JP3335696B2 - Steam generator and method of operating the same - Google Patents

Steam generator and method of operating the same

Info

Publication number
JP3335696B2
JP3335696B2 JP03822793A JP3822793A JP3335696B2 JP 3335696 B2 JP3335696 B2 JP 3335696B2 JP 03822793 A JP03822793 A JP 03822793A JP 3822793 A JP3822793 A JP 3822793A JP 3335696 B2 JP3335696 B2 JP 3335696B2
Authority
JP
Japan
Prior art keywords
pressure
economizer
drum
valve
water
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
JP03822793A
Other languages
Japanese (ja)
Other versions
JPH06249405A (en
Inventor
利則 重中
展雄 下野
貢 武蔵
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.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi 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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP03822793A priority Critical patent/JP3335696B2/en
Publication of JPH06249405A publication Critical patent/JPH06249405A/en
Application granted granted Critical
Publication of JP3335696B2 publication Critical patent/JP3335696B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、排熱回収ボイラなどの
蒸気発生装置に係り、特に節炭器を有し、上記節炭器内
の流体圧力をその流体温度の飽和蒸気圧以上に保持する
ように設計した蒸気発生装置および蒸気発生装置の運転
方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a steam generator such as an exhaust heat recovery boiler, and more particularly to a steam generator having a economizer, and keeping the fluid pressure in the economizer above the saturated vapor pressure of the fluid temperature. Steam generator designed to operate and operation of steam generator
It is about the method .

【0002】[0002]

【従来の技術】高効率発電の一環として、最近、複合発
電プラントの開発が進められている。このプラントは、
ガスタービンによって発電すると共に、ガスタービンか
ら排出された排ガスの保有熱を排熱回収ボイラで回収
し、その排熱回収ボイラで発生した蒸気により蒸気ター
ビンを駆動して発電させるシステムになっている。
2. Description of the Related Art As part of high-efficiency power generation, development of a combined power generation plant has recently been promoted. This plant
In this system, electric power is generated by a gas turbine, heat retained in exhaust gas discharged from the gas turbine is collected by an exhaust heat recovery boiler, and steam generated by the exhaust heat recovery boiler drives a steam turbine to generate power.

【0003】このプラントはこのような高効率発電に加
え、ガスタービンの特長である急速起動の容易性、高い
負荷応答性などの特長も有しており、近年の電力需要形
態に即した中間負荷運用に好適な発電プラントである。
[0003] In addition to such high-efficiency power generation, this plant also has the features of gas turbines, such as easy start-up and high load responsiveness. It is a power plant suitable for operation.

【0004】図4は、この複合発電プラントの系統を説
明するための概略図である。図中の1はガスタービン、
2は発電機、3は蒸気タービン、4は復水器、5は排熱
回収ボイラ、6は給水ポンプ、7は低圧節炭器、8は低
圧蒸発器、9は低圧ドラム、10は給水ポンプ、11は
高圧節炭器、12は高圧蒸発器、13は高圧ドラム、1
4は過熱器、15、16は流量調整弁(第1、第2の流
量調整弁)、17は逆止弁、38は給水ポンプ10の
ニマムフロー弁(ミニマムフロー調整弁)、39はミニ
マムフロー管である。
FIG. 4 is a schematic diagram for explaining a system of the combined cycle power plant. 1 in the figure is a gas turbine,
2 is a generator, 3 is a steam turbine, 4 is a condenser, 5 is a waste heat recovery boiler, 6 is a feedwater pump, 7 is a low-pressure economizer, 8 is a low-pressure evaporator, 9 is a low-pressure drum, and 10 is a feedwater pump. , 11 is a high-pressure economizer, 12 is a high-pressure evaporator, 13 is a high-pressure drum, 1
4 is a superheater, 15 and 16 are flow control valves (first and second flow
The amount regulating valve), 17 check valve, 38 is a feed water pump 10 Mi
A minimum flow valve (minimum flow regulating valve) 39 is a minimum flow pipe .

