JPH0692807B2 - Moisture separation heating system - Google Patents

Moisture separation heating system

Info

Publication number
JPH0692807B2
JPH0692807B2 JP61203746A JP20374686A JPH0692807B2 JP H0692807 B2 JPH0692807 B2 JP H0692807B2 JP 61203746 A JP61203746 A JP 61203746A JP 20374686 A JP20374686 A JP 20374686A JP H0692807 B2 JPH0692807 B2 JP H0692807B2
Authority
JP
Japan
Prior art keywords
steam
valve
turbine
heater
pipe
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 - Lifetime
Application number
JP61203746A
Other languages
Japanese (ja)
Other versions
JPS6361804A (en
Inventor
清純 伊藤
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP61203746A priority Critical patent/JPH0692807B2/en
Publication of JPS6361804A publication Critical patent/JPS6361804A/en
Publication of JPH0692807B2 publication Critical patent/JPH0692807B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、起動時における発電プラントの湿分分離加熱
系統に係り、経済性及び信頼性を向上せしめるように改
良した湿分分離加熱器系統に関するものである。
Description: TECHNICAL FIELD The present invention relates to a moisture separation heating system of a power plant at startup, and a moisture separation heater system improved so as to improve economic efficiency and reliability. It is about.

〔従来の技術〕[Conventional technology]

湿分分離加熱器に関して本発明に最も近い最新の公知技
術として特許公報昭55−38563号がある。
As the latest known technology closest to the present invention with respect to the moisture separation heater, there is Japanese Patent Publication No. 55-38563.

上記の公知技術においては、高圧タービンの抽気蒸気を
熱源として1次加熱器により該高圧タービンの排気を加
熱する構成であるが、この公知技術においてはタービン
の起動に先立つて1次加熱器を暖機(機器を稼動せしめ
る前に該機器を昇温させて、起動時に発生する熱応力・
熱歪を軽減する操作をいう)する為の格別な構成は考慮
されていない。
In the above-mentioned known technology, the exhaust gas of the high-pressure turbine is used as a heat source to heat the exhaust gas of the high-pressure turbine by the primary heater. However, in this known technology, the primary heater is warmed before starting the turbine. Machine (heat the equipment before operating it, and
It does not take into consideration a special configuration for reducing the thermal strain).

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

第2図は従来の湿分分離加熱系統の概要的な系統図であ
る。
FIG. 2 is a schematic system diagram of a conventional moisture separation heating system.

湿分分離加熱器3の1次加熱器4用の加熱蒸気は、高圧
タービン2の抽気蒸気を1次加熱蒸気管8によつて供給
されている。
As the heating steam for the primary heater 4 of the moisture separator / heater 3, the extracted steam of the high-pressure turbine 2 is supplied through the primary heating steam pipe 8.

また、2次加熱器5用の加熱蒸気は、蒸気発生器1から
発生した主蒸気1aを2次加熱蒸気管9によつて供給され
ている。
The heating steam for the secondary heater 5 is the main steam 1 a generated from the steam generator 1 supplied through the secondary heating steam pipe 9.

上述の1次加熱器4,2次加熱器5に対する初期の加熱蒸
気通気は次のように行なわれる。(第3図参照)。2次
加熱器5へは、タービン併入前に、小容量調整弁10を微
開しながら主蒸気を供給することにより十分時間をかけ
て2次加熱器5及び、配管11の暖機を行なうことができ
る。タービン併入後は小容量調整弁10の開度は次第に上
昇し、所定の部分負荷運転に達すると大容量調整弁12に
切替える。
The initial heating steam aeration for the above-mentioned primary heater 4 and secondary heater 5 is performed as follows. (See Figure 3). Before the turbine is installed in the secondary heater 5, main steam is supplied while the small capacity control valve 10 is slightly opened to warm up the secondary heater 5 and the pipe 11 for a sufficient time. be able to. After the turbine is installed, the opening of the small capacity control valve 10 gradually increases, and when it reaches a predetermined partial load operation, it is switched to the large capacity control valve 12.

1次加熱器4への加熱蒸気は、“タービン併入”の信号
により弁13を開し供給する。従つて1次加熱器4は暖機
無しで各タービン負荷条件での加熱蒸気を供給すること
になる。この場合、仮に弁13を絞り運転により暖機を行
なおうとすると2つの問題がある。1点は弁13が大口径
弁であり小流量の絞り運転が困難なことと、もう1点は
タービンの負荷上昇時間を大幅に遅らせることになりプ
ラント起動運転に大きな影響を受ける。特に、負荷追従
プラントにとつては、起動時間が延びることは重大な不
具合である。
The heating steam to the primary heater 4 is supplied by opening the valve 13 by the signal of "combination of turbine". Therefore, the primary heater 4 supplies heated steam under each turbine load condition without warming up. In this case, if the valve 13 is squeezed to warm up, there are two problems. The first point is that the valve 13 is a large-diameter valve and it is difficult to perform a throttle operation with a small flow rate, and the other point is that the load increase time of the turbine is significantly delayed, which greatly affects the plant start-up operation. Especially for a load following plant, extending the start-up time is a serious problem.

