JPH01300003A - Control device of degree of vacuum in condenser - Google Patents
Control device of degree of vacuum in condenserInfo
- Publication number
- JPH01300003A JPH01300003A JP12505888A JP12505888A JPH01300003A JP H01300003 A JPH01300003 A JP H01300003A JP 12505888 A JP12505888 A JP 12505888A JP 12505888 A JP12505888 A JP 12505888A JP H01300003 A JPH01300003 A JP H01300003A
- Authority
- JP
- Japan
- Prior art keywords
- steam
- condenser
- vacuum
- degree
- inlet valve
- 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
Landscapes
- Control Of Turbines (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の目的〕
(産業上の利用分野)
本発明は、蒸気タービン発電機設備の復水器の空気抽出
系統に係り、蒸気噴射式空気抽出器の吸込性能を可変と
し、復水器の真空度を制御する復水器真空度制御装置に
関する。[Detailed Description of the Invention] [Object of the Invention] (Industrial Application Field) The present invention relates to an air extraction system of a condenser of a steam turbine generator equipment, and relates to an air extraction system for a condenser of a steam turbine generator equipment, in which the suction performance of a steam injection air extractor is variable. The present invention relates to a condenser vacuum level control device that controls the vacuum level of a condenser.
(従来の技術)
従来の蒸気噴射式空気抽出器を具備した復水器抽出系統
は一般に第4図のように構成される。なお本図の蒸気噴
射式空気抽出器3は2連2段のものを示す。蒸気弁8a
、 8b、 9a、 9b、駆動蒸気入口弁6は手動も
しくは電動駆動の止め弁であるのが通例である。蒸気タ
ービン1の排気は、復水器2で凝縮される。蒸気タービ
ン1の排気中に存在していた不凝縮ガス及び蒸気タービ
ンサイクルが運転中に大気圧力以下になる機器及び配管
から漏れ込む空気は、空気管4を介して蒸気噴射式空気
抽出器3で大気中に排出される。駆動蒸気ライン20に
配設された駆動蒸気圧力制御弁5は、2次圧力を例えば
14atgとなるように一定制御されている。(Prior Art) A conventional condenser extraction system equipped with a steam injection type air extractor is generally constructed as shown in FIG. Note that the steam injection type air extractor 3 shown in this figure is a two-stage, two-stage type. steam valve 8a
, 8b, 9a, 9b, the actuated steam inlet valve 6 is typically a manually or electrically actuated stop valve. The exhaust gas of the steam turbine 1 is condensed in a condenser 2. The non-condensable gas present in the exhaust gas of the steam turbine 1 and the air leaking from equipment and piping whose pressure drops below atmospheric pressure during operation of the steam turbine cycle are removed by the steam injection air extractor 3 via the air pipe 4. Emitted into the atmosphere. The drive steam pressure control valve 5 disposed in the drive steam line 20 is constantly controlled to maintain a secondary pressure of, for example, 14 atg.
蒸気噴射式空気抽出器3の吸込性能は、駆動蒸気入口弁
6前の蒸気圧力及び蒸気量が一定のため固定されており
、駆動蒸気入口弁6を操作して復水器の真空度を制御す
ることは、なされていない。The suction performance of the steam injection air extractor 3 is fixed because the steam pressure and steam amount in front of the drive steam inlet valve 6 are constant, and the degree of vacuum of the condenser is controlled by operating the drive steam inlet valve 6. What is to be done is not done.
(発明が解決しようとする課m)
近時、発電設備とりわけ火力発電設備は、負荷調整運転
が余儀なくされている。負荷調整運転の場合、タービン
排気量が変化することになるが、従来は、前記したよう
に、蒸気噴射式空気抽出器の吸込性能が一定のため、復
水器の真空度は、タービン排気量と復水器冷却水温度・
冷却水量から定まる復水器性能と蒸気噴射式空気抽出器
の性能から定まる値となる。(Problem to be solved by the invention) Recently, power generation equipment, especially thermal power generation equipment, has been forced to perform load adjustment operation. In the case of load adjustment operation, the turbine displacement changes, but conventionally, as mentioned above, the suction performance of the steam injection air extractor is constant, so the degree of vacuum in the condenser depends on the turbine displacement. and condenser cooling water temperature/
The value is determined from the condenser performance determined by the amount of cooling water and the performance of the steam injection air extractor.
第2図は、タービン排気量と効率的真空度の相関関係の
一例を示す図である0図示するように、タービン効率を
最高効率とするためには、タービン排気量に見合った復
水器の真空度に調整する必要がある。ところが、従来は
必ずしもタービン効率が最高効率となる条件の復水器真
空度のもとでは運転されていなかった。Figure 2 is a diagram showing an example of the correlation between the turbine displacement and the effective degree of vacuum. It is necessary to adjust the vacuum level. However, in the past, turbines were not necessarily operated under the conditions of condenser vacuum that would result in the highest turbine efficiency.