【0005】同図において、排熱回収ボイラ5は、ガス
タービン1からの排熱を最大限に回収するために、排ガ
ス流路18上に過熱器14、高圧蒸発器12、高圧節炭
器11、低圧蒸発器8、低圧節炭器7などが配置されて
いる。しかし、特に、ホットスタートの起動時や低負荷
時には、排熱回収ボイラ5に流入するガス温度が低いた
め、比較的低温側の伝熱管群、すなわち、低圧節炭器7
や高圧節炭器11内で蒸発現象が生じる。そして、この
ように低圧節炭器7、高圧節炭器11内に気水混合流体
が存在すると、ボイラの制御が不安定になって運転継続
が困難になったり、ウオーターハンマ現象が生じて機器
が損傷する、などの種々の問題が生じる。
In FIG. 1, an exhaust heat recovery boiler 5 includes a superheater 14, a high-pressure evaporator 12, and a high-pressure economizer 11 on an exhaust gas passage 18 in order to recover exhaust heat from the gas turbine 1 to the maximum. , A low-pressure evaporator 8, a low-pressure economizer 7, and the like. However, particularly when the hot start is started or when the load is low, since the temperature of the gas flowing into the exhaust heat recovery boiler 5 is low, the heat transfer tube group on the relatively low temperature side, that is, the low pressure economizer 7 is used.
And an evaporation phenomenon occurs in the high-pressure economizer 11. When the air- water mixed fluid exists in the low-pressure economizer 7 and the high-pressure economizer 11 , the control of the boiler becomes unstable, making it difficult to continue the operation, and the water hammer phenomenon occurs, and Various problems occur, such as damage to the device.

【0006】このような問題を解決するために、同図に
示すように、低圧節炭器7と高圧節炭器11の出口側に
それぞれ流量調整弁15、16を設け、各給水ポンプ
6、10の吐出圧力を高めて、低圧節炭器7、高圧節炭
器11内の流体圧力をその流体温度の飽和蒸気圧以上に
保持し、蒸発現象の発生を防止している。
In order to solve such a problem, as shown in FIG. 1, flow control valves 15 and 16 are provided at the outlet side of the low-pressure economizer 7 and the high-pressure economizer 11, respectively. 10 discharge pressure is increased, low pressure economizer 7, high pressure economizer
The fluid pressure in the vessel 11 is maintained at or above the saturated vapor pressure of the fluid temperature, thereby preventing the occurrence of an evaporation phenomenon.

【0007】[0007]

【発明が解決しようとする課題】しかし、このような蒸
気発生装置においては、次のような問題があった。
However, such a steam generator has the following problems.

【0008】すなわち、起動時は給水ポンプ6、10を
起動して低圧ドラム9、高圧ドラム13のドラムレベル
が制御可能になった時点でガスタービンからの排ガス
を導入するが、低圧蒸発器8、高圧蒸発器12内の缶水
は昇温により体積が膨脹し、ドラム水位が上昇する。こ
のため、流量調整弁15、16は起動初期の10〜30
分間は閉じた状態にしておく。しかし、この間、低圧節
炭器7、高圧節炭器11系内の水は密閉された状態で加
熱されるので、流体の体積が毎分約1〜2%の割合で増
加する。水は非圧縮性流体であるから、内部流体の体積
増加分だけ系外に排出しなければ、低圧節炭器7、高圧
節炭器11内の圧力は毎分約30〜50kg/cm
加することになり、機器の破裂や噴破などの重大な事故
の原因となる。
Namely, the low-pressure drum 9 at start by starting the water supply pump 6, 10, but to introduce exhaust gas from the gas turbine 1 at the time when the drum level of the high-pressure drum 13 becomes controllable, low pressure evaporator 8 The volume of the can water in the high-pressure evaporator 12 expands due to the temperature rise, and the water level of the drum rises. For this reason, the flow control valves 15 and 16 are set to 10 to 30 in the initial stage of startup.
Keep closed for minutes. However, during this time, low pressure nodes
Since the water in the charcoal unit 7 and the high-pressure economizer 11 is heated in a sealed state, the volume of the fluid increases at a rate of about 1 to 2% per minute. Since water is an incompressible fluid, the low-pressure economizer 7 and the high-pressure
The pressure in the economizer 11 will increase by about 30 to 50 kg / cm 2 per minute, causing a serious accident such as rupture or blasting of equipment.

