JPS59221503A - Reheater for turbine power device - Google Patents

Reheater for turbine power device

Info

Publication number
JPS59221503A
JPS59221503A JP9562283A JP9562283A JPS59221503A JP S59221503 A JPS59221503 A JP S59221503A JP 9562283 A JP9562283 A JP 9562283A JP 9562283 A JP9562283 A JP 9562283A JP S59221503 A JPS59221503 A JP S59221503A
Authority
JP
Japan
Prior art keywords
reheater
steam
turbine
line
temperature
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP9562283A
Other languages
Japanese (ja)
Inventor
直昭 柴下
初 鳥谷
伊佐 均
辻 邦雄
金子 了市
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 JP9562283A priority Critical patent/JPS59221503A/en
Publication of JPS59221503A publication Critical patent/JPS59221503A/en
Pending legal-status Critical Current

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  • Control Of Turbines (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

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動力発生サイクルに供給される蒸
気の一部を用いることに2って、サイクル蒸気を低圧で
再熱する蒸気タービン動力装置に係り、特に、起動時の
再熱器内における熱応力の軽減手段に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a steam turbine power plant that reheats cycle steam at low pressure by using a part of steam supplied to a steam turbine power generation cycle. In particular, the present invention relates to means for reducing thermal stress within the reheater during startup.

〔発明の背景〕[Background of the invention]

実質的に飽和した蒸気の供給によって動く蒸気タービン
動力装置、たとえば、沸騰水型又は加圧水型原子炉によ
って蒸気を供給される動力装置では、通常、湿分分離再
熱器を用いることによって蒸気から水分を除去し、かつ
、高圧タービンと低るいは、別の圧力容器内に配置でれ
てもよく、通常蒸気タービンの給入蒸気の一部を低圧、
低温サイクル蒸気を加熱するための流体として、一段取
上の再熱機能をもつ再熱器へ導入する。
In steam turbine power plants that operate on a substantially saturated supply of steam, such as power plants supplied with steam by boiling water or pressurized water nuclear reactors, moisture is typically removed from the steam by using a moisture separator reheater. and may be placed in a pressure vessel separate from the high-pressure turbine; typically a portion of the steam input to the steam turbine is removed from the high-pressure turbine.
As a fluid for heating low-temperature cycle steam, it is introduced into a reheater with an additional reheating function.

再熱器内の最高温度の再熱段では、高圧タービンへ供給
する蒸気源からの蒸気の一部を再熱用加熱流体として用
いるため、再熱器管束の「管側」温度は負荷と共に大き
く変化することはない。他方、再熱されるサイクル蒸気
の通過する[外殻ill温度は、サイクル蒸気が高圧タ
ービンで仕事を行なっているため、負荷と共に広範囲に
変化する。
In the reheat stage, which has the highest temperature in the reheater, part of the steam from the steam source that supplies the high-pressure turbine is used as the heating fluid for reheating, so the temperature on the "tube side" of the reheater tube bundle increases with the load. It never changes. On the other hand, the temperature through which the cycle steam to be reheated varies over a wide range with load, as the cycle steam is performing work in the high pressure turbine.

従って、起動時及び部分負荷時には外殻側と管側間にか
なりの温度差が生じるため、再熱器内各部で温度差によ
る熱応力が発生する。
Therefore, at startup and under partial load, a considerable temperature difference occurs between the outer shell side and the tube side, and thermal stress is generated at various parts within the reheater due to the temperature difference.

〔発明の目的〕[Purpose of the invention]

本発明の目的は、蒸気タービン起動時の再熱器谷部の温
度差によって生ずる再熱器内熱応力の軽減を行なうター
ビン動力装置用再熱器を提供するにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide a reheater for a turbine power unit that reduces thermal stress within the reheater caused by a temperature difference in the valley of the reheater when a steam turbine is started.

〔発明の概要〕[Summary of the invention]

本発明の要点は蒸気タービン起動前に、予め、再熱器全
体を同−加熱温朋で予熱してνき、起動時に発生する再
熱器内熱応力発生を極力低減させるにある。
The key point of the present invention is to preheat the entire reheater to the same heating temperature before starting the steam turbine to minimize the generation of thermal stress within the reheater that occurs during startup.

〔発明の実施例〕[Embodiments of the invention]

本発明の実施例を添付の図面によって詳述する。 Embodiments of the invention will be described in detail with reference to the accompanying drawings.

第1図において、蒸気タービン動力装置は高圧タービン
部1と低圧タービン部2および、気水分離器と再熱器を
兼ねた湿分分離再熱器4を備える。
In FIG. 1, the steam turbine power plant includes a high-pressure turbine section 1, a low-pressure turbine section 2, and a moisture separation reheater 4 that serves as a steam separator and a reheater.

