JPS60233302A - Main steam pressure drop prevention device - Google Patents
Main steam pressure drop prevention deviceInfo
- Publication number
- JPS60233302A JPS60233302A JP8830084A JP8830084A JPS60233302A JP S60233302 A JPS60233302 A JP S60233302A JP 8830084 A JP8830084 A JP 8830084A JP 8830084 A JP8830084 A JP 8830084A JP S60233302 A JPS60233302 A JP S60233302A
- Authority
- JP
- Japan
- Prior art keywords
- pressure
- main steam
- load
- steam pressure
- prevention device
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
- F01D17/00—Regulating or controlling by varying flow
- F01D17/20—Devices dealing with sensing elements or final actuators or transmitting means between them, e.g. power-assisted
- F01D17/22—Devices dealing with sensing elements or final actuators or transmitting means between them, e.g. power-assisted the operation or power assistance being predominantly non-mechanical
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Control Of Turbines (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の利用分野〕
本発明は、蒸気タービン変圧プラントにおける主蒸気圧
力低下防止装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a main steam pressure drop prevention device in a steam turbine variable pressure plant.
第1図に標準的な蒸気タービン発電プラントの構成を示
す。ボイラ1からの主蒸気は、主蒸気止め弁2(以下M
SVと称す)。蒸気加減弁3 (SCV )を通り、高
圧タービン4 (以下HPTbと称す)へ流入する。H
PT)、で仕事をした蒸気は再熱器5で加熱され、再熱
蒸気止め弁6(以下R8Uと称す)。インターセプト弁
7(以下ICVと称す)を通り、中圧タービン8(以下
■p丁、と称す)へ流入する。■PTl、、を出た蒸気
は匠気タービン9 (以下LPTbと称す)に流入する
。その後、復水器10で復水され、低圧ヒータ11.脱
気器12、給水ポンプ13.高圧ヒータ14等を通って
ボイラに供給される。Figure 1 shows the configuration of a standard steam turbine power plant. Main steam from boiler 1 is passed through main steam stop valve 2 (hereinafter referred to as M
(referred to as SV). It passes through a steam control valve 3 (SCV) and flows into a high pressure turbine 4 (hereinafter referred to as HPTb). H
The steam that has done work in the reheater 5 is heated by the reheater 5, and then the reheat steam stop valve 6 (hereinafter referred to as R8U). It passes through an intercept valve 7 (hereinafter referred to as ICV) and flows into an intermediate pressure turbine 8 (hereinafter referred to as ``P''). ■The steam leaving the PTl flows into the Takumi turbine 9 (hereinafter referred to as LPTb). Thereafter, the water is condensed in a condenser 10, and is heated to a low pressure heater 11. Deaerator 12, water pump 13. It is supplied to the boiler through the high pressure heater 14 and the like.
第2図に、変圧プラントの負荷に対する主蒸気圧力の関
係を示す。変圧プラントでは、負荷Lt以下及び負荷I
、?以」二において、主蒸気圧力は各各Pl、P2一定
である。L、1 からL2まで主蒸気圧力を変化させる
事により、負荷を増減させる。Figure 2 shows the relationship between the main steam pressure and the load of the transformer plant. In transformer plants, loads below Lt and loads I
,? In the following, the main steam pressure is constant for each of Pl and P2. The load is increased or decreased by changing the main steam pressure from L,1 to L2.
第3図に変圧プラントの弁開度に対する負荷及び主蒸気
圧力の関係を示す。主蒸気圧力P、からP2まで変圧運
転を行なう場合、Cv開度はX点でほぼ一定開度を保つ
。X点におけるCV開度は絞り損失を考慮し、損失の少
ない弁全開点近傍が一般に選択される。Fig. 3 shows the relationship between the load and main steam pressure with respect to the valve opening of the transformer plant. When variable pressure operation is performed from the main steam pressure P to P2, the Cv opening degree remains approximately constant at point X. The CV opening degree at point X takes throttle loss into consideration, and is generally selected near the valve full-opening point where loss is small.