【0009】したがって、従来は、流量調整弁16のバ
イパス系として、オンオフ弁27とバイパス管26を設
け、流量調整弁16が閉のときにはオンオフ弁27を開
とし、低圧節炭器7、高圧節炭器11内流体の体積増加
分を高圧ドラム13に排出する。しかし、その分、高圧
ドラム13のレベルが上昇するので、今度はブロー弁3
0を開とし、系外に排水していた。この場合、高温の純
水を排出するため、非常にエネルギーの損失となってい
た。
Therefore, conventionally, an on / off valve 27 and a bypass pipe 26 are provided as a bypass system of the flow control valve 16, and the on / off valve 27 is opened when the flow control valve 16 is closed, so that the low pressure economizer 7 and the high pressure The increased volume of the fluid in the charcoal 11 is discharged to the high-pressure drum 13. However, since the level of the high-pressure drum 13 rises accordingly, the blow valve 3
0 was opened and water was drained out of the system. In this case, since high-temperature pure water is discharged, energy is extremely lost.

【0010】本発明は上記のような課題を解決するため
になされたもので、安全性が高く、かつ、省エネルギー
が図れる蒸気発生装置、蒸気発生装置の運転方法を提供
することを目的とする。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and an object of the present invention is to provide a steam generator and a method for operating the steam generator , which are highly safe and can save energy.

【0011】[0011]

【課題を解決するための手段】この目的を達成するた
め、本発明においては、高温ガスの流路中に配置された
節炭器に給水を供給する給水ポンプの出口に、上流から
逆止弁、給水止弁を設け、それらの弁の中間から給水ポ
ンプのミニマムフロー管を取り出す。また、上記給水止
弁の代りに、上記ミニマムフロー管に止弁を設ける。
In order to achieve this object, according to the present invention, a check valve is provided from the upstream to an outlet of a water supply pump for supplying water to a economizer disposed in a flow path of a high-temperature gas. A water supply stop valve is provided, and the minimum flow pipe of the water supply pump is taken out from the middle of the valves. Further, a stop valve is provided in the minimum flow pipe instead of the water supply stop valve.

【0012】また、ガスタービンから排出された高温ガ
スの流路中に低圧節炭器および高圧節炭器を配置し、該
低圧節炭器と該高圧節炭器との間に該高圧節炭器へ給水
を供給する給水ポンプを設置し、上記低圧節炭器に低圧
ドラムを接続し、上記高圧節炭器に高圧ドラムを接続
し、上記低圧節炭器と上記低圧ドラムとの間に第1の流
量調整弁を設け、上記高圧節炭器と上記高圧ドラムとの
間に第2の流量調整弁を設け、上記給水ポンプの出口に
上流から逆止弁、給水止弁を設け、該逆止弁と給水止弁
との間から、上記給水ポンプのミニマムフロー管を取り
出し、該ミニマムフロー管にミニマムフロー弁を設けた
蒸気発生装置の運転方法において、上記ガスタービンの
起動前に閉の上記ミニマムフロー弁を開とし、上記ガス
タービンの起動から上記低圧ドラムおよび上記高圧ドラ
ムの水位レベル変動がおさまるまでの間、上記第1、第
2の流量調整弁を全閉とする。
Further, the high-temperature gas discharged from the gas turbine is
A low-pressure economizer and a high-pressure economizer in the
Water supply to the high-pressure economizer between the low-pressure economizer and the high-pressure economizer
Install a water supply pump to supply low pressure to the low pressure economizer.
Connect the drum and connect the high pressure drum to the high pressure economizer
And a first flow between the low pressure economizer and the low pressure drum.
A quantity regulating valve is provided to connect the high-pressure economizer with the high-pressure drum.
A second flow control valve is provided in between, and at the outlet of the water supply pump
A check valve and a water supply stop valve are provided from the upstream, and the check valve and the water supply stop valve are provided.
Between the water pump and the minimum flow pipe.
The minimum flow pipe was provided with a minimum flow valve.
In the method for operating a steam generator, the gas turbine
Open the above minimum flow valve before starting and
From the start of the turbine, the low pressure drum and high pressure drum
Until the fluctuation of the water level of the
The flow control valve 2 is fully closed.