次に、1次加熱器4と2次加熱器5とにおける熱応力及
び熱歪を検討するための温度変化の情況を第4図につい
て説明する。
Next, the situation of temperature change for examining the thermal stress and thermal strain in the primary heater 4 and the secondary heater 5 will be described with reference to FIG.

第4図(B)は縦軸に温度をとり横軸に蒸気流れをとつ
た図表であり、第4図(A)は上記図表に示した温度符
号の測定点の説明図である。
FIG. 4 (B) is a chart in which temperature is plotted on the vertical axis and steam flow is plotted on the horizontal axis, and FIG. 4 (A) is an explanatory diagram of the measurement points of the temperature symbols shown in the chart.

各加熱器における加熱蒸気と暖機前の常温との温度差比
(ΔT1N/ΔT2N)は約0.85,被加熱蒸気と加熱蒸気温度
差比(ΔT1/ΔT2)は約0.7となり、いずれの場合も1
次加熱器と2次加熱器との間での温度差比はほぼ近い値
となり、2次加熱器5同様、1次加熱器4も暖機をする
必要性が高い。
The temperature difference ratio (ΔT 1N / ΔT 2N ) between the heated steam and the room temperature before warming up in each heater is about 0.85, and the temperature difference ratio between the heated steam and the heated steam (ΔT 1 / ΔT 2 ) is about 0.7. In case of
The temperature difference ratio between the secondary heater and the secondary heater is a value close to each other, and like the secondary heater 5, the primary heater 4 needs to be warmed up.

しかし従来の技術では上記の如く、系統構成上暖機が不
可能であつたため、1次加熱器4の暖機を行つていなか
つた。このため湿分分離加熱系統の各構成機器に熱応
力,熱歪の発生を招き(特に起動時)該部の耐久性に悪
影響を及ぼしていた。
However, in the conventional technique, the warm-up of the primary heater 4 was not performed because the warm-up was impossible due to the system configuration as described above. For this reason, thermal stress and thermal strain are generated in each component of the moisture separation and heating system (especially at startup), which adversely affects the durability of the part.

本発明は上述の事情に鑑みて為されたもので、起動時の
み該起動所要時間を延長することなく、1次加熱器を充
分に暖機し得る湿分分離加熱系統を提供することを目的
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 moisture separation heating system capable of sufficiently warming up a primary heater without extending the required startup time only at startup. And

〔問題点を解決するための手段〕[Means for solving problems]

上記の目的を達成するため、本発明の湿分分離加熱系統
は、蒸気源と、上記の蒸気源から主蒸気管を介して供給
される主蒸気によつて駆動される高圧タービンと、該高
圧タービンの抽気蒸気を熱源として該高圧タービンの排
気を加熱する1次加熱器と、該高圧タービンの入口蒸気
の一部を熱源として該高圧タービンの排気を加熱する2
次加熱器と、前記1次加熱器、2次加熱器に熱源用蒸気
を供給する配管および弁、並びに制御装置とを備えた湿
分分離加熱系統において、前記主蒸気管と、1次加熱器
用の熱源蒸気供給配管とを連絡する管路を設けるととも
に、上記管路に弁を介装接続し、かつ前記の管路に介装
接続した弁は、タービンの起動操作制御信号を入力され
て開閉制御を行う制御装置を備え、起動時のみ主蒸気の
1部を1次加熱器に供給し得るようにしたことを特徴と
する。
In order to achieve the above object, the moisture separation heating system of the present invention comprises a steam source, a high pressure turbine driven by main steam supplied from the steam source through a main steam pipe, and the high pressure turbine. A primary heater that heats the exhaust gas of the high-pressure turbine by using the extracted steam of the turbine as a heat source, and a exhaust gas of the high-pressure turbine that heats part of the inlet steam of the high-pressure turbine as a heat source 2
In a moisture separation heating system including a secondary heater, a pipe and a valve for supplying heat source steam to the primary heater, the secondary heater, and a control device, the main steam pipe and the primary heater The pipe connected to the heat source steam supply pipe is connected to the pipe, and the valve connected to the pipe is opened / closed by receiving a turbine start operation control signal. It is characterized in that a control device for controlling is provided, and a part of the main steam can be supplied to the primary heater only at the time of starting.

