JPH05288301A - Coal firing discharged gas re-igniting combined cycle plant - Google Patents

Coal firing discharged gas re-igniting combined cycle plant

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Publication number
JPH05288301A
JPH05288301A JP4115498A JP11549892A JPH05288301A JP H05288301 A JPH05288301 A JP H05288301A JP 4115498 A JP4115498 A JP 4115498A JP 11549892 A JP11549892 A JP 11549892A JP H05288301 A JPH05288301 A JP H05288301A
Authority
JP
Japan
Prior art keywords
duct
exhaust gas
boiler
air
air preheater
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
JP4115498A
Other languages
Japanese (ja)
Inventor
Masahiro Ozawa
政弘 小沢
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.)
IHI Corp
Original Assignee
IHI Corp
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 IHI Corp filed Critical IHI Corp
Priority to JP4115498A priority Critical patent/JPH05288301A/en
Publication of JPH05288301A publication Critical patent/JPH05288301A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To improve a combustion stability, simplify a facility, reduce a facility expenditure, decrease a consumption power and further reduce a leaking rate of an air preheater. CONSTITUTION:A primary air duct 15 having a primary air preheater 7 for use in preheating primary air with discharged gas flowing in a boiler discharged gas branching duct 23 branched from a boiler discharged gas duct 17 at an upstream side of a gas cooler 9 arranged in the midway part thereof is connected to a mill 4 connected to a fuel pipe 14 of a boiler 1, a primary blower 5 is arranged at an upstream side and then a primary air preheater bypass duct 24 connecting an upstream side and a downstream side of the primary air preheater 7 is installed. A secondary air preheater 8 for use in preheating secondary air with heat of the discharged gas flowing within the boiler discharged gas duct 17 is arranged in the midway part of the secondary air duct 16 of the boiler 1. A steam type air preheater 11 is arranged in the midway part of the secondary air duct 16 at an upstream side of the secondary air preheater 8 and a forced drafting machine 6 is arranged at an upstream side of it.

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、石炭焚排気再燃コンバ
インドサイクルプラントに関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a coal-fired exhaust gas re-combustion combined cycle plant.

【0002】[0002]

【従来の技術】近年、ガスタービンにより発電機を駆動
すると共にガスタービンからのタービン排ガス中の未燃
焼酸素をボイラでの燃料の燃焼に使用し、ボイラで生成
された蒸気により発電機を駆動し、ボイラ排ガスにより
ボイラへ供給される給水を加熱する、石炭焚排気再燃コ
ンバインドサイクルプラントが実用化されている。
2. Description of the Related Art In recent years, a generator is driven by a gas turbine, and unburned oxygen in turbine exhaust gas from the gas turbine is used to burn fuel in a boiler, and the generator is driven by steam generated in the boiler. A coal-fired exhaust gas re-combustion combined cycle plant that heats feed water supplied to the boiler by the boiler exhaust gas has been put into practical use.

【0003】前記石炭焚排気再燃コンバインドサイクル
プラントのガス系統を主体としたフローは図3に示さ
れ、図中、1は石炭焚のボイラ、2はガスタービン、3
はガスタービン2により駆動される発電機であり、ボイ
ラ1には、燃料としての微粉炭を供給するための燃料管
14と、燃焼用の二次空気を供給するための二次空気ダ
クト16とを接続すると共に、燃焼排ガスを図示してい
ない電気集塵機を介して煙突から排出するためのボイラ
排ガスダクト17を接続してある。
A flow mainly composed of a gas system of the coal-fired exhaust gas re-combustion combined cycle plant is shown in FIG. 3, in which 1 is a coal-fired boiler, 2 is a gas turbine, and 3 is a gas turbine.
Is a generator driven by the gas turbine 2, and the boiler 1 is provided with a fuel pipe 14 for supplying pulverized coal as a fuel, and a secondary air duct 16 for supplying secondary air for combustion. And a boiler exhaust gas duct 17 for discharging the combustion exhaust gas from the chimney via an electric dust collector (not shown).

【0004】前記二次空気ダクト16途中には、前記ボ
イラ排ガスダクト17内を流れる排ガスの熱により二次
空気を予熱するための空気予熱器8’を設け、該空気予
熱器8’の上流側には押込通風機6を設けてある。
An air preheater 8'for preheating the secondary air by the heat of the exhaust gas flowing in the boiler exhaust gas duct 17 is provided in the middle of the secondary air duct 16 and the upstream side of the air preheater 8 '. A push-in fan 6 is provided in the.

【0005】前記燃料管14には石炭粉砕用のミル4を
接続し、該ミル4には、前記空気予熱器8’より下流側
の二次空気ダクト16から分岐し且つ途中に一次通風機
5が設けられた一次空気ダクト15を接続してある。
A coal crushing mill 4 is connected to the fuel pipe 14, and the mill 4 is branched from a secondary air duct 16 downstream of the air preheater 8'and a primary blower 5 is provided midway. Is connected to the primary air duct 15.