第4図に変圧プラントにおける起動パターンの一例を示
す。タービンへ蒸気を供給した時点(通気時)において
、蒸気圧力は定格圧力のa%であるが、定格負荷のb%
点でCvを全開点近傍までいた後論々に圧力を上昇させ
て定格出力のC%点で定格圧力となる様に運転される。FIG. 4 shows an example of a startup pattern in a voltage transformation plant. At the time of supplying steam to the turbine (during ventilation), the steam pressure is a% of the rated pressure, but b% of the rated load.
After Cv reaches near the full-open point at point Cv, the pressure is naturally increased to reach the rated pressure at point C% of the rated output.
さて蒸気タービンは一般に主蒸気圧力低下防止装置が設
置されている。この装置は、タービン運転中ボイラー制
御異常等により主蒸気圧力が急激に低下し、水が蒸気タ
ービンに流入またはHPTb最終段が湿り状態となり、
過大なスラスト力が蒸気タービンにかかることにより、
過大な熱応力の発生、スラスト軸受摩耗・振動発生、静
・動翼接触等の異常が発生することを防止する目的で設
置されており、主蒸気圧力が規定値まで下がるとCvを
絞り始め(すなわち負荷を減少させ)更に主蒸気圧力が
下がり続ける場合は最終的にタービン無負荷までCvを
絞る機能を有する。Now, steam turbines are generally equipped with a main steam pressure drop prevention device. This system is designed to prevent main steam pressure from dropping rapidly due to boiler control abnormalities during turbine operation, causing water to flow into the steam turbine or the HPTb final stage to become wet.
Due to excessive thrust force being applied to the steam turbine,
It is installed to prevent abnormalities such as excessive thermal stress, thrust bearing wear/vibration, and static/rotor blade contact, and when the main steam pressure falls to a specified value, it starts to throttle the Cv ( In other words, if the main steam pressure continues to decrease (by reducing the load), it has the function of ultimately reducing Cv to no load on the turbine.
まず、従来例のうち、定圧蒸気タービンの機械油圧式ガ
バナを例にとって説明する。主蒸気圧力低下防止装置は
、タービン制御装置が内蔵されたタービン前側軸受箱内
に他のタービン制御装置と共に設けられている。First, among conventional examples, a mechanical-hydraulic governor for a constant pressure steam turbine will be explained as an example. The main steam pressure drop prevention device is provided together with other turbine control devices in a turbine front bearing box in which the turbine control device is built.
主蒸気圧力低下防止装置は、ボイラからの主蒸気圧力が
正常な値を保つ限り作動せず、一般に圧力が定格の約9
0%以下に低下すると作動を開始して、CVを開じ始め
る。主蒸気圧力低下防止装置は7〜13%の固定率を持
っており、主蒸気圧力が定格の83〜71%に達すると
、Cvを無負荷開度まで閉じる。The main steam pressure drop prevention device does not operate as long as the main steam pressure from the boiler maintains a normal value, and generally the pressure is approximately 90% below the rated pressure.
When it drops to 0% or less, it starts operating and begins to open the CV. The main steam pressure drop prevention device has a fixed rate of 7 to 13%, and when the main steam pressure reaches 83 to 71% of the rated value, Cv is closed to the no-load opening.
このような主蒸気圧力の急激な低下はボイラチューブ内
での水発生等のボイラ側の異常発生によるものであり同
時に主蒸気温度の低下も起こる。Such a sudden drop in main steam pressure is due to an abnormality occurring on the boiler side, such as water generation within the boiler tube, and at the same time, a drop in main steam temperature also occurs.
前述した如くタービンに水が流入する事は、エロージョ
ン、局部冷却による熱応力発生等、タービンにとって極
めて重大な事故発生の原因となるので、通常主蒸気圧力
の低下を検知してタービンを無負荷流量まで絞り込む装
置が設けである。As mentioned above, water flowing into the turbine can cause extremely serious accidents for the turbine, such as erosion and thermal stress caused by local cooling. A device is provided to narrow down the results.