〔作用〕[Action]

上記の構成によれば、主蒸気の1部を弁によつて流量制
御しつつ1次加熱器に流して暖機することができる。し
かも、この暖機操作はタービン併入前において充分の時
間的余裕をもつて行い得るので、起動時における熱応
力,熱歪の防止効果が著しい。
According to the above configuration, part of the main steam can be warmed up by flowing through the primary heater while controlling the flow rate with the valve. In addition, since this warm-up operation can be performed with a sufficient time margin before the turbine is combined, the effect of preventing thermal stress and thermal strain at the time of starting is remarkable.

〔実施例〕〔Example〕

第1図は本発明の1実施例における湿分分離加熱系統を
示す。この実施例は第3図に示した従来例に本発明を適
用して改良したものであつて、従来の湿分分離加熱系と
異なるところは、湿分分離加熱器の1次加熱器4の1次
加熱蒸気管8と2次加熱器5の2次加熱蒸気管9とを連
絡する暖機管14と暖機弁15とを設け、タービン併入前に
2次加熱器と一緒に2次加熱器も暖機を完了させ得べく
為したことである。
FIG. 1 shows a moisture separation heating system in one embodiment of the present invention. This embodiment is an improvement of the conventional example shown in FIG. 3 by applying the present invention. The difference from the conventional moisture separation heating system is that of the primary heater 4 of the moisture separation heater. A warm-up pipe 14 and a warm-up valve 15 which connect the primary heating steam pipe 8 and the secondary heating steam pipe 9 of the secondary heater 5 are provided, and the secondary heating device is connected to the secondary heating device before the turbine is installed. The heater was also done in order to complete warming up.

このように構成された1次加熱器4は以下の様に暖機さ
れる。
The primary heater 4 thus configured is warmed up as follows.

2次加熱器5のタービン併入前暖機を、小容量調整弁10
を微開して主蒸気を通気することにより行なう。一方、
1次加熱器の暖機は本発明を適用して設けた小口径の暖
機弁15を小容量調整弁10の開信号(主蒸気圧力規定圧力
等)と同一信号でインターロツクにより開弁して主蒸気
を供給することにより行なう。暖機蒸気の流量,圧力,
温度は夫々の計器16,17,18によつて監視する。暖機後の
ドレンはドレンタンク19及びドレン弁20を介して復水器
に回収する。
Before warming up the secondary heater 5 with the turbine, the small capacity control valve 10
By slightly opening and ventilating the main steam. on the other hand,
For warm-up of the primary heater, the small-diameter warm-up valve 15 provided by applying the present invention is opened by the interlock with the same signal as the open signal (main steam pressure specified pressure, etc.) of the small capacity control valve 10. By supplying main steam. Warm steam flow rate, pressure,
The temperature is monitored by respective instruments 16,17,18. The drain after warming up is collected in the condenser via the drain tank 19 and the drain valve 20.

以上の操作を行うと、タービン併入時期には1次加熱器
4の暖機は終了しているため、“タービン併入”の信号
により暖機弁15をインターロツクにて開弁する。
When the above operation is performed, since the warm-up of the primary heater 4 is completed at the turbine adjoining time, the warm-up valve 15 is opened by the interlock in response to the "turbine adjoining" signal.

1次加熱器4の加熱蒸気入口の弁13は、従来例(第3
図)にも本実施例(第1図)にも設けられている。
The valve 13 at the heating steam inlet of the primary heater 4 is a conventional example (third
(Fig.) And this embodiment (Fig. 1).

従来例においては、この弁13は「タービン併入」の信号
に基づきインターロツクによつて開弁していたが、本実
施例では「タービン併入」前においても「暖機弁15閉」
信号とAND条件にてインターロツクにて開弁するように
構成する。このインターロツクのAND条件を設けること
により、暖機用主蒸気の高圧タービン2への逆流防止が
図られる。
In the conventional example, this valve 13 was opened by the interlock based on the signal of "combining turbines", but in this embodiment, "warm-up valve 15 closed" even before "combining turbines".
It is configured so that the valve is opened by the interlock according to the AND condition with the signal. By providing the AND condition of this interlock, it is possible to prevent the backflow of the main steam for warm-up to the high-pressure turbine 2.

第5図は前述の各弁の開閉状態を示す図表である。FIG. 5 is a chart showing the open / closed state of each valve described above.

第6図は本発明の他の実施例を示す。第1図の実施例と
異なる点は、前例における暖機弁15を調整弁21とし、小
容量調整弁10の上流側から主蒸気を供給し、圧力制御装
置22によつて調整弁21を制御する構成である。
FIG. 6 shows another embodiment of the present invention. The difference from the embodiment of FIG. 1 is that the warm-up valve 15 in the previous example is a regulating valve 21, main steam is supplied from the upstream side of the small capacity regulating valve 10, and the regulating valve 21 is controlled by a pressure control device 22. This is the configuration.