【0013】[0013]

【作用】上記のようにミニマムフロー管を取り付けるこ
とにより、給水ポンプのミニマムフローが行われると同
時に、上記蒸気発生装置における蒸気の昇圧時ならびに
降圧時のいずれか一方、またはその両方の状態におい
て、上記節炭器内にある被加熱流体(水)の体積膨脹分
を逃がす系統が実現したことになる。これにより、高温
純水の流出によるエネルギー損失が防止できると共に、
節炭器などの機器の裂傷の恐れも未然に防止できるよう
になった。
By installing the minimum flow pipe as described above, the minimum flow of the water supply pump is performed, and at the same time, when the steam is increased or decreased in the steam generator, or when both are reduced, This means that a system for releasing the volume expansion of the fluid to be heated (water) in the economizer has been realized. This can prevent energy loss due to the outflow of high-temperature pure water,
The possibility of laceration of equipment such as economizers can now be prevented.

【0014】[0014]

【実施例】(実施例1) 図1に、本発明に係る蒸気発生装置の系統図を示す。FIG. 1 shows a system diagram of a steam generator according to the present invention.

【0015】まず、図示してないが、空気供給管からの
燃焼用空気と燃料供給管からの燃料を燃焼室で混合、燃
焼させ、その燃焼ガスでガスタービン1を回転させて発
電を行う。ガスタービン1の回転に使用された排ガスは
排熱回収ボイラ5の排ガス流路18に導入される。この
排ガス流路18には、下流側から上流側に向けて、低圧
節炭器7、低圧蒸発器8、低圧ドラム9とからなる低圧
ボイラ、ならびに、高圧節炭器11、高圧蒸発器12、
高圧ドラム13および過熱器14とからなる高圧ボイラ
が配置されている。
First, although not shown, combustion air from an air supply pipe and fuel from a fuel supply pipe are mixed and burned in a combustion chamber, and the combustion gas is used to rotate the gas turbine 1 to generate power. The exhaust gas used for rotating the gas turbine 1 is introduced into an exhaust gas passage 18 of the exhaust heat recovery boiler 5. The exhaust gas passage 18 includes a low-pressure boiler including a low-pressure economizer 7, a low-pressure evaporator 8, and a low-pressure drum 9, and a high-pressure economizer 11, a high-pressure evaporator 12,
A high-pressure boiler including a high-pressure drum 13 and a superheater 14 is provided.

【0016】一方、被加熱流体である水は給水ポンプ6
により給水配管19を経て低圧節炭器7に供給され、所
定の温度まで加熱された後、流量調整弁15を介して低
圧ドラム9に導入される。低圧ドラム9に供給された水
は低圧蒸発器8、低圧ドラム9の順に自然に、または強
制的に循環され、その間に加熱されて低圧ドラム9内で
水と蒸気とに分離される。そして、分離された蒸気は低
圧主蒸気管21を通って蒸気タービン3に供給される。
On the other hand, the water to be heated is supplied by a water supply pump 6.
Is supplied to the low-pressure economizer 7 through the water supply pipe 19, is heated to a predetermined temperature, and is introduced into the low-pressure drum 9 via the flow control valve 15. The water supplied to the low-pressure drum 9 is circulated naturally or forcibly in the order of the low-pressure evaporator 8 and the low-pressure drum 9, while being heated and separated into water and steam in the low-pressure drum 9. Then, the separated steam is supplied to the steam turbine 3 through the low-pressure main steam pipe 21.

