JP3117392B2 - Start-up method of an exhaust gas re-combustion complex plant - Google Patents

Start-up method of an exhaust gas re-combustion complex plant

Info

Publication number
JP3117392B2
JP3117392B2 JP07206982A JP20698295A JP3117392B2 JP 3117392 B2 JP3117392 B2 JP 3117392B2 JP 07206982 A JP07206982 A JP 07206982A JP 20698295 A JP20698295 A JP 20698295A JP 3117392 B2 JP3117392 B2 JP 3117392B2
Authority
JP
Japan
Prior art keywords
boiler
pressure
gas
exhaust gas
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 - Fee Related
Application number
JP07206982A
Other languages
Japanese (ja)
Other versions
JPH0953801A (en
Inventor
聡 野中
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 Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP07206982A priority Critical patent/JP3117392B2/en
Publication of JPH0953801A publication Critical patent/JPH0953801A/en
Application granted granted Critical
Publication of JP3117392B2 publication Critical patent/JP3117392B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/16Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]

Landscapes

  • Engine Equipment That Uses Special Cycles (AREA)
  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)

Description

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

【0001】[0001]

【発明の属する技術分野】本発明はガスタービンの排気
をボイラの燃焼用空気として熱回収する複合プラントの
起動方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of starting a combined plant for recovering heat of gas turbine exhaust as boiler combustion air.

【0002】[0002]

【従来の技術】図2は従来の排気再燃型複合プラントの
一例を示す系統図である。従来はガスタービン(1)の
出口に排気筒を設置し、ガスタービン系と汽力系を、別
々に起動して、おのおのの単独運転から複合運転に切換
えるか、排気筒がない場合にはボイラを先に起動して、
ある程度負荷を取ったのち、ガスタービンを起動してい
た。これらの場合、いずれも押込通風機(FDF)を用
いボイラを起動する必要があった。
2. Description of the Related Art FIG. 2 is a system diagram showing an example of a conventional exhaust gas reburning type combined plant. Conventionally, an exhaust stack is installed at the outlet of the gas turbine (1), and the gas turbine system and the steam system are separately activated to switch from individual operation to combined operation, or to operate the boiler if there is no exhaust stack. Start first,
After some load, he started the gas turbine. In each of these cases, it was necessary to start the boiler using a forced air ventilator (FDF).

【0003】すなわち、ユニット起動時にガスタービン
単独運転を行なう場合には、ガスタービン出口に排気筒
を設置し、更にその排気筒の出口に脱硝装置を設けるこ
とが必要となる。この時、排気筒のダンパ(13)を開
き、ガスタービン出口〜ボイラ間に設置されたダンパ
(10)は閉じる。
[0003] That is, when the gas turbine alone is operated at the time of starting the unit, it is necessary to install an exhaust pipe at the outlet of the gas turbine and further provide a denitration device at the outlet of the exhaust pipe. At this time, the damper (13) of the exhaust stack is opened, and the damper (10) installed between the gas turbine outlet and the boiler is closed.

【0004】次に空気予熱器(AH),押込通風機(F
DF)を使用して蒸気タービン,ボイラ系統を起動する
ためには、ガスタービン出口ダンパ(10)を閉じると
共にガスクーラ系をダンパ(11)によって系統より切
離す必要がある。これと同時に空気予熱器入口ダンパ
(12)を開き、脱硝装置出口より空気予熱器(AH)
側へボイラ排ガスを導く。ボイラの昇温,昇圧後は押込
通風機(FDF)を徐々に絞り、O2 源をガスタービン
出口排ガスに切換える。(ダンパ(12),(13)を
閉じダンパ(10),(11)を開く。)このようにボ
イラを単独で起動するためには、燃焼用空気が必要とな
るので、押込送風機(FDF)を別途設けることが必要
であり、更にガスクーラを経由せずにボイラからの排ガ
スを大気に出すため、従来の通常のボイラと同様に空気
予熱器(AH),誘引送風機(IDF),煙突を設ける
必要がある。
Next, an air preheater (AH) and a forced draft fan (F)
In order to start the steam turbine and the boiler system using the DF), it is necessary to close the gas turbine outlet damper (10) and disconnect the gas cooler system from the system by the damper (11). At the same time, the air preheater inlet damper (12) is opened, and the air preheater (AH) is opened from the denitration device outlet.
Boiler exhaust gas to the side. After the boiler is heated and pressurized, the forced air ventilator (FDF) is gradually throttled to switch the O 2 source to the exhaust gas at the gas turbine outlet. (The dampers (12) and (13) are closed and the dampers (10) and (11) are opened.) In order to start the boiler alone, combustion air is required, so a forced air blower (FDF) It is necessary to provide an air preheater (AH), an induction blower (IDF), and a chimney in the same manner as a conventional ordinary boiler in order to discharge exhaust gas from the boiler to the atmosphere without passing through a gas cooler. There is a need.