【0006】前記空気予熱器8’より上流側のボイラ排
ガスダクト17途中には、ボイラ1へ送給される給水を
加熱し且つ排ガスを冷却するためのガスクーラ9を設け
てあり、又、前記一次空気ダクト15分岐部より下流側
の二次空気ダクト16途中には、ガスタービン2の排気
を導入するための排気導入ダクト18を接続し、該排気
導入ダクト18から分岐せしめた排気導入分岐ダクト1
9を前記一次空気ダクト15途中に接続すると共に、前
記排気導入ダクト18から分岐し且つボイラ1をバイパ
スするボイラバイパス排気ダクト20を前記ガスクーラ
9より上流側のボイラ排ガスダクト17途中に接続して
ある。
A gas cooler 9 for heating the feed water fed to the boiler 1 and cooling the exhaust gas is provided in the middle of the boiler exhaust gas duct 17 upstream of the air preheater 8 ', and the primary An exhaust gas introduction duct 18 for introducing the exhaust gas of the gas turbine 2 is connected in the middle of the secondary air duct 16 downstream of the branch portion of the air duct 15, and the exhaust gas introduction branch duct 1 is branched from the exhaust gas introduction duct 18.
9 is connected in the middle of the primary air duct 15, and a boiler bypass exhaust duct 20 that branches from the exhaust introduction duct 18 and bypasses the boiler 1 is connected in the middle of the boiler exhaust gas duct 17 upstream of the gas cooler 9. ..

【0007】前記空気予熱器8’より上流側の二次空気
ダクト16から分岐し且つ空気予熱器8’をバイパスす
る空気予熱器バイパスダクト21を、前記一次通風機5
より上流側の一次空気ダクト15途中に接続し、又、前
記ボイラ排ガスダクト17途中に、ガスクーラ9の上下
流位置を結ぶガスクーラバイパスダクト22を設けてあ
る。
An air preheater bypass duct 21 that branches from the secondary air duct 16 upstream of the air preheater 8'and bypasses the air preheater 8'is connected to the primary air blower 5 '.
A gas cooler bypass duct 22 connecting the upstream and downstream positions of the gas cooler 9 is provided in the middle of the boiler exhaust gas duct 17 connected to the upstream primary air duct 15.

【0008】尚、図中、26〜32は前記各ダクトを開
閉可能なダンパである。
In the figure, 26 to 32 are dampers that can open and close the ducts.

【0009】ボイラ1のみを駆動する、いわゆる汽力単
独運転時には、ダンパ28,29,30が閉じ、ガスタ
ービン2が切り離された状態であり、またダンパ31が
閉じ且つダンパ32が開かれ、この状態で、押込通風機
6により二次空気ダクト16内に圧送された空気は、空
気予熱器8’でボイラ1からの排ガスにより加熱された
後、そのまま二次空気ダクト16内を流れて燃焼用の二
次空気としてボイラ1へ供給されると共に、そのうちの
一部が一次空気ダクト15側へ分岐し一次通風機5を経
て燃料搬送用の一次空気としてミル4へ導入され、微粉
炭を伴って燃料管14からボイラ1へ供給され、微粉炭
の燃焼が行われる。
During the so-called steam power alone operation in which only the boiler 1 is driven, the dampers 28, 29, 30 are closed and the gas turbine 2 is disconnected, and the damper 31 is closed and the damper 32 is opened. Then, the air pressure-fed by the forced draft fan 6 into the secondary air duct 16 is heated by the exhaust gas from the boiler 1 in the air preheater 8 ′ and then flows through the secondary air duct 16 as it is for combustion. While being supplied to the boiler 1 as secondary air, a part of it is branched to the side of the primary air duct 15 and is introduced into the mill 4 as primary air for fuel transportation through the primary air blower 5 and is accompanied by pulverized coal and fuel. The pulverized coal is burned by being supplied from the pipe 14 to the boiler 1.

【0010】前記微粉炭の燃焼後の排ガスは、ボイラ排
ガスダクト17からガスクーラバイパスダクト22を流
れ、ガスクーラ9を迂回して空気予熱器8’へ導入さ
れ、該空気予熱器8’で前記押込通風機6から圧送され
る空気と熱交換を行った後、図示していない電気集塵機
を介して煙突から排出される。
The exhaust gas after combustion of the pulverized coal flows from the boiler exhaust gas duct 17 through the gas cooler bypass duct 22, bypasses the gas cooler 9 and is introduced into the air preheater 8 ', and the forced draft is blown by the air preheater 8'. After exchanging heat with the air pressure-fed from the machine 6, the air is discharged from the chimney via an electric dust collector (not shown).

【0011】ここで、前記ミル4内で粉砕される石炭中
の水分量が少なく、一次空気の温度をあまり高める必要
がない場合には、空気予熱器バイパスダクト21のダン
パ26の開度を調節することにより空気予熱器8’で加
熱される前の空気の一部が一次空気ダクト15へ導か
れ、一次空気の温度調節が行われる。
Here, when the amount of water in the coal pulverized in the mill 4 is small and it is not necessary to raise the temperature of the primary air so much, the opening degree of the damper 26 of the air preheater bypass duct 21 is adjusted. By doing so, a part of the air before being heated by the air preheater 8 ′ is guided to the primary air duct 15, and the temperature of the primary air is adjusted.