【0017】一方、低圧節炭器の出口側で分流された高
温水の一部は、給水ポンプ10により高温給水管22を
経て高圧節炭器11に供給され、所定の温度まで加熱さ
れた後、流量調整弁16を有するドラム給水管23を通
って、高圧ドラム13に供給される。高圧ドラム13に
供給された温水は、高圧蒸発器12、高圧ドラム13の
順で循環され、高圧ドラム13内で分離された蒸気は、
ドラム蒸気出口管24を経て過熱器14へ送られ、ここ
でさらに昇温された後に、高圧主蒸気管25より蒸気タ
ービン3へ送気される。
On the other hand, a part of the high-temperature water diverted at the outlet side of the low-pressure economizer is supplied to the high-pressure economizer 11 through the high-temperature water supply pipe 22 by the water supply pump 10 and is heated to a predetermined temperature. Is supplied to the high-pressure drum 13 through a drum water supply pipe 23 having a flow control valve 16. The hot water supplied to the high-pressure drum 13 is circulated in the order of the high-pressure evaporator 12 and the high-pressure drum 13, and the steam separated in the high-pressure drum 13 is
After being sent to the superheater 14 via the drum steam outlet pipe 24 and further heated here, the air is sent from the high-pressure main steam pipe 25 to the steam turbine 3.

【0018】こうして、蒸気タービン3による発電が行
われる。そして、蒸気タービン3の回転に使用された蒸
気は復水器4で水となり、給水ポンプ6により再び排熱
回収ボイラ5に供給される。
In this way, power is generated by the steam turbine 3. Then, the steam used for rotating the steam turbine 3 becomes water in the condenser 4, and is supplied again to the exhaust heat recovery boiler 5 by the water supply pump 6.

【0019】ここで上記流量調整弁15、16は、低圧
節炭器7、高圧節炭器11内の流体圧力(水圧)をその
流体温度の飽和蒸気圧以上に保持するように調整され、
器内での蒸気発生が抑制されている。
Here, the flow control valves 15 and 16 are connected to a low pressure
The fluid pressure (water pressure) in the economizer 7 and the high-pressure economizer 11 is adjusted to be equal to or higher than the saturated vapor pressure of the fluid temperature,
Steam generation in the vessel is suppressed.

【0020】本実施例の場合、給水ポンプ10出口の逆
止弁17の下流側に給水止弁32を設け、逆止弁17と
給水止弁32の間から、復水器4につながるミニマムフ
ロー管29とミニマムフロー弁(ミニマムフロー調整
弁)28とが設置されている。
In this embodiment, a water stop valve 32 is provided downstream of the check valve 17 at the outlet of the water supply pump 10, and a minimum flow connecting the condenser 4 from the space between the check valve 17 and the water stop valve 32. Pipe 29 and minimum flow valve (minimum flow adjustment
Valve 28 ) .

【0021】図2は、ガスタービン出力とドラムレベル
の特性図である。図中の曲線Aは高圧ドラムの水位レベ
ル、曲線Bは低圧ドラムの水位レベル、曲線Cはガスタ
ービンの出力を示している。この図のように、ガスター
ビン1が起動すると、低圧ドラム9と高圧ドラム13の
水位レベルが変動する。このため、本発明に係る蒸気発
生装置の運転方法においては、ガスタービンの起動か
低圧ドラム9と高圧ドラム13の水位レベルの変動が
おさまるまでの一定時間Tの間、上記流量調整弁15、
16を全閉とする
FIG. 2 is a characteristic diagram of gas turbine output and drum level. In the figure, curve A indicates the water level of the high pressure drum, curve B indicates the water level of the low pressure drum, and curve C indicates the output of the gas turbine. As shown in this figure, when the gas turbine 1 starts, the water level of the low-pressure drum 9 and the high-pressure drum 13 fluctuates. Therefore, the steam generation according to the present invention
In the operation method of the raw device, the flow control valve 15 is used for a certain time T from the start of the gas turbine 1 until the fluctuation of the water level of the low-pressure drum 9 and the high-pressure drum 13 stops.
16 is fully closed .