【0005】[0005]

【発明が解決しようとする課題】従来、ガスタービンを
先に起動する時は、コンバインド運転へ移行するまでの
間、ガスタービンの排気が直接大気へ放出されることが
あったが、公害規制が厳しくなり起動時でも未処理のガ
スを大気放出できない状況となっており、脱硝装置が必
要である。またボイラを先に起動する場合、通常運転時
に押込通風機や起動用のファンを使用する必要がなくと
も、ボイラの先行的な起動のために、空気予熱器,押込
通風機等を使用せざるを得ないことになる。
Conventionally, when the gas turbine is started first, the exhaust gas of the gas turbine may be directly discharged to the atmosphere until the operation is switched to the combined operation. The situation has become so severe that untreated gas cannot be released to the atmosphere even at the time of startup, and a denitration device is required. In addition, when starting the boiler first, it is not necessary to use a forced draft fan or a startup fan during normal operation, but it is necessary to use an air preheater, a forced draft fan, etc. for the advance startup of the boiler. You will not get.

【0006】そこでガスタービンとボイラを同時に起動
することが望ましいが、図2に示される従来の系統によ
って起動を行なう場合には、高圧ガスクーラ(4)にお
いて給水が加熱されて蒸発してしまう可能性がある。本
発明は、この高圧ガスクーラ(4)における給水の蒸発
を防止しつつ、起動する方法を提案するものである。
Therefore, it is desirable to start the gas turbine and the boiler at the same time. However, when starting with the conventional system shown in FIG. 2, there is a possibility that the feed water is heated and evaporated in the high-pressure gas cooler (4). There is. The present invention proposes a method of starting the feed water in the high-pressure gas cooler (4) while preventing the feed water from evaporating.

【0007】[0007]

【課題を解決するための手段】本発明者は、前記従来の
課題を解決するために、給水を蒸気で加熱する高圧給水
ヒータとボイラ排ガスで加熱する高圧ガスクーラとがボ
イラ給水系に並列に設置され、かつガスタービン排気中
の残存酸素をボイラの燃焼用に用いる排気再燃型複合プ
ラントにおいて、上記高圧ガスクーラの給水出口に止め
弁を設け、起動に際しては、上記止め弁を閉じ、その上
流の給水圧力をボイラ側残圧よりも高く、起動時のガス
熱吸収に対してスチーミングしない圧力に設定した状態
で、上記ガスタービンおよびボイラを順次点火して、上
記高圧給水ヒータから低温の給水をボイラに供給し、ボ
イラ昇圧によりボイラ側の圧力が給水側とバランスした
時点で上記止め弁を開いて、上記高圧給水ヒータと高圧
ガスクーラから同時に連続して給水を供給することを特
徴とする排気再燃型複合プラントの起動方法を提案する
ものである。
In order to solve the above-mentioned conventional problems, the present inventor has set up a high-pressure water heater for heating feed water with steam and a high-pressure gas cooler for heating boiler exhaust gas in parallel in a boiler feed system. And a stop valve is provided at a water supply outlet of the high-pressure gas cooler, and at the time of start-up, the stop valve is closed and the upstream water supply is performed. The gas turbine and the boiler are sequentially ignited in a state where the pressure is set to a pressure higher than the boiler side residual pressure and does not steam against gas heat absorption at the time of startup, and low-temperature water is supplied from the high-pressure water heater to the boiler. When the boiler pressure rises and the boiler side pressure balances with the water supply side, the stop valve is opened and the high pressure water heater and high pressure gas cooler It proposes a method of starting repowering composite plant and supplying the water continuously to.

【0008】本発明の方法によれば上記のとおり、起動
に際して、高圧ガスクーラの給水出口に設けられた止め
弁を閉じ、その上流の給水圧力をボイラ側残圧よりも高
く、起動時のガス熱吸収に対してスチーミングしない圧
力に設定した状態で、上記ガスタービンおよびボイラを
順次点火して、上記高圧給水ヒータから低温の給水をボ
イラに供給するので、ボイラ側の残圧が低い場合にも高
圧ガスクーラのスチーミングが防止される。またボイラ
昇圧によりボイラ側の圧力が給水側とバランスし、両系
統の圧力がほぼ等しくなった時点で上記止め弁を開い
て、上記高圧給水ヒータと高圧ガスクーラから同時に連
続して給水を供給するので、外乱が少なく円滑な起動が
可能となる。
According to the method of the present invention, as described above, at the time of startup, the stop valve provided at the water supply outlet of the high-pressure gas cooler is closed, the upstream water supply pressure is higher than the boiler side residual pressure, and the gas heat While the gas turbine and the boiler are sequentially ignited and the low-temperature water is supplied from the high-pressure water heater to the boiler in a state where the pressure is set so as not to be steamed for absorption, even when the residual pressure on the boiler side is low. Steaming of the high pressure gas cooler is prevented. Also, when the pressure on the boiler balances with the water supply side due to the boiler pressure increase, the stop valve is opened when the pressures of both systems become substantially equal, and the water supply is continuously and simultaneously supplied from the high pressure water heater and the high pressure gas cooler. In addition, smooth start-up is possible with less disturbance.