本発明は、上記の従来技術の問題点を改善し。The present invention improves the problems of the prior art described above.
熱効率が改善される復水器真空度制御装置を提供するこ
とを目的とする。It is an object of the present invention to provide a condenser vacuum degree control device with improved thermal efficiency.
(課題を解決するための手段)
本発明に係る復水器真空度の制御方法は、復水器の真空
度をタービン排気量に見合った最適真空度に制御するた
めに、蒸気噴射式空気抽出器の駆動蒸気入口弁を調節弁
として、駆動蒸気圧力及び駆動蒸気量を変化させ蒸気噴
射式空気抽出器の吸込性能を可変とする。(Means for Solving the Problems) A method for controlling the degree of vacuum in a condenser according to the present invention is to control the degree of vacuum in the condenser to the optimum degree of vacuum corresponding to the turbine displacement. The suction performance of the steam injection type air extractor is made variable by using the drive steam inlet valve of the steam injection device as a control valve to change the drive steam pressure and drive steam amount.
第3図は、蒸気噴射式空気抽出器の駆動蒸気量の変化と
蒸気噴射式空気抽出器の吸込性能との相関関係の一例を
示した図である。FIG. 3 is a diagram showing an example of the correlation between a change in the amount of driving steam of the steam injection type air extractor and the suction performance of the steam injection type air extractor.
本発明の制御装置の場合、駆動蒸気入口弁を絞り込むこ
とにより、駆動蒸気量を減小させるとともに駆動蒸気圧
力を減少させることになる。図示するように、駆動蒸気
量が減少すると、蒸気噴射式空気抽出器の吸込空気量が
少なくなる。そこでこの特徴を有効利用しタービンの排
気量の変化に見合った復水器真空度となるように、蒸気
噴射式空気抽出器の吸込性能を可変とする。In the case of the control device of the present invention, by throttling the drive steam inlet valve, the drive steam amount is reduced and the drive steam pressure is reduced. As shown, as the amount of driving steam decreases, the amount of air sucked into the steam injection air extractor decreases. Therefore, by effectively utilizing this feature, the suction performance of the steam injection air extractor is made variable so that the degree of vacuum in the condenser matches changes in the displacement of the turbine.
(作 用)
上記構成の復水器真空度制御方法によれば1例えば負荷
調整運転時、部分負荷運転時、復水器冷却水温度が復水
器の設計点よりも低い時等の場合にもタービン効率が最
高効率となるよう復水器の真空度を制御することができ
、熱効率を改善させることができる。(Function) According to the condenser vacuum degree control method with the above configuration, 1. For example, during load adjustment operation, partial load operation, when the condenser cooling water temperature is lower than the design point of the condenser, etc. The degree of vacuum in the condenser can also be controlled so that the turbine efficiency is maximized, and thermal efficiency can be improved.
(実施例)
以下本発明の一実施例について図面を参照して説明する
。第1図は本発明に係る復水器真空度制御装置の一実施
例を示す系統制御方法を表す図である。なお第4図に示
す従来例と同一要素には同一符号を付して、その詳細説
明は省略する。(Example) An example of the present invention will be described below with reference to the drawings. FIG. 1 is a diagram showing a system control method showing an embodiment of the condenser vacuum level control device according to the present invention. Note that the same elements as those in the conventional example shown in FIG. 4 are given the same reference numerals, and detailed explanation thereof will be omitted.
発電機10の出力信号は、演算器11で、タービン排気
量を示す信号に変換される1次にタービン排気量を示す
信号は、演算器12で最適真空度を示す信号に変換され
る6次に最適真空度を示す信号は、加減器15にて復水
器2の真空度を検出するトランスミッタ13の信号と比
較される。加減器15にて得られた偏差信号は、コント
ローラ16で駆動蒸気入口弁6の弁開度設定信号に変換
され、駆動蒸気入口弁6が制御される。なお本実施例で
はタービンの排気量を算出するために発電機出力信号を
用いているが、他に図示しない復水流量信号等タービン
排気量に容易に変換できる信号も利用することが可能で
ある。The output signal of the generator 10 is converted into a signal indicating the turbine displacement by a computing unit 11. The primary signal indicating the turbine displacement is converted into a signal indicating the optimum degree of vacuum by the computing unit 12. The signal indicating the optimum degree of vacuum is compared with the signal from the transmitter 13 which detects the degree of vacuum in the condenser 2 at the adjuster 15. The deviation signal obtained by the adjuster 15 is converted into a valve opening degree setting signal for the drive steam inlet valve 6 by the controller 16, and the drive steam inlet valve 6 is controlled. In this embodiment, the generator output signal is used to calculate the turbine displacement, but it is also possible to use other signals that can be easily converted into the turbine displacement, such as a condensate flow rate signal (not shown). .