【0022】この場合、給水ポンプ10は過熱防止用に
ミニマムフローを確保する必要があるので、ミニマムフ
ロー弁28を開とする。また、給水止弁32は、ガスタ
ービン1が起動する前に開の状態にするので、ミニマム
フロー管29により、流量調整弁16が閉となっていて
も、高圧節炭器11内の膨脹した流体は、復水器4へ排
出することができる。これにより、高圧節炭器11の異
常昇圧が防止でき、従来のようにブロー弁を設けて系外
に排水する必要がなくなり、エネルギーの損失が防止で
きる。また本実施例では、ミニマムフロー管29が復水
器4につなげられているので、給水が十分に冷却され、
給水ポンプ10の異常過熱も防止できるようになった。
[0022] In this case, since the feed water pump 10, it is necessary to ensure a minimum flow for overheat Minimamufu
The low valve 28 is opened. Further, since the water supply stop valve 32 is opened before the gas turbine 1 starts, even if the flow control valve 16 is closed by the minimum flow pipe 29, the inside of the high-pressure economizer 11 expands. The fluid can be discharged to the condenser 4. As a result, abnormal high pressure of the high-pressure economizer 11 can be prevented, and there is no need to provide a blow valve and drain the water to the outside of the system as in the related art, thereby preventing energy loss. In this embodiment, since the minimum flow pipe 29 is connected to the condenser 4, the water supply is sufficiently cooled,
Abnormal overheating of the water supply pump 10 can also be prevented.

【0023】なお、図1では、ドラムが2個の場合につ
いて記載してあるが、ドラムが3個以上となり、給水ポ
ンプ10も複数台となっても、各ポンプのミニマムフロ
ー管29を逆止弁17の後流より取り出すことによっ
て、同様の効果が得られる。
Although FIG. 1 shows the case where there are two drums, even if the number of drums is three or more and the number of water supply pumps 10 is plural, the minimum flow pipe 29 of each pump must be checked. The same effect can be obtained by extracting from the downstream of the valve 17.

【0024】(実施例2) 図3は、本発明に係る他の実施例を示したものである。
ここでは、高圧節炭器11入口の給水止弁32を無く
し、その代りに、ミニマムフロー管29に止弁33を設
けたものである。この止弁33を設けた理由は、停止中
に、節炭器11内の給水が復水器4へ流れ出し、高圧
炭器11が空になることを防止するためである。
Embodiment 2 FIG. 3 shows another embodiment according to the present invention.
Here, the water supply stop valve 32 at the inlet of the high-pressure economizer 11 is eliminated, and a stop valve 33 is provided in the minimum flow pipe 29 instead. The reason why the stop valve 33 is provided is to prevent the supply of water in the economizer 11 from flowing out to the condenser 4 during stoppage, thereby preventing the high-pressure economizer 11 from being emptied.

【0025】[0025]

【発明の効果】以上説明したように、本発明に係る蒸気
発生装置、蒸気発生装置の運転方法においては、給水ポ
ンプ出口からミニマムフロー管を取り出したので、熱膨
脹した被加熱流体による節炭器などの破裂損傷がなくな
り、安全性が確保できると共に、節炭器内の膨脹水は全
て系内で回収できるので、エネルギーの損失がなく経済
性の向上を図ることができる。
As described above , in the steam generator and the operation method of the steam generator according to the present invention, the minimum flow pipe is taken out from the outlet of the feed water pump, so that the economizer using the heat-expanded fluid to be heated can be used. As a result, the explosion damage of the fuel cell can be eliminated, the safety can be ensured, and all the inflation water in the economizer can be recovered in the system.

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

【図1】本発明に係る排熱回収ボイラの概略構成図であ
る。
FIG. 1 is a schematic configuration diagram of an exhaust heat recovery boiler according to the present invention.

