and the second boiler B (2) is 4 t / h, and the second boiler B (2) and the third boiler Flow rate between B (3):
f (2) (3) is 32 t / h, and the flow rate between the third boiler B (3) and the fourth boiler B (4): f (3) (4) is 44 t / h.
h. Then, the pipeline resistance of the first boiler B (1): R
B (1) is 0.043 kPa / (t / h) 2 , the second boiler B
Pipe resistance of (2) : RB (2) is set to 0.035 kPa / (t /
h) 2 , the pipeline resistance of the third boiler B (3): R B (3) is set to 0.
035 kPa / (t / h) 2 , pipeline resistance of the fourth boiler B (4): R B (4) is 0.043 kPa / (t / h) 2 , the first boiler B (1) and the second boiler B Pipe resistance between (2): R (1) (2) is 0.112 kPa / (t / h) 2 ,
Pipe resistance between the boiler B (2) and the third boiler B (3): R (2) (3) is set to 0.092 kPa / (t / h) 2 ,
The pipe resistance between the boiler B (3) and the fourth boiler B (4): R (3) (4) is set to 0.092 kPa / (t / h) 2 , and the reference pressure in the above equation (2) is In the first boiler B (1), the pressure is set to 11.7 MPa.

【0032】したがって、前記式(2)より、第2ボイ
ラB(2)の圧力PB(2)は11.93MPa、第3ボイ
ラB(3)の圧力PB(3)は11.83MPa、第4ボイ
ラB(4)の圧力PB(4)は11.43MPaとなる。す
なわち、第1ボイラB(1)の圧力PB(1)を11.7M
Pa、第2ボイラB(2)の圧力PB(2)を11.93M
Pa、第3ボイラB(3)の圧力PB(3)を11.84M
Pa、第4ボイラB(4)の圧力PB(4)を11.43M
Paとなるように制御すれば、例えば燃料量f F(1)〜f
F(4)を制御すれば、第1ボイラB(1)〜第4ボイラB
(4)において所望の発生蒸気量が得られる。
Therefore, from the above equation (2), the second boy
La B (2) pressure PB (2)Is 11.93MPa, 3rd boil
La B (3) pressure PB (3)Is 11.83MPa, 4th boil
La B (4) pressure PB (4)Becomes 11.43 MPa. You
That is, the pressure P of the first boiler B (1)B (1)11.7M
Pa, pressure P of second boiler B (2)B (2)11.93M
Pa, pressure P of the third boiler B (3)B (3)11.84M
Pa, pressure P of the fourth boiler B (4)B (4)11.43M
If the fuel pressure is controlled to be Pa, the fuel amount f F (1)~ F
F (4)Is controlled, the first boiler B (1) to the fourth boiler B
In (4), a desired amount of generated steam is obtained.

【0033】以上、本発明を実施形態および実施例に基
づいて説明してきたが、本発明はかかる実施形態および
実施例に限定されるものではなく、種々改変が可能であ
る。例えば、実施形態3および実施例3では蒸気タービ
ンは全てについて抽気がなされているが、必ずしも全て
の蒸気タービンから抽気される必要はない。また、実施
形態2では隣接する2缶の管路抵抗が無視し得るとされ
ているが、3缶もしくはそれ以上とされてもよい。
Although the present invention has been described based on the embodiments and the examples, the present invention is not limited to the embodiments and the examples, and various modifications are possible. For example, in Embodiment 3 and Example 3, bleeding is performed for all steam turbines, but it is not always necessary to bleed from all steam turbines. In the second embodiment, the pipe resistance of two adjacent cans is negligible, but may be three or more.

【0034】[0034]

【発明の効果】以上詳述したように、本発明によれば、
複数のボイラと複数の蒸気タービンとから構成される発
電プラントにおいて、管路抵抗が無視し得ない場合であ
っても各ボイラの圧力を発生蒸気量配分に対応した圧力
に制御できるという優れた効果が得られる。
As described in detail above, according to the present invention,
In a power plant consisting of a plurality of boilers and a plurality of steam turbines, an excellent effect that the pressure of each boiler can be controlled to a pressure corresponding to the generated steam amount distribution even when the pipeline resistance cannot be ignored. Is obtained.

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

【図1】本発明の実施形態1にかかる発電プラントのブ
ロック図である。
FIG. 1 is a block diagram of a power plant according to Embodiment 1 of the present invention.

【図2】本発明の実施形態2にかかる発電プラントのブ
ロック図である。
FIG. 2 is a block diagram of a power plant according to Embodiment 2 of the present invention.

【図3】本発明の実施形態3にかかる発電プラントのブ
ロック図である。
FIG. 3 is a block diagram of a power plant according to Embodiment 3 of the present invention.

【図4】本発明の実施例1にかかる発電プラントのブロ
ック図である。
FIG. 4 is a block diagram of a power plant according to the first embodiment of the present invention.

【図5】本発明の実施例2にかかる発電プラントのブロ
ック図である。
FIG. 5 is a block diagram of a power plant according to a second embodiment of the present invention.

【図6】本発明の実施例3にかかる発電プラントのブロ
ック図である。
FIG. 6 is a block diagram of a power plant according to a third embodiment of the present invention.

【図7】従来の発電プラントのブロック図である。FIG. 7 is a block diagram of a conventional power plant.