機械式主蒸気圧力低下防止装置を示す図5において、主
蒸気圧力変化は、圧力検出器15変換器16を通り、空
気圧力の変化に変換されて、ベロー17に入る。主蒸気
圧力が低下すると、バネ18とベローが組込まれた圧力
検出部において、ベローが下方向に動き、パイロットピ
ストン19を下方向に動作させる。そして、アンロード
ピストン20の上側に制御油が供給され、アンロードピ
ストンは下方向に動く。アンロードピストンはスピード
リレーからタービンの加減弁を動作させるサーボモータ
パイロットピストンに通じるロッドの途中に設けられた
回転レバー21に連通されているので、下方向のアンロ
ードピストンの動きにより、サーボモータを閉方向に動
作させて加減弁を絞り込む。In FIG. 5, which shows a mechanical main steam pressure drop prevention device, the main steam pressure change passes through the pressure detector 15 converter 16 and is converted into a change in air pressure and enters the bellows 17. When the main steam pressure decreases, the bellows move downward in the pressure detection section incorporating the spring 18 and the bellows, causing the pilot piston 19 to move downward. Control oil is then supplied to the upper side of the unload piston 20, and the unload piston moves downward. The unload piston is connected to a rotary lever 21 installed in the middle of the rod that leads from the speed relay to the servo motor pilot piston that operates the turbine control valve, so the downward movement of the unload piston causes the servo motor to operate. Operate in the closing direction to narrow down the control valve.
通常使用される主蒸気圧力低下防止装置は、前述したよ
うに、バネとベローとの釣り合いによって、アンロード
ピストンを動作させるため、定格主蒸気圧力で動作する
ようにレバー系統を設定した後は、同じ圧力でしかアン
ロードピストンは動作しない。すなわち、一般に第6図
に示す如く主蒸気圧力が定格圧の90%まで低下すると
Cvを絞り始め、更に80%まで下がると、Cvはター
ビン無負荷相当位置まで、閉じられるものである。As mentioned above, the normally used main steam pressure drop prevention device operates the unload piston by the balance between the spring and the bellows, so after setting the lever system to operate at the rated main steam pressure, The unload piston will only operate at the same pressure. That is, generally, as shown in FIG. 6, when the main steam pressure decreases to 90% of the rated pressure, Cv starts to be throttled, and when it further decreases to 80%, Cv is closed to a position corresponding to no load on the turbine.
したがって、第4図に示すような主蒸気圧力を定格圧力
のa%から0%まで変化させる変圧プラントにおいては
、変圧運転中、主蒸気圧力低下防止装置を除外して、プ
ラントを運転しなければならなかった。この除外操作は
、第5図において、変圧運転中ベローに人為的に、疑似
圧力を加えて、アンロードピストンが、あたかも、定格
主蒸気圧力を保つがごとく、ベローを上げておくもので
ある。従って、変圧運転中、ボイラ異常が発生し、主蒸
気圧力が低下しても、Cvを絞り込み、タービンを保護
することができないという欠点があった。Therefore, in a variable pressure plant that changes the main steam pressure from a% to 0% of the rated pressure as shown in Figure 4, the plant must be operated without the main steam pressure drop prevention device during variable pressure operation. did not become. This exclusion operation, as shown in FIG. 5, involves artificially applying pseudo pressure to the bellows during variable pressure operation to raise the bellows as if the unloading piston were to maintain the rated main steam pressure. Therefore, even if a boiler abnormality occurs and the main steam pressure decreases during variable pressure operation, there is a drawback that it is not possible to reduce Cv and protect the turbine.
本発明の目的は、変圧運転中、主蒸気圧力低下を検知し
、加減弁を絞り込むための主蒸気圧力低下防止装置を提
供するにある。SUMMARY OF THE INVENTION An object of the present invention is to provide a main steam pressure drop prevention device for detecting a main steam pressure drop and throttling a control valve during pressure variable operation.