【0012】一方、ボイラ1とガスタービン2とを同時
に駆動する、いわゆるコンバインド運転時には、ダンパ
32が閉じ且つダンパ31が開かれ、この状態で、押込
通風機6により二次空気ダクト16内に圧送された空気
が、空気予熱器8’でボイラ1からの排ガスにより加熱
された後、そのまま二次空気ダクト16内を流れて燃焼
用の二次空気としてボイラ1へ供給される際、該二次空
気にガスタービン2からの排気が排気導入ダクト18を
介して混入される。
On the other hand, at the time of so-called combined operation in which the boiler 1 and the gas turbine 2 are simultaneously driven, the damper 32 is closed and the damper 31 is opened. In this state, the forced draft fan 6 pressure-feeds the secondary air duct 16 into the secondary air duct 16. When the generated air is heated by the exhaust gas from the boiler 1 in the air preheater 8 ′ and then flows through the secondary air duct 16 as it is to be supplied to the boiler 1 as secondary air for combustion, the secondary air Exhaust gas from the gas turbine 2 is mixed into air through the exhaust gas introduction duct 18.

【0013】同時に、前記空気予熱器8’を通過した空
気の一部が一次空気ダクト15側へ分岐し一次通風機5
を経て燃料搬送用の一次空気としてミル4へ導入され、
微粉炭を伴って燃料管14からボイラ1へ供給され、微
粉炭の燃焼が行われる。
At the same time, a part of the air that has passed through the air preheater 8'is branched to the side of the primary air duct 15 and the primary fan 5 is blown.
Is introduced into the mill 4 as primary air for fuel transfer via
The pulverized coal is supplied from the fuel pipe 14 to the boiler 1 and is burned.

【0014】前記微粉炭の燃焼後の排ガスは、ボイラ排
ガスダクト17を流れ、ガスクーラ9を通過する際、ボ
イラ1へ送給される給水に熱を奪われて冷却され、この
後、空気予熱器8’へ導入され、該空気予熱器8’で前
記押込通風機6から圧送される空気と熱交換を行った
後、図示していない電気集塵機を介して煙突から排出さ
れる。
The exhaust gas after combustion of the pulverized coal flows through the boiler exhaust gas duct 17 and, when passing through the gas cooler 9, is deprived of heat by the feed water supplied to the boiler 1 and cooled, and thereafter, the air preheater. After being introduced into the air preheater 8 ', heat is exchanged with the air fed under pressure from the forced draft fan 6'in the air preheater 8', and then discharged from the chimney via an electric dust collector (not shown).

【0015】ここで、前記ミル4内で粉砕される石炭中
の水分量が少なく、一次空気の温度をあまり高める必要
がない場合には、空気予熱器バイパスダクト21のダン
パ26の開度を調節することにより空気予熱器8’で加
熱される前の空気の一部が一次空気ダクト15へ導か
れ、一次空気の温度調節が行われ、又、前記石炭中の水
分量が非常に多く一次空気の温度を更に高める必要があ
る場合には、前記ダンパ26が閉じ、排気導入分岐ダク
ト19のダンパ29の開度が大となり、ガスタービン2
からの排気が前記一次空気に混入され、該一次空気の温
度が高められる。
Here, when the amount of water in the coal pulverized in the mill 4 is small and it is not necessary to raise the temperature of the primary air so much, the opening degree of the damper 26 of the air preheater bypass duct 21 is adjusted. By doing so, a part of the air before being heated by the air preheater 8 ′ is guided to the primary air duct 15, the temperature of the primary air is adjusted, and the amount of water in the coal is very large and the primary air is When it is necessary to further raise the temperature of the gas turbine 2, the damper 26 is closed and the opening degree of the damper 29 of the exhaust introduction branch duct 19 is increased, and the gas turbine 2
The exhaust gas from the air is mixed with the primary air to raise the temperature of the primary air.

【0016】[0016]

【発明が解決しようとする課題】しかしながら、前述の
如き石炭焚排気再燃コンバインドサイクルプラントで
は、コンバインド運転時にミル4内で粉砕される石炭中
の水分量が多い場合、一次空気にガスタービン2からの
排気が使用されるため、一次空気の酸素濃度が下がり、
燃焼安定性に欠けるという問題を有していた。
However, in the coal-fired exhaust gas re-combustion combined cycle plant as described above, when the amount of water in the coal pulverized in the mill 4 during the combined operation is large, the primary air from the gas turbine 2 is discharged. Since the exhaust gas is used, the oxygen concentration of the primary air decreases,
It had a problem of lacking combustion stability.

【0017】又、一次通風機5を空気予熱器8’の下流
側即ち高温側に設置してあるため、一次通風機5を通過
する一次空気の体積流量が増大し、ミル4が複数台設け
られる場合にはそれと同数の一次通風機5が必要とな
り、設備の複雑化並びに設備費の増加につながると共
に、消費電力も増大していた。
Further, since the primary air blower 5 is installed on the downstream side of the air preheater 8 ', that is, on the high temperature side, the volumetric flow rate of the primary air passing through the primary air blower 5 increases, and a plurality of mills 4 are provided. In that case, the same number of primary ventilators 5 as that is required, which leads to complication of equipment and an increase in equipment cost, and also increases power consumption.