第1図は本発明に係る復水器真空度制御装置の一実施例
を示す系統図、第2図はタービン排気量と効率的真空度
の相関関係の一例を示す図、第3図は蒸気噴射式゛空気
抽出器の駆動蒸気量の変化と蒸気噴射式空気抽出器の吸
込性能との相関関係の一例を示す図、第4図は従来の蒸
気噴射式空気抽出器を具備した復水器真空度制御装置を
示す系統図である。
1・・・蒸気タービン 2・・・復水器3・・・蒸気
噴射式空気抽出器
4・・・空気管 5・・・駆動蒸気圧力制御弁
6・・・駆動蒸気入口弁 7a・・・抽出空気入口弁7
b・・・抽出空気入口弁 8a 、 8b・・・第1段
蒸気弁’Ja 、 9b・・・第2段蒸気弁
10・・・発電機 11・・・演算器12・・
・演算器 13・・・圧カドランスミッタ14
・・・圧カドランスミッタ
15・・・加減器 16・・・コントローラ2
0・・・駆動蒸気ライン
代理人 弁理士 則 近 憲 佑
同 第子丸 健
第1図
復水器真茎戻 高
第2図
第3図
第4図Fig. 1 is a system diagram showing an embodiment of the condenser vacuum degree control device according to the present invention, Fig. 2 is a diagram showing an example of the correlation between turbine displacement and efficient vacuum degree, and Fig. 3 is a diagram showing an example of the correlation between the turbine displacement and the effective degree of vacuum. A diagram showing an example of the correlation between changes in the driving steam amount of an injection type air extractor and the suction performance of the steam injection type air extractor. Figure 4 shows a condenser equipped with a conventional steam injection type air extractor. FIG. 2 is a system diagram showing a vacuum degree control device. 1...Steam turbine 2...Condenser 3...Steam injection air extractor 4...Air pipe 5...Drive steam pressure control valve 6...Drive steam inlet valve 7a... Extraction air inlet valve 7
b... Extraction air inlet valve 8a, 8b... First stage steam valve 'Ja, 9b... Second stage steam valve 10... Generator 11... Arithmetic unit 12...
・Arithmetic unit 13... Pressure quadrature transmitter 14
...Pressure transmitter 15...Adjuster 16...Controller 2
0... Drive steam line agent Patent attorney Nori Ken Chika Yudo Daishimaru Ken Figure 1 Condenser Maki Return High Figure 2 Figure 3 Figure 4
Claims (1)
、この復水器の空気を排出するための蒸気噴射式の空気
抽出器と、この空気抽出器にこれを駆動するための高圧
蒸気を供給する駆動蒸気ラインと、この駆動蒸気ライン
に配設された駆動蒸気入口弁とを具備する復水器真空度
制御装置において、上記蒸気タービンから復水器への排
出蒸気量相当量を測定する手段と、この排出蒸気量相当
量に対応する最適駆動蒸気量を算出する手段と、この最
適駆動蒸気量を空気抽出器に供給するように駆動蒸気入
口弁を制御する手段とを具備することを特徴とする復水
器真空度制御装置。A condenser that condenses steam discharged from a steam turbine, a steam injection air extractor that discharges air from this condenser, and high-pressure steam that drives this air extractor. In a condenser vacuum degree control device that includes a supply drive steam line and a drive steam inlet valve disposed on the drive steam line, an amount equivalent to the amount of exhaust steam discharged from the steam turbine to the condenser is measured. means for calculating an optimum amount of driving steam corresponding to the equivalent amount of exhaust steam; and means for controlling a driving steam inlet valve to supply the optimum amount of driving steam to the air extractor. Features a condenser vacuum control device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12505888A JPH01300003A (en) | 1988-05-24 | 1988-05-24 | Control device of degree of vacuum in condenser |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12505888A JPH01300003A (en) | 1988-05-24 | 1988-05-24 | Control device of degree of vacuum in condenser |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH01300003A true JPH01300003A (en) | 1989-12-04 |
Family
ID=14900779
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12505888A Pending JPH01300003A (en) | 1988-05-24 | 1988-05-24 | Control device of degree of vacuum in condenser |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01300003A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10280910A (en) * | 1997-04-07 | 1998-10-20 | Hitachi Zosen Corp | Steam turbine equipment |
-
1988
- 1988-05-24 JP JP12505888A patent/JPH01300003A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10280910A (en) * | 1997-04-07 | 1998-10-20 | Hitachi Zosen Corp | Steam turbine equipment |
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