本発明は、変圧運転中主蒸気圧力の変化を検知し、主蒸
気圧力を空気圧力に変換させる過程において、発電機の
出力またはタービン負荷信号を取り込み、主蒸気圧力と
負荷の変化を予め定めた、設定値との比較によって、加
減弁の絞り込みを制御する事を特徴とするものである。The present invention detects changes in main steam pressure during variable pressure operation, and in the process of converting main steam pressure into air pressure, captures the generator output or turbine load signal, and predetermines changes in main steam pressure and load. , is characterized by controlling the narrowing of the adjustment valve by comparing it with a set value.
本発明は電気油圧式ガバナ及び機械油圧式ガバナにおけ
る主蒸気圧力低下防止装置に関する。まず電圧油圧式ガ
バナの場合を示す。第7図に電気油圧式ガバナの信号処
理ブロック線図を示す。The present invention relates to a main steam pressure drop prevention device in an electro-hydraulic governor and a mechanical-hydraulic governor. First, the case of a voltage-hydraulic governor will be shown. FIG. 7 shows a signal processing block diagram of the electrohydraulic governor.
主蒸気圧力は、主蒸気止め弁より上流側に取付けられた
圧力検出器により検出され、変換器により、電気信号と
して得られる一方負荷信号は、本例では発電機出力から
得るものとしたが、周知のごとく、タービン負荷は、高
圧第一段以後の段落の蒸気圧力に比例するため、負荷の
検出方法として高圧タービン第一段後の圧力または中圧
タービン第一段後等の蒸気圧力を測定する事によっても
得られる。The main steam pressure is detected by a pressure detector installed upstream of the main steam stop valve, and is obtained as an electrical signal by a converter, while the load signal is obtained from the generator output in this example. As is well known, the turbine load is proportional to the steam pressure in the stages after the high-pressure first stage, so the load can be detected by measuring the pressure after the first stage of the high-pressure turbine or the steam pressure after the first stage of the intermediate-pressure turbine. It can also be obtained by doing.
蒸気タービンは、通常給電指令に基づき、負荷を定め運
転している(設定負荷Ls)。変圧プラントでは、前述
した第2図に示すように、設定負荷Lsが変圧領域の場
合、一義的に設定圧力Psが定まり、負荷変化に対し、
ボイラの主蒸気圧力を制御する事により、加減弁開度を
ほぼ一定のまま、運転を行なっている。The steam turbine normally operates with a determined load based on the power supply command (set load Ls). In a transformer plant, as shown in Fig. 2 mentioned above, when the set load Ls is in the transformer pressure region, the set pressure Ps is uniquely determined, and with respect to load changes,
By controlling the main steam pressure of the boiler, operation is performed with the opening of the control valve kept almost constant.
電気油圧式ガバナでは、速度制御、負荷制御はタービン
周り各部に取り付けられた、検出器の信号を制御用計算
機に取り込み、計算器内部で演算し、加減弁開度信号等
を出力する。In an electro-hydraulic governor, speed control and load control are performed by inputting signals from detectors attached to various parts around the turbine into a control computer, performing calculations within the computer, and outputting a control valve opening signal, etc.
制御用計算機において、設定負荷Ls、実圧力P、実負
荷Loの電気信号が入力されると、設定圧力計算機22
において第8図に示す負荷−圧力線図から設定負荷Ls
に対する設定圧力Psがめられる。次に、絞り込み圧力
設定器23において、設定圧力Psの90%相当の加減
弁絞り込み開始圧力P eo(= 0 、9 P s
)と設定圧力Psの80%相当の加減弁憾り込み終了圧
力Pao(=0.8 P s)をめて、運転中、単位時
間毎にP2Oは比較器24で、実圧力Pと比較する。P
> P e。In the control computer, when the electric signals of the set load Ls, the actual pressure P, and the actual load Lo are input, the set pressure calculator 22
From the load-pressure diagram shown in Fig. 8, set load Ls
The set pressure Ps is determined. Next, in the throttling pressure setting device 23, a regulating valve throttling start pressure Peo (= 0, 9 Ps
) and the adjustment valve stagnation end pressure Pao (=0.8 Ps) equivalent to 80% of the set pressure Ps, and during operation, P2O is compared with the actual pressure P using the comparator 24 every unit time. . P
> P e.