【0018】更に又、汽力単独運転時にはガスクーラ9
を使用しないことから空気予熱器8’の排ガス入口温度
が高く空気入口温度との差が大きいのに対し、コンバイ
ンド運転時にはガスクーラ9を使用することから空気予
熱器8’の排ガス入口温度が低く空気入口温度との差が
小さくなるため、汽力単独運転とコンバインド運転の切
り換えに伴って空気予熱器8’に生ずる熱歪が非常に大
きくなり、空気予熱器8’のリーク率が高くなるという
不具合も生じていた。
Furthermore, the gas cooler 9 is used when the steam power is independently operated.
Since the exhaust gas inlet temperature of the air preheater 8'is high and the difference from the air inlet temperature is large because it is not used, the exhaust gas inlet temperature of the air preheater 8'is low because the gas cooler 9 is used during combined operation. Since the difference with the inlet temperature becomes small, the thermal strain generated in the air preheater 8 ′ accompanying the switching between the steam power single operation and the combined operation becomes very large, and the leak rate of the air preheater 8 ′ also becomes high. It was happening.

【0019】本発明は、斯かる実情に鑑み、燃焼安定性
に優れ、設備の簡素化並びに設備費低減を図り得ると共
に消費電力を削減し得、空気予熱器のリーク率低下を図
り得る石炭焚排気再燃コンバインドサイクルプラントを
提供しようとするものである。
In view of the above situation, the present invention is a coal-fired fuel which has excellent combustion stability, simplifies the equipment, reduces the equipment cost, reduces the power consumption, and reduces the leak rate of the air preheater. The present invention aims to provide an exhaust gas recombustion combined cycle plant.

【0020】[0020]

【課題を解決するための手段】本発明は、ボイラに、燃
料としての微粉炭を供給するための燃料管と、燃焼用の
二次空気を供給するための二次空気ダクトと、燃焼排ガ
スを排出するためのボイラ排ガスダクトとを接続し、前
記燃料管に石炭粉砕用のミルを接続すると共に、該ミル
に燃料搬送用の一次空気を供給するための一次空気ダク
トを接続し、該一次空気ダクト並びに二次空気ダクト途
中に、ボイラ排ガスダクトから分岐せしめたボイラ排ガ
ス分岐ダクト内を流れる排ガスの熱により一次空気を予
熱し且つボイラ排ガスダクト内を流れる排ガスの熱によ
り二次空気を予熱するための空気予熱器を設け、該空気
予熱器より上流側の一次空気ダクトに一次通風機を、前
記空気予熱器より上流側の二次空気ダクトに押込通風機
を夫々接続し、前記空気予熱器の上下流位置の一次空気
ダクトを結ぶ空気予熱器バイパスダクトを設け、前記押
込通風機と空気予熱器との間の二次空気ダクト途中に蒸
気式空気予熱器を設け、前記空気予熱器より上流側のボ
イラ排ガスダクト途中に、ボイラへ送給される給水を加
熱し且つ排ガスを冷却するためのガスクーラを設け、前
記ガスクーラの上下流位置のボイラ排ガスダクトを結ぶ
ガスクーラバイパスダクトを設け、前記空気予熱器より
下流側の二次空気ダクト途中に、ガスタービンの排気を
導入するための排気導入ダクトを接続し、該排気導入ダ
クトから分岐し且つボイラをバイパスするボイラバイパ
ス排気ダクトを前記ガスクーラより上流側のボイラ排ガ
スダクト途中に接続したことを特徴とする石炭焚排気再
燃コンバインドサイクルプラントにかかるものである。
The present invention provides a boiler with a fuel pipe for supplying pulverized coal as fuel, a secondary air duct for supplying secondary air for combustion, and a combustion exhaust gas. A boiler exhaust gas duct for discharging is connected, a mill for coal crushing is connected to the fuel pipe, and a primary air duct for supplying primary air for fuel transportation to the mill is connected to the primary air. To preheat the primary air with the heat of the exhaust gas flowing in the boiler exhaust gas branch duct branched from the boiler exhaust gas duct in the middle of the duct and the secondary air duct, and to preheat the secondary air with the heat of the exhaust gas flowing in the boiler exhaust gas duct. Of the air preheater, a primary air blower is connected to the primary air duct upstream of the air preheater, and a forced draft fan is connected to the secondary air duct upstream of the air preheater. An air preheater bypass duct that connects the primary air ducts at upstream and downstream positions of the air preheater is provided, and a steam type air preheater is provided in the middle of the secondary air duct between the forced draft fan and the air preheater, and the air preheater is used. In the middle of the boiler exhaust gas duct on the upstream side of the reactor, a gas cooler for heating the feed water fed to the boiler and cooling the exhaust gas is provided, and a gas cooler bypass duct that connects the boiler exhaust gas ducts at the upstream and downstream positions of the gas cooler is provided, A boiler bypass exhaust duct, which is connected to an exhaust introduction duct for introducing exhaust gas of a gas turbine and is branched from the exhaust introduction duct and bypasses the boiler, is connected to the gas cooler in the middle of the secondary air duct downstream of the air preheater. A coal-fired exhaust gas re-combustion combined cycle plant characterized by being connected to the boiler exhaust gas duct on the upstream side It is hunt thing.