実際には、いくつかの湿分分離再熱器を用いるが、図を
明瞭にするため、1個だけ示しである。主蒸気ライン5
よジ流入する蒸気は、高圧タービン1を通る間に膨張し
て湿度を増す。この湿度の高いサイクル蒸気は、ライン
6ft通ジ、湿分分離再熱器4の圧力外殻底部にある複
数の入口より湿分分離再熱器4に流入し、圧力外殻頂部
にある複数の出口から流出後、ライン9を通って低圧タ
ービン2に流入し、更に、ライン10より復水器3へ導
かれる。
In practice, several moisture separator reheaters are used, but only one is shown for clarity of illustration. Main steam line 5
The incoming steam expands and becomes more humid while passing through the high pressure turbine 1. This high-humidity cycle steam flows through a 6-ft line into the moisture separator reheater 4 through a plurality of inlets at the bottom of the pressure shell of the moisture separator reheater 4, and enters the moisture separator reheater 4 through a plurality of inlets at the top of the pressure shell. After flowing out from the outlet, it flows into the low pressure turbine 2 through line 9 and is further led to condenser 3 through line 10.

湿分分離再熱器4の内部には、湿分をサイクル蒸気から
除くための複数の湿分分離要素(図示せず)をもち、又
、高圧タービン1から抽気ライン8に導く蒸気でサイク
ル蒸気を再熱する第1段再熱器、及び、主蒸気ライン5
から分岐ライン7に導く蒸気でサイクル蒸気を再熱する
第2段再熱器(図示せず)を備えている。ここで、第2
再熱器ヘライン11よシ流入する蒸気は主蒸気ライン5
よシ導かれるため、そ9蒸気温度はタービンの運転条件
とは無関係にほぼ一定である。一方、第1再熱器へ導か
れ名蒸気及びサイクル蒸気は、高圧タービン1で仕事を
行なってくるため、タービンの運転条件と共に、蒸気温
度を変化させる。
The moisture separator reheater 4 has a plurality of moisture separation elements (not shown) for removing moisture from the cycle steam, and the moisture separation reheater 4 has a plurality of moisture separation elements (not shown) for removing moisture from the cycle steam. and the main steam line 5.
A second stage reheater (not shown) is provided for reheating the cycle steam with steam introduced from the steam line to the branch line 7. Here, the second
The steam flowing from the reheater line 11 flows into the main steam line 5.
Therefore, the steam temperature is approximately constant regardless of the operating conditions of the turbine. On the other hand, since the raw steam and cycle steam guided to the first reheater perform work in the high-pressure turbine 1, the steam temperature changes together with the operating conditions of the turbine.

本発明によれば、タービン通常運転ラインとは別に、主
蒸気ライン5よシ分岐したライン11及び12、更に湿
分分離再熱器4の出口と復水器を結ぶライン13を別途
設けておき、タービン起動に先立ち湿分分離再熱器4を
タービン系内蒸気最高温度である主蒸気ライン蒸気で暖
機できるようにする。
According to the present invention, lines 11 and 12 branched from the main steam line 5 and a line 13 connecting the outlet of the moisture separation reheater 4 and the condenser are separately provided in addition to the turbine normal operation line. , the moisture separator reheater 4 can be warmed up with main steam line steam, which is the highest steam temperature in the turbine system, prior to starting the turbine.

高圧タービン1、湿分分離再熱器4、低圧タービン2、
腹水器3間を結“ぶラインには、通常運転ライン部と湿
分分離再熱器暖機ライン部とを区切るために、それぞれ
のラインに仕切弁15,16゜17.18,20,22
.24を設ける。まず、湿分分離再熱器4の暖機に先立
ち、各仕切弁を閉じた後、湿分分離再熱器の暖機ライン
11,12゜13及び、第2段再熱器へ通ずるライン7
の仕切弁15,20,22.24を開く。その後、湿分
分離再熱器の暖機ライン11,12,13及び第2段再
熱器ライン7の流量制御弁19,21゜23で、徐々に
、湿分分離再熱器4へ主蒸気ライン蒸気を流入させ、湿
分分離再熱器を予熱する。
High pressure turbine 1, moisture separation reheater 4, low pressure turbine 2,
In the line connecting the ascites device 3, gate valves 15, 16, 17, 18, 20, 22 are installed in each line to separate the normal operation line and the moisture separation reheater warm-up line.
.. 24 will be provided. First, before warming up the moisture separator reheater 4, after closing each gate valve, the warm-up lines 11, 12, 13 of the moisture separator reheater and the line 7 leading to the second stage reheater are opened.
Open the gate valves 15, 20, 22, and 24. Thereafter, the main steam is gradually transferred to the moisture separator reheater 4 through the warm-up lines 11, 12, 13 of the moisture separator reheater and the flow control valves 19, 21° 23 of the second stage reheater line 7. Line steam is introduced to preheat the moisture separator reheater.