【0009】[0009]

【発明の実施の形態】図1は本発明の実施の一形態を示
す系統図である。本実施形態では、高圧ガスクーラ
(4)の給水出口に止め弁(7)が設けられる。
FIG. 1 is a system diagram showing an embodiment of the present invention. In the present embodiment, a stop valve (7) is provided at a water supply outlet of the high-pressure gas cooler (4).

【0010】この複合プラントを起動するに際しては、
まず高圧ガスクーラ(4)の給水系をボイラ残圧よりも
高圧で高圧ガスクーラ(4)でスチーミングを起こさな
い圧力に保持し、止め弁(7)を閉じることによってボ
イラ系と給水系を切離した状態で、ガスタービン(1)
とボイラ(2)に点火する。その場合、給水はドラムレ
ベル調節弁(6)を介して間欠的に給水する。また高圧
ガスクーラ(4)通過後の給水は、再循環流量調節弁
(8)を経由して復水器へ再循環させる。
When starting up the combined plant,
First, the water supply system of the high-pressure gas cooler (4) was maintained at a pressure higher than the boiler residual pressure so as not to cause steaming in the high-pressure gas cooler (4), and the stop valve (7) was closed to separate the boiler system and the water supply system. In the state, the gas turbine (1)
And ignite the boiler (2). In this case, the water is supplied intermittently via the drum level control valve (6). The water supply after passing through the high-pressure gas cooler (4) is recirculated to the condenser via the recirculation flow control valve (8).

【0011】点火後はドラムレベル調節弁(6)により
ボイラドラムへ給水を供給しつつボイラ(2)を昇圧し
てゆく。そしてボイラ(2)と高圧ガスクーラ(4)の
圧力が一致した時点で、止め弁(7)を全開にすること
により、高圧給水ヒータ(3)側と高圧ガスクーラ
(4)側の両系統から並行してボイラ(1)に給水する
系統が確立される。
After the ignition, the boiler (2) is pressurized while supplying water to the boiler drum by the drum level control valve (6). Then, when the pressures of the boiler (2) and the high-pressure gas cooler (4) match, the stop valve (7) is fully opened, so that the two systems on the high-pressure feed water heater (3) side and the high-pressure gas cooler (4) side operate in parallel. Then, a system for supplying water to the boiler (1) is established.

【0012】その後は従来の一般的なボイラと同様に昇
圧する。なお、止め弁(7)を開いた後は、ドラムレベ
ルの制御を起動用のドラムレベル調節弁(6)から常用
のドラムレベル調節弁(9)に切換えるとともに、高圧
ガスクーラ(4)側に十分な給水を供給するため、再循
環流量調節弁(8)を用いて、高圧ガスクーラ(4)出
口の給水の温度を制御する。ボイラ給水の温度が高くな
れば節炭器のスチーミングが懸念されるからである。特
に低負荷時や起動時はガスタービンの排ガス量が一定と
なるため、ボイラ給水温度(高圧ガスクーラ出口給水温
度)が高めになり、再循環流量調節弁(8)が開く。
Thereafter, the pressure is increased as in a conventional general boiler. After the stop valve (7) is opened, the control of the drum level is switched from the starting drum level adjusting valve (6) to the regular drum level adjusting valve (9), and the high-pressure gas cooler (4) side is sufficiently controlled. In order to supply a proper supply of water, the temperature of the supply water at the outlet of the high-pressure gas cooler (4) is controlled using the recirculation flow control valve (8). This is because if the temperature of the boiler feedwater increases, steaming of the economizer may become a concern. In particular, when the load is low or when the engine is started, the exhaust gas amount of the gas turbine is constant, so that the boiler feedwater temperature (the high-pressure gas cooler outlet feedwater temperature) increases, and the recirculation flow control valve (8) opens.

【0013】[0013]

【発明の効果】従来は、起動時にガスタービンの排ガス
を公害規制値内に処理するため、別途脱硝装置等の排ガ
ス処理系を設けるか、またはボイラを先行的に起動する
場合には空気予熱器や押込通風機等をプラント起動のた
めだけに設ける必要があった。
Conventionally, an exhaust gas treatment system such as a denitration apparatus is separately provided in order to treat the exhaust gas of the gas turbine within the pollution regulation value at the time of starting, or an air preheater is used when the boiler is started in advance. It was necessary to provide a fan and a forced draft fan only for starting the plant.