の関係が成立する時は、主蒸気圧力(実圧力P)が加減
弁絞り込み開始圧力より高く、タービン発生負荷の絞り
込みは不要となる。よって以後の信号処理計算過程は省
略される。P < P 90の関係が成立する時は、タ
ービン発生負荷の絞り込みを行なう。目標負荷設定器2
5において第8図に示すように、無負荷で設定圧力の8
0%に相当する加減弁絞り込み終了圧力Pao(座標(
0,Pso))と設定負荷Lsにおいて、加減弁絞り込
み開始圧力Pno(座i1 (L s 、 P2O)
)を結ぶ直線A式上を移動する様に負荷を制御する。When the following relationship holds true, the main steam pressure (actual pressure P) is higher than the regulating valve throttle start pressure, and there is no need to throttle the turbine generated load. Therefore, the subsequent signal processing calculation process is omitted. When the relationship P < P 90 is established, the turbine generated load is narrowed down. Target load setter 2
5, the set pressure is 8 with no load, as shown in Figure 8.
Adjustment valve throttle end pressure Pao (coordinates (
0, Pso)) and the set load Ls, the regulator valve throttling start pressure Pno (seat i1 (Ls, P2O)
) The load is controlled so that it moves on the straight line A that connects the
目標負荷設定器内では、(A)式を変形したCB)式に
より、負荷を制御する。すなわち、時時刻々制御用計算
器内部に取り込まれた実圧力PはP2Oと比較され、P
< P 90の条件が成立した場合にのみB式のPに
代入し、絞り込み時の負荷■。In the target load setter, the load is controlled using equation (CB), which is a modification of equation (A). That is, the actual pressure P taken into the control calculator from time to time is compared with P2O, and P
< P Substitute for P in formula B only when the condition of 90 is satisfied, and the load when narrowing down ■.
をめる。I put it on.
(B)式で算出された絞り込みの負荷は変圧プラントに
おける全ての運転範囲に適用できる。すなわち、第9図
において100%定格運転中の目標負荷設定器の動作は
図中a−b−c点上を移動し、変圧過室、例えば75%
負荷運転中ではd−e−f点上を移動し、低負荷領域、
例えば25%負荷ではg −h −iとなる。The narrowing load calculated by equation (B) can be applied to all operating ranges in the transformer plant. In other words, in Fig. 9, the operation of the target load setter during 100% rated operation moves on points a-b-c in the figure, and the over-transformation chamber, for example, 75%
During load operation, it moves on the d-e-f point, and moves to the low load area,
For example, at 25% load, it becomes g - h - i.
目標負荷設定器から出た目標負荷信号■、は実負荷T−
oとの差(L −L o )を計算し、PI演算器26
により加減弁制御信号(ET−信号)に変換され、加減
弁駆動部27に送られる。L −L oが負の場合に、
加減弁の絞り込みが行なオ〕れる。The target load signal ■ output from the target load setter is the actual load T-
PI calculation unit 26 calculates the difference (L − L o ) with
The signal is converted into a control valve control signal (ET-signal) and sent to the control valve drive unit 27. When L −Lo is negative,
The adjustment valve is narrowed down.
他の実施例として、機械油圧式ガバナ(Ml−IG)に
おける主蒸気圧力低下防止装置について説明する。As another example, a main steam pressure drop prevention device in a mechanical hydraulic governor (Ml-IG) will be described.
機械油圧式ガバナでは目標負荷設定器までの信号処理方
法は、前述した電気油圧式ガバナと同一である。機械油
圧式ガバナにおける主蒸気圧力低下防止装置を示す第1
1図において、主蒸気止め弁の上流側圧力を測定する圧
力検出器28からのt蒸気圧力骨分と、主蒸気圧力低下
防止装置を構成するベローの中間に主蒸気圧力信号処理
演算器29を設ける。主蒸気圧力信号処理演算器とベロ
−の間には、電空変換器30を設ける。In the mechanical hydraulic governor, the signal processing method up to the target load setter is the same as that of the electrohydraulic governor described above. The first diagram shows the main steam pressure drop prevention device in a mechanical hydraulic governor.