蒸気流入の際、ライン13における減圧弁25で減圧後
、復水器3へ導く。予熱後、タービン通常運転の前に、
暖機ライン7.11,12,13の仕切弁を閉じ、ター
ビン通常運転に入る。ここで、第2段再熱器ライン7は
、通常運転及び暖機時とも共用とする。又、暖機運転は
、高圧タービン部の暖機等で既存運転技術で行なってお
り、運転上特に問題はない。なお、図中14は仕切弁で
ある。
When steam is introduced, the pressure is reduced by the pressure reducing valve 25 in the line 13 and then the steam is introduced into the condenser 3. After preheating and before normal turbine operation,
The gate valves of warm-up lines 7.11, 12, and 13 are closed and the turbine enters normal operation. Here, the second stage reheater line 7 is shared during normal operation and during warm-up. In addition, the warm-up operation is performed using existing operating techniques such as warming up the high-pressure turbine section, and there are no particular operational problems. In addition, 14 in the figure is a gate valve.

第2図は、湿分分離再熱器4への初期蒸気流入時の各部
の温度を示す。
FIG. 2 shows the temperature of each part when steam initially flows into the moisture separation reheater 4.

すなわち、第2段再熱器温度101、第2段再熱器温度
102、サイクル蒸気温度103、湿分分離再熱器外殻
温度104及び105について、横軸に時間、縦軸に温
度を取って示す。本発明の暖機を行なわなかった場合の
外殻の温度は線104で示されておシ、湿分分離再熱器
4内最大温度部である第2段再熱器温度101との温度
差ΔTlで過大な熱応力が発生する。一方、本発明で示
す暖機を用φれば、外殻温度は線105で示すようにな
り、第2段再熱器温度101との温度差はΔT2となり
、熱応力が低減する。
That is, regarding the second stage reheater temperature 101, second stage reheater temperature 102, cycle steam temperature 103, and moisture separation reheater shell temperatures 104 and 105, the horizontal axis represents time and the vertical axis represents temperature. Shown. The temperature of the outer shell when the warm-up of the present invention is not performed is shown by a line 104, which is the temperature difference from the second stage reheater temperature 101, which is the maximum temperature part in the moisture separation reheater 4. Excessive thermal stress occurs at ΔTl. On the other hand, if the warm-up shown in the present invention is used, the outer shell temperature becomes as shown by the line 105, the temperature difference from the second stage reheater temperature 101 becomes ΔT2, and the thermal stress is reduced.

〔発明の効果〕〔Effect of the invention〕

本究明によ扛ば、タービン起動時に湿分分離再熱器内に
発生ずる過大な熱応力を回避でき、迅速、かつ、安全に
タービン起動を行なえる。
According to this research, it is possible to avoid excessive thermal stress generated in the moisture separator reheater when starting the turbine, and it is possible to start the turbine quickly and safely.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例の蒸気タービン動力装置の系
統図、g2図は湿分分離再熱器における各部温度と時間
を示すグラフである。
Fig. 1 is a system diagram of a steam turbine power plant according to an embodiment of the present invention, and Fig. g2 is a graph showing temperatures and times at various parts in a moisture separation reheater.

Claims (1)

【特許請求の範囲】[Claims] 1、管束内にある蒸気源からの蒸気を用いて、高圧ター
ビンからのサイクル蒸気を再熱するタービン動力装置用
再熱器において、前記再熱器のサイクル蒸気流入部及び
加熱用蒸気流入部と前記蒸気源を結ぶ前記高圧タービン
のノ(イノ(スライ、このバイパスラインに装着する仕
切弁及び流量制御弁、前記再熱器のサイクル蒸気流出部
と覆水器を結ぶ低圧夛−ビンバイパスライン、前記サイ
クル蒸気流出部と凝縮器を結ぶバイパスラインに設けた
仕切弁および減圧弁からなることを特徴とするタービン
動力装置用再熱器。
1. In a reheater for a turbine power unit that reheats cycle steam from a high-pressure turbine using steam from a steam source located within a tube bundle, a cycle steam inflow portion and a heating steam inflow portion of the reheater; A gate valve and a flow rate control valve are installed in the bypass line of the high-pressure turbine that connects the steam source, a low-pressure bin bypass line that connects the cycle steam outlet of the reheater and the water coverer, A reheater for a turbine power unit characterized by comprising a gate valve and a pressure reducing valve provided in a bypass line connecting a cycle steam outlet and a condenser.
JP9562283A 1983-06-01 1983-06-01 Reheater for turbine power device Pending JPS59221503A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9562283A JPS59221503A (en) 1983-06-01 1983-06-01 Reheater for turbine power device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9562283A JPS59221503A (en) 1983-06-01 1983-06-01 Reheater for turbine power device

Publications (1)

Publication Number Publication Date
JPS59221503A true JPS59221503A (en) 1984-12-13

Family

ID=14142629

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9562283A Pending JPS59221503A (en) 1983-06-01 1983-06-01 Reheater for turbine power device

Country Status (1)

Country Link
JP (1) JPS59221503A (en)

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