【0021】又、前記石炭焚排気再燃コンバインドサイ
クルプラントにおいて、空気予熱器バイパスダクトの分
岐位置と空気予熱器との間における一次空気ダクト途中
に蒸気式空気予熱器を設け、ボイラバイパス排気ダクト
の分岐位置より上流側の排気導入ダクト途中に、ボイラ
へ送給される給水を加熱し且つガスタービンの排気を冷
却するためのガスクーラを設け、ボイラバイパス排気ダ
クトの接続位置より下流側で且つガスクーラバイパスダ
クト及びボイラ排ガス分岐ダクトの分岐位置より上流側
のボイラ排ガスダクト途中に脱硝装置を設け、ガスクー
ラとガスクーラバイパスダクトの接続位置との間のボイ
ラ排ガスダクト途中から分岐し且つ空気予熱器より上流
側のボイラ排ガス分岐ダクト途中に接続されるボイラ排
ガス分岐補助ダクトを形成してもよい。
In the coal-fired exhaust gas re-combustion combined cycle plant, a steam type air preheater is provided in the middle of the primary air duct between the branch position of the air preheater bypass duct and the air preheater to branch the boiler bypass exhaust duct. A gas cooler for heating the feed water sent to the boiler and cooling the exhaust gas of the gas turbine is provided in the middle of the exhaust introduction duct upstream of the position, and the gas cooler bypass duct is downstream from the connection position of the boiler bypass exhaust duct. Also, a denitration device is installed in the boiler exhaust gas duct upstream of the branch position of the boiler exhaust gas branch duct, and the boiler is branched from the boiler exhaust gas duct midway between the gas cooler and the connection position of the gas cooler bypass duct and upstream of the air preheater. Boiler exhaust gas branch auxiliary duct connected in the middle of the exhaust gas branch duct It may be formed.

【0022】[0022]

【作用】従って、汽力単独運転時には、押込通風機によ
り二次空気ダクト内に圧送された空気が、蒸気式空気予
熱器により予熱されてから空気予熱器でボイラからの排
ガスにより加熱された後、二次空気ダクト内を流れて燃
焼用の二次空気としてボイラへ供給されると共に、一次
通風機により一次空気ダクト内に圧送された空気が、空
気予熱器でボイラ排ガス分岐ダクト内を流れる排ガスに
より加熱された後、燃料搬送用の一次空気としてミルへ
導入され、微粉炭を伴って燃料管からボイラへ供給さ
れ、微粉炭の燃焼が行われ、前記微粉炭の燃焼後の排ガ
スの一部は、ボイラ排ガスダクトからガスクーラバイパ
スダクトを流れ、ガスクーラを迂回して空気予熱器へ導
入され、該空気予熱器において前記押込通風機から圧送
され蒸気式空気予熱器を通過して予熱された空気と熱交
換を行い、又、それ以外の排ガスは、ボイラ排ガスダク
トからボイラ排ガス分岐ダクトへ分岐し、空気予熱器へ
導入され、該空気予熱器において前記一次通風機から圧
送された空気と熱交換を行い、ここで、前記ミル内で粉
砕される石炭中の水分量が少なく、一次空気の温度をあ
まり高める必要がない場合には、空気予熱器で加熱され
る前の空気の一部が空気予熱器バイパスダクトを介して
ミルへ導かれ、一次空気の温度調節が行われる。
[Operation] Therefore, during the steam power alone operation, after the air forced into the secondary air duct by the forced draft fan is preheated by the steam type air preheater and then heated by the exhaust gas from the boiler by the air preheater, The air that flows in the secondary air duct is supplied to the boiler as secondary air for combustion, and the air that has been pressure-fed into the primary air duct by the primary air blower is the exhaust gas that flows in the boiler exhaust gas branch duct in the air preheater. After being heated, it is introduced into the mill as primary air for fuel transportation, is supplied from the fuel pipe to the boiler with pulverized coal, the pulverized coal is burned, and part of the exhaust gas after combustion of the pulverized coal is , Flows from the boiler exhaust gas duct through the gas cooler bypass duct, bypasses the gas cooler and is introduced into the air preheater, and the air preheater is pressure-fed from the forced draft fan in the air preheater. Through which heat is exchanged with the preheated air, and the exhaust gas other than that is branched from the boiler exhaust gas duct to the boiler exhaust gas branch duct and introduced into the air preheater, and in the air preheater, the primary blower is introduced. Heat is exchanged with the air pumped from, where the amount of water in the coal crushed in the mill is small, and when the temperature of the primary air does not need to be raised too much, it is heated with an air preheater. A portion of the previous air is introduced into the mill via the air preheater bypass duct and the temperature of the primary air is adjusted.