【図2】ガスタービンの出力とドラムレベルの特性を示
す図である。
FIG. 2 is a diagram showing characteristics of a gas turbine output and a drum level.

【図3】本発明に係る他の実施例の構成を示す部分図で
ある。
FIG. 3 is a partial view showing the configuration of another embodiment according to the present invention.

【図4】従来技術の排熱回収ボイラの概略構成図であ
る。
FIG. 4 is a schematic configuration diagram of a conventional exhaust heat recovery boiler.

【符号の説明】[Explanation of symbols]

1 ガスタービン 2 発電機 3 蒸気タービン 4 復水器 5 排熱回収ボイラ 6 給水ポンプ 7 低圧節炭器 8 低圧蒸発器 9 低圧ドラム 10 給水ポンプ 11 高圧節炭器 12 高圧蒸発器 13 高圧ドラム 14 過熱器 15、16 流量調整弁 17 逆止弁 18 排ガス流路 19 給水配管 21 低圧主蒸気管 22 高圧給水管 23 ドラム給水管 24 ドラム蒸気出口管 25 高圧主蒸気管 26 バイパス管 27 バイパスオンオフ弁 28 ミニマムフロー弁 29 ミニマムフロー管 30 ドラムブロー弁 31 ドラムブロー管 32 給水止弁 33 止弁 DESCRIPTION OF SYMBOLS 1 Gas turbine 2 Generator 3 Steam turbine 4 Condenser 5 Exhaust heat recovery boiler 6 Feed water pump 7 Low pressure economizer 8 Low pressure evaporator 9 Low pressure drum 10 Water pump 11 High pressure economizer 12 High pressure evaporator 13 High pressure drum 14 Superheat Apparatus 15, 16 Flow control valve 17 Check valve 18 Exhaust gas flow path 19 Water supply pipe 21 Low pressure main steam pipe 22 High pressure water supply pipe 23 Drum water supply pipe 24 Drum steam outlet pipe 25 High pressure main steam pipe 26 Bypass pipe 27 Bypass on / off valve 28 Minimum Flow valve 29 Minimum flow pipe 30 Drum blow valve 31 Drum blow pipe 32 Water supply stop valve 33 Stop valve

フロントページの続き (56)参考文献 特開 平4−116301(JP,A) 特開 平1−179805(JP,A) 特開 平5−296409(JP,A) 実開 昭63−5206(JP,U) (58)調査した分野(Int.Cl.7,DB名) F22D 11/00 F22B 1/18 Continuation of the front page (56) References JP-A-4-116301 (JP, A) JP-A-1-179805 (JP, A) JP-A-5-296409 (JP, A) JP-A-63-5206 (JP) , U) (58) Field surveyed (Int. Cl. 7 , DB name) F22D 11/00 F22B 1/18