【0014】本発明によれば、ガスタービン排気筒の排
ガス処理を常用の設備で行なうことができる。また空気
予熱器,押込通風機等の補機をプラントの起動時のみ運
転する必要がなくなり、ガスタービン排ガスのみを用い
た起動が可能となる。これにより、空気予熱器やファン
等の設備が不要となり、また起動損失を減少し、起動時
間を短縮する。
According to the present invention, the exhaust gas treatment of the gas turbine exhaust stack can be performed by ordinary equipment. Further, it is not necessary to operate auxiliary equipment such as an air preheater and a forced draft fan only at the time of starting the plant, and starting using only gas turbine exhaust gas becomes possible. This eliminates the need for equipment such as an air preheater and a fan, reduces startup loss, and shortens startup time.

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

【図1】図1は本発明の実施の一形態を示す系統図であ
る。
FIG. 1 is a system diagram showing an embodiment of the present invention.

【図2】図2は従来の排気再燃型複合プラントの一例を
示す系統図である。
FIG. 2 is a system diagram showing an example of a conventional exhaust gas reburning combined plant.

【符号の説明】[Explanation of symbols]

(1) ガスタービン (2) ボイラ (3) 高圧給水ヒータ (4) 高圧ガスクーラ (6) ドラムレベル調節弁(起動用) (7) 止め弁 (8) 再循環流量調節弁 (9) ドラムレベル調節弁(常用) (10),(11),(12),(13) ダンパ (AH) 空気予熱器 (FDF) 押込通風機 (IDF) 誘引通風機 (1) Gas turbine (2) Boiler (3) High pressure feed water heater (4) High pressure gas cooler (6) Drum level control valve (for starting) (7) Stop valve (8) Recirculation flow rate control valve (9) Drum level control Valve (common use) (10), (11), (12), (13) Damper (AH) Air preheater (FDF) Push-in ventilator (IDF) Induction ventilator

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 給水を蒸気で加熱する高圧給水ヒータと
ボイラ排ガスで加熱する高圧ガスクーラとがボイラ給水
系に並列に設置され、かつガスタービン排気中の残存酸
素をボイラの燃焼用に用いる排気再燃型複合プラントに
おいて、上記高圧ガスクーラの給水出口に止め弁を設
け、起動に際しては、上記止め弁を閉じ、その上流の給
水圧力をボイラ側残圧よりも高く、起動時のガス熱吸収
に対してスチーミングしない圧力に設定した状態で、上
記ガスタービンおよびボイラを順次点火して、上記高圧
給水ヒータから低温の給水をボイラに供給し、ボイラ昇
圧によりボイラ側の圧力が給水側とバランスした時点で
上記止め弁を開いて、上記高圧給水ヒータと高圧ガスク
ーラから同時に連続して給水を供給することを特徴とす
る排気再燃型複合プラントの起動方法。
1. A high-pressure water heater for heating feedwater with steam and a high-pressure gas cooler for heating with boiler exhaust gas are installed in parallel in a boiler water supply system, and exhaust gas refueling using residual oxygen in gas turbine exhaust for boiler combustion. In the combined type plant, a stop valve is provided at the water supply outlet of the high-pressure gas cooler, and at the time of startup, the stop valve is closed, and the upstream water supply pressure is higher than the boiler side residual pressure. In a state where the steaming is set at a non-steaming pressure, the gas turbine and the boiler are sequentially ignited, and low-temperature water is supplied from the high-pressure water heater to the boiler. Opening the stop valve and supplying water continuously from the high-pressure water heater and the high-pressure gas cooler simultaneously; How to start the event.
JP07206982A 1995-08-14 1995-08-14 Start-up method of an exhaust gas re-combustion complex plant Expired - Fee Related JP3117392B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP07206982A JP3117392B2 (en) 1995-08-14 1995-08-14 Start-up method of an exhaust gas re-combustion complex plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP07206982A JP3117392B2 (en) 1995-08-14 1995-08-14 Start-up method of an exhaust gas re-combustion complex plant

Publications (2)

Publication Number Publication Date
JPH0953801A JPH0953801A (en) 1997-02-25
JP3117392B2 true JP3117392B2 (en) 2000-12-11

Family

ID=16532225

Family Applications (1)

Application Number Title Priority Date Filing Date
JP07206982A Expired - Fee Related JP3117392B2 (en) 1995-08-14 1995-08-14 Start-up method of an exhaust gas re-combustion complex plant

Country Status (1)

Country Link
JP (1) JP3117392B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4771309B2 (en) * 2005-12-20 2011-09-14 独立行政法人土木研究所 Pressurized fluidized incineration equipment and its startup method

Also Published As

Publication number Publication date
JPH0953801A (en) 1997-02-25

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