In Figure 1, a main steam pressure signal processing calculator 29 is installed between the steam pressure component from the pressure detector 28 that measures the upstream pressure of the main steam stop valve and the bellows that constitutes the main steam pressure drop prevention device. establish. An electro-pneumatic converter 30 is provided between the main steam pressure signal processing calculator and the bellows.
主蒸気圧力信号処理演算器内の信号処理方法を示す第1
1図の信号処理ブロック線図において、主蒸気圧力検出
器から得られた実圧力Pは、設定負荷Lsから算出され
た加減弁絞り込み開始圧力pooと比較され、設定圧力
Psの90%以下において、加減弁の絞り込みを開始し
、負荷信号の設定圧力の90%点(第8図中座標(L
s 、 Poo))と無負荷において設定圧力の80%
点(第8図中座標(0,P2O) )を結ぶ直線上を動
くように、目標負荷設定器から目標負荷信号が出力され
る。Part 1 showing the signal processing method in the main steam pressure signal processing calculator
In the signal processing block diagram of FIG. 1, the actual pressure P obtained from the main steam pressure detector is compared with the regulating valve throttling start pressure poo calculated from the set load Ls, and at 90% or less of the set pressure Ps, Start narrowing down the control valve and set the 90% point of the set pressure of the load signal (coordinates (L) in Figure 8).
s, Poo)) and 80% of the set pressure at no load
A target load signal is output from the target load setting device so as to move on a straight line connecting the points (coordinates (0, P2O) in FIG. 8).
ここまでの過程は前述した電気油圧式ガバナの場合と同
じである。The process up to this point is the same as in the case of the electrohydraulic governor described above.
次に、目標負荷はベロー動作信号発生器において、設定
負荷Psとの比に対するベロー動作信号に変換される。Next, the target load is converted in a bellows operation signal generator into a bellows operation signal for the ratio to the set load Ps.
ベロー動作信号は第10図に示した電空変換器30で空
・気圧力に変換されベローに入る。The bellows operation signal is converted into air/pneumatic pressure by an electro-pneumatic converter 30 shown in FIG. 10, and then enters the bellows.
ベローは、内蔵されたバネとの釣合いによりベロー動作
信号に応じて、乙ンロードピストンを動作させる。ベロ
ーに内蔵されたバネの取付荷重に見合う分の信号として
、L / L o = Oにおいて、ベロー動作信号に
ある一定値aを出力させる様にする。The bellows actuate the load piston in response to the bellows operation signal in balance with a built-in spring. A certain constant value a is outputted as a bellows operation signal at L/Lo=O as a signal commensurate with the mounting load of the spring built into the bellows.
ベローの動きは、アンロードピストンを介し、スピード
リレーからタービンの加減弁を動作させるサーボモータ
パイロットピストンに通じるロッドの途中に設けられた
回転レバーに連結され、加減弁を駆動させる。The movement of the bellows is connected via an unloading piston to a rotary lever provided in the middle of a rod leading from the speed relay to a servo motor pilot piston that operates the regulator valve of the turbine, thereby driving the regulator valve.
本発明の適用により、従来は変圧過程中に主蒸気圧力低
下防止装置を除外していた為、変圧過程におけるボイラ
異常による水発生等からタービン保護ができなかったが
、変圧プラントの全ての運転領域において、主蒸気圧力
低下防止装置を動作させ、主機保護を行なう事ができる
。By applying the present invention, the main steam pressure drop prevention device was excluded during the pressure transformation process, which made it impossible to protect the turbine from water generation due to boiler abnormalities during the pressure transformation process, but now it can be used in all operating areas of the transformation plant. , the main steam pressure drop prevention device can be operated to protect the main engine.