【0023】一方、コンバインド運転時には、押込通風
機により二次空気ダクト内に圧送された空気は、蒸気式
空気予熱器を通過するだけで予熱されずに空気予熱器で
ボイラからの排ガスにより加熱された後、二次空気ダク
ト内を流れて燃焼用の二次空気としてボイラへ供給され
る際、該二次空気にガスタービンからの排気が排気導入
ダクトを介して混入され、同時に、一次通風機により一
次空気ダクト内に圧送された空気は、空気予熱器でボイ
ラ排ガス分岐ダクト内を流れる排ガスにより加熱された
後、燃料搬送用の一次空気としてミルへ導入され、微粉
炭を伴って燃料管からボイラへ供給され、微粉炭の燃焼
が行われ、前記微粉炭の燃焼後の排ガスの一部は、ボイ
ラ排ガスダクトを流れ、ガスクーラを通過する際、ボイ
ラへ送給される給水に熱を奪われて冷却され、この後、
前記空気予熱器へ導入され、該空気予熱器において前記
押込通風機から圧送され蒸気式空気予熱器を通過するだ
けで予熱されていない空気と熱交換を行い、又、それ以
外の排ガスは、ガスクーラ上流側の高温部ボイラ排ガス
ダクトからボイラ排ガス分岐ダクトへ分岐し、空気予熱
器へ導入され、該空気予熱器において前記一次通風機か
ら圧送された空気と熱交換を行い、ここで、前記ミル内
で粉砕される石炭中の水分量が少なく、一次空気の温度
をあまり高める必要がない場合には、空気予熱器で加熱
される前の空気の一部が空気予熱器バイパスダクトを介
してミルへ導かれ、一次空気の温度調節が行われ、又、
前記石炭中の水分量が非常に多く一次空気の温度を更に
高める必要がある場合には、ボイラバイパス排気ダクト
を介してガスタービンの排気の一部をボイラ排ガスダク
トへ導くことにより、ボイラ排ガス分岐ダクト内を流れ
空気予熱器へ導入される排ガスの温度が高められる。
On the other hand, during the combined operation, the air forced into the secondary air duct by the forced draft fan is not preheated only by passing through the steam type air preheater but is heated by the exhaust gas from the boiler in the air preheater. After that, when it flows in the secondary air duct and is supplied to the boiler as secondary air for combustion, the exhaust gas from the gas turbine is mixed into the secondary air through the exhaust introduction duct, and at the same time, the primary air blower. The air pumped into the primary air duct by the air is heated by the exhaust gas flowing in the boiler exhaust gas branch duct in the air preheater and then introduced into the mill as the primary air for fuel transportation, and from the fuel pipe along with pulverized coal. The pulverized coal is supplied to the boiler and burned, and part of the exhaust gas after combustion of the pulverized coal flows through the boiler exhaust gas duct and is sent to the boiler when passing through the gas cooler. Deprived of heat is cooled, after this,
It is introduced into the air preheater, and in the air preheater, heat is exchanged with the air which is not preheated only by passing under pressure from the forced draft fan and passing through the steam type air preheater. Branches from the upstream high temperature part boiler exhaust gas duct to the boiler exhaust gas branch duct, is introduced into the air preheater, and performs heat exchange with the air pressure-fed from the primary fan in the air preheater, where the inside of the mill When the amount of water in the coal pulverized in is low and it is not necessary to raise the temperature of the primary air so much, part of the air before being heated by the air preheater is passed to the mill via the air preheater bypass duct. Is introduced, the temperature of the primary air is adjusted, and
When the amount of water in the coal is very large and it is necessary to further raise the temperature of the primary air, by guiding a part of the exhaust gas of the gas turbine to the boiler exhaust gas duct through the boiler bypass exhaust duct, the boiler exhaust gas branching is performed. The temperature of the exhaust gas flowing in the duct and introduced into the air preheater is increased.

【0024】又、脱硝装置等を付加したものの場合、汽
力単独運転時には、押込通風機により二次空気ダクト内
に圧送された空気が、蒸気式空気予熱器により予熱され
てから空気予熱器でボイラからの排ガスにより加熱され
た後、二次空気ダクト内を流れて燃焼用の二次空気とし
てボイラへ供給されると共に、一次通風機により一次空
気ダクト内に圧送された空気が、蒸気式空気予熱器によ
り予熱されてから空気予熱器でボイラ排ガス分岐ダクト
内を流れる排ガスにより加熱された後、燃料搬送用の一
次空気としてミルへ導入され、微粉炭を伴って燃料管か
らボイラへ供給され、微粉炭の燃焼が行われ、前記微粉
炭の燃焼後の排ガスは脱硝装置を通過して脱硝が行わ
れ、そのうちの一部は、ボイラ排ガスダクトからガスク
ーラバイパスダクトを流れ、ガスクーラを迂回して空気
予熱器へ導入され、該空気予熱器において前記押込通風
機から圧送され蒸気式空気予熱器を通過して予熱された
空気と熱交換を行い、又、それ以外の排ガスは、ボイラ
排ガスダクトからボイラ排ガス分岐ダクトへ分岐し、空
気予熱器へ導入され、該空気予熱器において前記一次通
風機から圧送された空気と熱交換を行い、ここで、前記
ミル内で粉砕される石炭中の水分量が少なく、一次空気
の温度をあまり高める必要がない場合には、空気予熱器
で加熱される前の空気の一部が空気予熱器バイパスダク
トを介してミルへ導かれ、一次空気の温度調節が行われ
る。
Further, in the case of adding a denitration device etc., in the steam power independent operation, the air pressure-fed into the secondary air duct by the forced draft fan is preheated by the steam type air preheater and then the air preheater is used. After being heated by the exhaust gas from the air, it flows in the secondary air duct and is supplied to the boiler as secondary air for combustion, and the air that is pressure-fed by the primary air blower into the primary air duct is steam-type air preheat. After being preheated by the furnace, it is heated by the exhaust gas flowing in the boiler exhaust gas branch duct by the air preheater, then introduced into the mill as primary air for fuel transportation, and is supplied to the boiler from the fuel pipe together with pulverized coal, The charcoal is burned, and the exhaust gas after burning the pulverized coal passes through a denitration device to be denitrified, and a part of it is discharged from the boiler exhaust gas duct to the gas cooler bypass duct. Flow, bypassing the gas cooler and introduced into the air preheater, where heat is exchanged with the preheated air that has been pressure-fed from the forced draft fan in the air preheater and passed through the steam air preheater, and The exhaust gas is branched from the boiler exhaust gas duct to the boiler exhaust gas branch duct, introduced into the air preheater, and exchanges heat with the air pressure-fed from the primary fan in the air preheater, where it is pulverized in the mill. When the amount of water in the coal is low and it is not necessary to raise the temperature of the primary air so much, a part of the air before being heated by the air preheater is introduced to the mill through the air preheater bypass duct. The temperature of the primary air is adjusted.