〔発明の効果〕〔The invention's effect〕

本発明によれば起動時のみ湿分分離加熱器の1次加熱器
をタービン併入前に十分に暖機出来るため、 (i)1次加熱器の熱応力の問題を解決し、クラツク等
の事故防止を図り信頼性が向上する。
According to the present invention, since the primary heater of the moisture separation heater can be sufficiently warmed up before the turbine is incorporated only at the time of start-up, (i) the problem of thermal stress of the primary heater can be solved, and cracks such as cracks Prevent accidents and improve reliability.

(ii)負荷運転段階での1次加熱器への急激な加熱蒸気
供給が可能となり、起動時のみ起動時間の短縮が必須条
件となる急速起動停止プラントにとつてきわめて有効で
ある。
(Ii) Rapid heating steam can be supplied to the primary heater in the load operation stage, which is extremely effective for a quick start-stop plant in which shortening the start-up time is an essential condition only at start-up.

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

第1図は本発明の1実施例の系統図、第2図及び第3図
は従来の湿分分離加熱系統の説明図、第4図は本発明の
背景となる温度分布の説明図表、第5図は本発明の実施
例における弁開閉手順とタービン負荷との説明図表、第
6図は本発明の他の実施例における系統図である。 2…高圧タービン、4…1次加熱器、5…2次加熱器、
8…1次加熱蒸気管、9…2次加熱蒸気管、10…小容量
調整弁、11…配管、13…弁、14…暖機管、15…暖機弁、
21…調整弁、22…圧力制御装置。
FIG. 1 is a system diagram of one embodiment of the present invention, FIGS. 2 and 3 are explanatory diagrams of a conventional moisture separation heating system, and FIG. 4 is an explanatory diagram of temperature distribution which is the background of the present invention. FIG. 5 is an explanatory diagram of a valve opening / closing procedure and a turbine load in the embodiment of the present invention, and FIG. 6 is a system diagram in another embodiment of the present invention. 2 ... High-pressure turbine, 4 ... Primary heater, 5 ... Secondary heater,
8 ... Primary heating steam pipe, 9 ... Secondary heating steam pipe, 10 ... Small capacity adjusting valve, 11 ... Piping, 13 ... Valve, 14 ... Warming pipe, 15 ... Warming valve,
21 ... Regulator valve, 22 ... Pressure control device.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】蒸気源と、上記の蒸気源から主蒸気管を介
して供給される主蒸気によって駆動される高圧タービン
と、該高圧タービンの抽気蒸気を熱源として該高圧ター
ビンの排気を加熱する1次加熱器と、該高圧タービンの
入口蒸気の一部を熱源として該高圧タービンの排気を加
熱する2次加熱器と、前記1次加熱器、2次加熱器に熱
源用蒸気を供給する配管および弁とを備えた湿分分離器
加熱系統において、前記主蒸気管と、1次加熱器用の熱
源蒸気供給配管とを連絡する管路を設けるとともに、上
記管路に弁を介装接続し、かつ前記の管路に介装接続し
た弁は、タービンの起動時該タービンの起動操作制御信
号開閉制御を行う制御装置を備え、起動時のみ主蒸気の
1部を1次加熱器に供給し得るようにしたことを特徴と
する湿分分離加熱系統。
1. A steam source, a high-pressure turbine driven by main steam supplied from the steam source through a main steam pipe, and bleeding steam of the high-pressure turbine as a heat source for heating exhaust gas of the high-pressure turbine. A primary heater, a secondary heater that heats exhaust gas of the high-pressure turbine by using a part of inlet steam of the high-pressure turbine as a heat source, and a pipe that supplies heat source steam to the primary heater and the secondary heater In a moisture separator heating system including a valve and a valve, a pipe line that connects the main steam pipe and the heat source steam supply pipe for the primary heater is provided, and a valve is connected to the pipe line. Further, the valve connected to the above-mentioned pipeline is equipped with a control device for performing opening / closing control signal for opening / closing the turbine when the turbine is started, and a part of main steam can be supplied to the primary heater only when the turbine is started. Moisture separation heating characterized by Integration.
JP61203746A 1986-09-01 1986-09-01 Moisture separation heating system Expired - Lifetime JPH0692807B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61203746A JPH0692807B2 (en) 1986-09-01 1986-09-01 Moisture separation heating system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61203746A JPH0692807B2 (en) 1986-09-01 1986-09-01 Moisture separation heating system

Publications (2)

Publication Number Publication Date
JPS6361804A JPS6361804A (en) 1988-03-18
JPH0692807B2 true JPH0692807B2 (en) 1994-11-16

Family

ID=16479160

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61203746A Expired - Lifetime JPH0692807B2 (en) 1986-09-01 1986-09-01 Moisture separation heating system

Country Status (1)

Country Link
JP (1) JPH0692807B2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5646041A (en) * 1979-09-21 1981-04-27 Hokuetsu Kogyo Co Drain cleaning apparatus

Also Published As

Publication number Publication date
JPS6361804A (en) 1988-03-18

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