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】高温ガスの流路中に少なくとも節炭器を配
置し、該節炭器へ給水を供給する給水ポンプを設置し
上記節炭器にドラムを接続し、上記節炭器と上記ドラム
との間に流量調整弁を設けた蒸気発生装置において、上
記給水ポンプの出口に上流から逆止弁、給水止弁を設
け、該逆止弁と給水止弁との間から、上記給水ポンプの
ミニマムフロー管を取り出し、該ミニマムフロー管にミ
ニマムフロー弁を設けたことを特徴とする蒸気発生装
置。
At least a economizer is disposed in a flow path of a high-temperature gas, and a water supply pump for supplying water to the economizer is installed .
Connect a drum to the economizer, and save the economizer and the drum
In the steam generator provided with a flow control valve in between, a check valve and a water stop valve are provided from the upstream at the outlet of the water supply pump, and between the check valve and the water stop valve, the check valve of the water supply pump is provided. Take out the minimum flow tube and insert it into the minimum flow tube.
A steam generator characterized by having a nimum flow valve .
【請求項2】高温ガスの流路中に少なくとも節炭器を配
置し、該節炭器へ給水を供給する給水ポンプを設置し
上記節炭器にドラムを接続し、上記節炭器と上記ドラム
との間に流量調整弁を設けた蒸気発生装置において、上
記給水ポンプの出口側に逆止弁を設け、さらに該逆止弁
と上記節炭器との間から上記給水ポンプのミニマムフロ
ー管を取り出し、該ミニマムフロー管に上流から止弁
ミニマムフロー弁を設けたことを特徴とする蒸気発生装
置。
2. At least a economizer is disposed in a flow path of a high-temperature gas, and a water supply pump for supplying water to the economizer is installed .
Connect a drum to the economizer, and save the economizer and the drum
In the steam generator provided with a flow control valve between the check valve, a check valve is provided on the outlet side of the feed pump, and furthermore, a minimum flow pipe of the feed pump is provided between the check valve and the economizer. Take out, stop valve from the upstream to the minimum flow pipe ,
A steam generator characterized by having a minimum flow valve .
【請求項3】ガスタービンから排出された高温ガスの流
路中に低圧節炭器および高圧節炭器を配置し、該低圧節
炭器と該高圧節炭器との間に該高圧節炭器へ給水を供給
する給水ポンプを設置し、上記低圧節炭器に低圧ドラム
を接続し、上記高圧節炭器に高圧ドラムを接続し、上記
低圧節炭器と上記低圧ドラムとの間に第1の流量調整弁
を設け、上記高圧節炭器と上記高圧ドラムとの間に第2
の流量調整弁を設け、上記給水ポンプの出口に上流から
逆止弁、給水止弁を設け、該逆止弁と給水止弁との間か
ら、上記給水ポンプのミニマムフロー管を取り出し、該
ミニマムフロー管にミニマムフロー弁を設けた蒸気発生
装置の運転方法において、上記ガスタービンの起動前に
閉の上記ミニマムフロー弁を開とし、上記ガスタービン
の起動から上記低圧ドラムおよび上記高圧ドラムの水位
レベル変動がおさまるまでの間、上記第1、第2の流量
調整弁を全閉とすることを特徴とする蒸気発生装置の運
転方法。
3. A low-pressure economizer and a high-pressure economizer are arranged in a flow path of a high-temperature gas discharged from a gas turbine, and the high-pressure economizer is disposed between the low-pressure economizer and the high-pressure economizer. A water supply pump that supplies water to the vessel is installed, a low-pressure drum is connected to the low-pressure economizer, a high-pressure drum is connected to the high-pressure economizer, and a water pump is connected between the low-pressure economizer and the low-pressure drum. 1 is provided between the high-pressure economizer and the high-pressure drum.
And a check valve and a water stop valve are provided at the outlet of the water supply pump from the upstream, and a minimum flow pipe of the water supply pump is taken out from between the check valve and the water stop valve. In the method for operating a steam generator in which a minimum flow valve is provided in a flow pipe, the minimum flow valve that is closed is opened before the gas turbine is started, and the water level of the low-pressure drum and the high-pressure drum is changed from the start of the gas turbine. A method for operating a steam generator, wherein the first and second flow control valves are fully closed until the fluctuation stops.
JP03822793A 1993-02-26 1993-02-26 Steam generator and method of operating the same Expired - Lifetime JP3335696B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP03822793A JP3335696B2 (en) 1993-02-26 1993-02-26 Steam generator and method of operating the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP03822793A JP3335696B2 (en) 1993-02-26 1993-02-26 Steam generator and method of operating the same

Publications (2)

Publication Number Publication Date
JPH06249405A JPH06249405A (en) 1994-09-06
JP3335696B2 true JP3335696B2 (en) 2002-10-21

Family

ID=12519427

Family Applications (1)

Application Number Title Priority Date Filing Date
JP03822793A Expired - Lifetime JP3335696B2 (en) 1993-02-26 1993-02-26 Steam generator and method of operating the same

Country Status (1)

Country Link
JP (1) JP3335696B2 (en)

Also Published As

Publication number Publication date
JPH06249405A (en) 1994-09-06

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