【0025】一方、コンバインド運転時には、押込通風
機により二次空気ダクト内に圧送された空気は、蒸気式
空気予熱器を通過するだけで予熱されずに空気予熱器で
ボイラからの排ガスにより加熱された後、二次空気ダク
ト内を流れて燃焼用の二次空気としてボイラへ供給され
る際、ガスタービンから排出されガスクーラでボイラへ
送給される給水に熱を奪われて冷却された排気が排気導
入ダクトを介して前記二次空気に混入され、同時に、一
次通風機により一次空気ダクト内に圧送された空気は、
蒸気式空気予熱器を通過するだけで予熱されずに空気予
熱器でボイラ排ガス分岐ダクト内を流れる排ガスにより
加熱された後、燃料搬送用の一次空気としてミルへ導入
され、微粉炭を伴って燃料管からボイラへ供給され、微
粉炭の燃焼が行われ、前記微粉炭の燃焼後の排ガスは脱
硝装置を通過して脱硝が行われ、ボイラ排ガスダクトを
流れ、ガスクーラを通過する際、ボイラへ送給される給
水に熱を奪われて冷却され、この後、前記排ガスの一部
が前記空気予熱器へ導入され、該次空気予熱器において
前記押込通風機から圧送され蒸気式空気予熱器を通過す
るだけで予熱されていない空気と熱交換を行い、又、そ
れ以外の排ガスは、ボイラ排ガスダクトからボイラ排ガ
ス分岐補助ダクトへ分岐し、空気予熱器へ導入され、該
空気予熱器において前記一次通風機から圧送された空気
と熱交換を行う。
On the other hand, during the combined operation, the air pressure-fed into the secondary air duct by the forced draft fan is not preheated only by passing through the steam type air preheater but is heated by the exhaust gas from the boiler in the air preheater. After that, when the air flows in the secondary air duct and is supplied to the boiler as secondary air for combustion, heat is taken from the water supplied from the gas turbine and sent to the boiler by the gas cooler. Air mixed into the secondary air through the exhaust introduction duct, at the same time, the air pressure-fed into the primary air duct by the primary fan,
After passing through the steam-type air preheater and not being preheated, it is heated by the exhaust gas flowing in the boiler exhaust gas branch duct in the air preheater and then introduced into the mill as the primary air for fuel transportation, and the fuel is accompanied by pulverized coal. It is supplied to the boiler from a pipe, the pulverized coal is burned, and the exhaust gas after combustion of the pulverized coal passes through a denitration device for denitration, flows through the boiler exhaust gas duct, and is sent to the boiler when passing through the gas cooler. It is cooled by the heat supplied to the supplied water, after which part of the exhaust gas is introduced into the air preheater, and in the next air preheater, it is pressure-fed from the forced draft fan and passes through the steam air preheater. Heat exchange with the unpreheated air, and the other exhaust gas is branched from the boiler exhaust gas duct to the boiler exhaust gas branch auxiliary duct, introduced into the air preheater, and then placed in the air preheater. Performing heat exchange with air pumped from the primary ventilator.

【0026】ここで、前記ミル内で粉砕される石炭中の
水分量が少なく、一次空気の温度をあまり高める必要が
ない場合には、空気予熱器で加熱される前の空気の一部
が空気予熱器バイパスダクトを介してミルへ導かれ、一
次空気の温度調節が行われ、又、前記石炭中の水分量が
多く一次空気の温度を高める必要がある場合には、一次
通風機から圧送された空気が蒸気式空気予熱器で予熱さ
れた後空気予熱器へ導かれると共に、ガスクーラを通過
する前の高温の排ガスの一部がボイラ排ガス分岐ダクト
を介して空気予熱器へ導かれ、前記石炭中の水分量が更
に多く一次空気の温度を更に高める必要がある場合に
は、ガスタービンの排気の一部をボイラバイパス排気ダ
クトを介してボイラ排ガスダクトへ導くことにより、ボ
イラ排ガス分岐ダクト内を流れ空気予熱器へ導入される
排ガスの温度が高められ、この結果、ミルへ導入される
一次空気の温度を石炭中の水分量に応じてよりきめ細か
く調整することが可能となる。
Here, when the amount of water in the coal pulverized in the mill is small and it is not necessary to raise the temperature of the primary air so much, part of the air before being heated by the air preheater is air. It is guided to the mill through the preheater bypass duct, the temperature of the primary air is adjusted, and when there is a large amount of water in the coal and it is necessary to raise the temperature of the primary air, it is pumped from the primary fan. Air is preheated by the steam air preheater and then introduced to the air preheater, and part of the hot exhaust gas before passing through the gas cooler is introduced to the air preheater via the boiler exhaust gas branch duct, and the coal When the amount of water in the air is higher and it is necessary to raise the temperature of the primary air further, a part of the gas turbine exhaust is guided to the boiler exhaust gas duct through the boiler bypass exhaust duct, so that the boiler exhaust gas branch duct The temperature of the exhaust gas is increased to be introduced to flow into the air preheater inner, this result, the temperature of the primary air introduced into the mill can be more finely adjusted according to the amount of moisture in the coal.