【符号の説明】[Explanation of symbols]

B ボイラ T 蒸気タービン fF 燃料量 fB ボイラ発生蒸気量 fT タービン供給蒸気量 fP 抽気量 CB ボイラマスター制御器 CT 発電量制御器 P ボイラ出口圧力 W 電力 R 管路抵抗B Boiler T Steam turbine f F Fuel amount f B Boiler generated steam amount f T Turbine supply steam amount f P Bleed amount C B Boiler master controller C T Power generation amount controller P Boiler outlet pressure W Power R Pipe resistance

フロントページの続き (72)発明者 伊藤 俊郎 東京都江東区南砂2丁目11番1号 川崎 重工業株式会社 東京設計事務所内 (72)発明者 和佐田 憲彦 東京都江東区南砂2丁目11番1号 川崎 重工業株式会社 東京設計事務所内 (72)発明者 羽鳥 光俊 東京都江東区南砂2丁目11番1号 川崎 重工業株式会社 東京設計事務所内 (56)参考文献 特開 平4−55601(JP,A) 特開 平3−158601(JP,A) (58)調査した分野(Int.Cl.7,DB名) F22B 35/00 F01D 17/00 F01D 17/24 F01K 7/38 102 Continued on the front page (72) Inventor Toshiro Ito 2-11-1, Minamisuna, Koto-ku, Tokyo Kawasaki Heavy Industries, Ltd. Tokyo Design Office (72) Inventor Norihiko Wasada 2-1-1, Minamisuna, Koto-ku, Tokyo Kawasaki Heavy Industries, Ltd. Tokyo Design Office (72) Inventor Mitoshitoshi Hatori 2-1-1, Minamisuna, Koto-ku, Tokyo Kawasaki Heavy Industries, Ltd. Tokyo Design Office (56) References JP-A-4-55601 (JP, A) Kaihei 3-158601 (JP, A) (58) Fields studied (Int. Cl. 7 , DB name) F22B 35/00 F01D 17/00 F01D 17/24 F01K 7/38 102

Claims (5)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 所要数のボイラと所要数の蒸気タービン
とを備える発電プラントの制御方法であって、電力デマ
ンドに基づいて各蒸気タービンへの供給蒸気配分比およ
び各ボイラの発生蒸気配分比を設定し、ついで基準ボイ
ラの設定蒸圧力を設定ししかるのち供給蒸気配分比
発生蒸気配分比およびボイラ間流量に基づいて管路に発
生する管路抵抗と、前記設定蒸気圧力とを用いて基準ボ
イラ以外の各ボイラの必要圧力を算出し、前記設定蒸気
圧力により前記基準ボイラを制御し、前記算出された各
ボイラの必要圧力により各ボイラを制御することを特徴
とする発電プラントの制御方法。
1. A method for controlling a power plant including a required number of boilers and a required number of steam turbines, wherein a distribution ratio of supply steam to each steam turbine and a distribution ratio of generated steam of each boiler are determined based on an electric power demand. set, then set the configuration蒸圧force reference boiler, accordingly later steam supply distribution ratio,
Generated in pipeline based on generated steam distribution ratio and flow rate between boilers
And pipeline resistance to live, to calculate the required pressure for each boiler other than the reference boiler using said setting steam pressure, the setting steam
A control method for a power plant, wherein the reference boiler is controlled by pressure, and each boiler is controlled by the calculated required pressure of each boiler.
【請求項2】 各ボイラの必要圧力が下記式により算出
されることを特徴とする請求項1記載の発電プラントの
制御方法。 【数1】
2. The method according to claim 1, wherein the required pressure of each boiler is calculated by the following equation. (Equation 1)
【請求項3】 隣接する各ボイラの管路抵抗が無視し得
る場合、前記各ボイラを接続する蒸気ラインの圧力を同
ボイラの必要圧力とすることを特徴とする請求項1記載
の発電プラントの制御方法。
3. The power plant according to claim 1, wherein when the line resistance of each adjacent boiler is negligible, the pressure of the steam line connecting each of the boilers is set to a required pressure of the boiler. Control method.
【請求項4】 ボイラの管路抵抗およびボイラ間の管路
抵抗が無視し得るとされているボイラ群の燃料量を発生
蒸気量配分比により制御することを特徴とする請求項3
記載の発電プラントの制御方法。
4. The boiler's pipeline resistance and the pipeline resistance between the boilers are controlled to be negligible, and the fuel amount of the boiler group is controlled by the generated steam distribution ratio.
The control method of the power plant according to the above.
【請求項5】 蒸気タービンにおいて抽気がなされてい
る場合、蒸気タービン入口における蒸気量を計測し、そ
の計測値に基づいて供給蒸気配分比の設定がなされるこ
とを特徴とする請求項1記載の発電プラントの制御方
法。
5. The steam turbine according to claim 1, wherein when bleeding is performed in the steam turbine, a steam amount at a steam turbine inlet is measured, and a supply steam distribution ratio is set based on the measured value. Power plant control method.
JP10370755A 1998-12-25 1998-12-25 Power plant control method Expired - Fee Related JP3080228B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10370755A JP3080228B2 (en) 1998-12-25 1998-12-25 Power plant control method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10370755A JP3080228B2 (en) 1998-12-25 1998-12-25 Power plant control method

Publications (2)

Publication Number Publication Date
JP2000193201A JP2000193201A (en) 2000-07-14
JP3080228B2 true JP3080228B2 (en) 2000-08-21

Family

ID=18497544

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Link
JP (1) JP3080228B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2023123154A (en) * 2022-02-24 2023-09-05 三菱重工業株式会社 Piping unit for boiler system, modification method of boiler system, and boiler system

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