第1図は、従来のプラント系統図、第2図は変圧プラン
トの負荷対蒸気圧力の関係線図、第3図゛は変圧プラン
トの弁開度対負荷、蒸気圧力の関係線図、第4図は変圧
プラントの起動パターン説明図、第5図は機械油圧式ガ
バナにおける主蒸気圧力低下防止装置機構説明図、第6
図は機械油圧式ガバナにおける主蒸気圧力低下防止装置
動作説明図、第7図は本発明の一実施例の電気油圧式ガ
Aすにおける信号処理ブロック図、第8.第9図は信号
処理説明図、第10図は機械油圧式ガAナシSおける、
主蒸気圧力低下防止装置の系統図、第11図は機械油圧
式ガバナにおける信号処理ブロック図である。
25・・・負荷設定器、26・・・PI演算器、27・
・・加減弁駆動部、29・・・信号処理演算器、30・
・・電空変換器。
代理人 弁理士 高橋明夫
躬1霞
第2図
抽30
□斗間度−
纂ば
蓮
几一時間
妬6霞
駿 イ吋
晃80
φ 荷 L
躬 9 m
Q +00c%)
@ 荷Figure 1 is a conventional plant system diagram, Figure 2 is a diagram of the relationship between load and steam pressure in a transformer pressure plant, Figure 3 is a diagram of the relationship between valve opening and load and steam pressure in a transformer pressure plant, and Figure 4 is a diagram of the relationship between load and steam pressure in a transformer plant. The figure is an explanatory diagram of the startup pattern of a transformer plant, Figure 5 is an explanatory diagram of the main steam pressure drop prevention device mechanism in a mechanical hydraulic governor, and Figure 6 is an explanatory diagram of the main steam pressure drop prevention device mechanism in a mechanical hydraulic governor.
8 is an explanatory diagram of the operation of the main steam pressure drop prevention device in a mechanical-hydraulic governor, FIG. 7 is a signal processing block diagram in an electro-hydraulic governor according to an embodiment of the present invention, and FIG. Fig. 9 is an explanatory diagram of signal processing, and Fig. 10 is a diagram showing the mechanical/hydraulic type control A/S.
A system diagram of the main steam pressure drop prevention device, FIG. 11 is a signal processing block diagram in the mechanical hydraulic governor. 25... Load setting device, 26... PI calculator, 27.
...Adjustment valve drive unit, 29...Signal processing calculator, 30.
...Electro-pneumatic converter. Agent Patent Attorney Akio Takahashi 1 Kasumi 2nd drawing 30 □ Toma degree - In short, Ren 几 1 hour envy 6 Kasumi Shun ii 80 φ load L 躬 9 m Q +00c%) @ load
Claims (1)
蒸気圧力信号と負荷信号とを設定値と比較する事により
、全ての主蒸気圧力範囲にわたり、蒸気加減弁の絞り込
みが可能なことを特徴とする主蒸気圧力低下防止装置。1. The steam turbine main steam pressure drop prevention device is characterized in that it is possible to narrow down the steam control valve over the entire main steam pressure range by comparing the main steam pressure signal and the load signal with a set value. Main steam pressure drop prevention device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8830084A JPS60233302A (en) | 1984-05-04 | 1984-05-04 | Main steam pressure drop prevention device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8830084A JPS60233302A (en) | 1984-05-04 | 1984-05-04 | Main steam pressure drop prevention device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS60233302A true JPS60233302A (en) | 1985-11-20 |
Family
ID=13939072
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8830084A Pending JPS60233302A (en) | 1984-05-04 | 1984-05-04 | Main steam pressure drop prevention device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60233302A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05296002A (en) * | 1992-04-20 | 1993-11-09 | Toshiba Corp | Steam turbine protector |
-
1984
- 1984-05-04 JP JP8830084A patent/JPS60233302A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05296002A (en) * | 1992-04-20 | 1993-11-09 | Toshiba Corp | Steam turbine protector |
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