【0027】[0027]

【実施例】以下、本発明の実施例を図面を参照しつつ説
明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0028】図1は本発明の一実施例であって、図中、
図3と同一の符号を付した部分は同一物を表わしてお
り、ボイラ1に通ずる燃料管14に接続されたミル4
に、後述するボイラ排ガス分岐ダクト23内を流れる排
ガスの熱により一次空気を予熱するための一次空気予熱
器7が途中に設けられた一次空気ダクト15を接続し、
該一次空気ダクト15の一次空気予熱器7より上流側に
一次通風機5を設けると共に、前記一次空気予熱器7の
上下流位置を結ぶ一次空気予熱器バイパスダクト24を
設ける。
FIG. 1 shows an embodiment of the present invention.
The parts denoted by the same reference numerals as in FIG. 3 represent the same things, and the mill 4 connected to the fuel pipe 14 leading to the boiler 1
Is connected to a primary air duct 15 in which a primary air preheater 7 for preheating the primary air by the heat of exhaust gas flowing in a boiler exhaust gas branch duct 23 described later is provided,
A primary air blower 5 is provided on the upstream side of the primary air preheater 7 of the primary air duct 15, and a primary air preheater bypass duct 24 connecting the upstream and downstream positions of the primary air preheater 7 is provided.

【0029】ボイラ1に接続された二次空気ダクト16
途中に、ボイラ排ガスダクト17内を流れる排ガスの熱
により二次空気を予熱するための二次空気予熱器8を設
け、該二次空気予熱器8より上流側の二次空気ダクト1
6途中に蒸気式空気予熱器11を設けると共に、該蒸気
式空気予熱器11の上流側に押込通風機6を設ける。
Secondary air duct 16 connected to the boiler 1
A secondary air preheater 8 for preheating the secondary air with the heat of the exhaust gas flowing in the boiler exhaust gas duct 17 is provided on the way, and the secondary air duct 1 upstream of the secondary air preheater 8 is provided.
6. A steam type air preheater 11 is provided on the way, and a forced draft fan 6 is provided on the upstream side of the steam type air preheater 11.

【0030】ガスクーラ9より上流側のボイラ排ガスダ
クト17から分岐し且つ二次空気予熱器8より下流側の
ボイラ排ガスダクト17に接続されるボイラ排ガス分岐
ダクト23を設け、該ボイラ排ガス分岐ダクト23途中
に前記一次空気予熱器7を設ける。
A boiler exhaust gas branch duct 23, which branches from the boiler exhaust gas duct 17 upstream of the gas cooler 9 and is connected to the boiler exhaust gas duct 17 downstream of the secondary air preheater 8, is provided in the middle of the boiler exhaust gas branch duct 23. Is provided with the primary air preheater 7.

【0031】尚、図中、33〜36は各ダクトを開閉可
能なダンパである。
In the figure, 33 to 36 are dampers that can open and close each duct.

【0032】次に、上記実施例の作動を説明する。Next, the operation of the above embodiment will be described.

【0033】ボイラ1のみを駆動する、いわゆる汽力単
独運転時には、ダンパ31が閉じ且つダンパ32が開か
れ、この状態で、押込通風機6により二次空気ダクト1
6内に圧送された空気が、蒸気式空気予熱器11により
予熱されてから二次空気予熱器8でボイラ1からの排ガ
スにより加熱された後、二次空気ダクト16内を流れて
燃焼用の二次空気としてボイラ1へ供給されると共に、
一次通風機5により一次空気ダクト15内に圧送された
空気が、一次空気予熱器7でボイラ排ガス分岐ダクト2
3内を流れる排ガスにより加熱された後、燃料搬送用の
一次空気としてミル4へ導入され、微粉炭を伴って燃料
管14からボイラ1へ供給され、微粉炭の燃焼が行われ
る。
During the so-called steam alone operation in which only the boiler 1 is driven, the damper 31 is closed and the damper 32 is opened. In this state, the forced draft fan 6 is used to drive the secondary air duct 1
The air pressure-fed into 6 is preheated by the steam type air preheater 11 and then heated by the exhaust gas from the boiler 1 in the secondary air preheater 8 and then flows in the secondary air duct 16 for combustion. While being supplied to the boiler 1 as secondary air,
The air pressure-fed by the primary fan 5 into the primary air duct 15 is transferred to the boiler exhaust gas branch duct 2 by the primary air preheater 7.
After being heated by the exhaust gas flowing in 3, the air is introduced into the mill 4 as primary air for fuel transportation and is supplied to the boiler 1 from the fuel pipe 14 together with the pulverized coal, and the pulverized coal is burned.

【0034】前記微粉炭の燃焼後の排ガスの一部は、ボ
イラ排ガスダクト17からガスクーラバイパスダクト2
2を流れ、ガスクーラ9を迂回して二次空気予熱器8へ
導入され、該二次空気予熱器8において前記押込通風機
6から圧送され蒸気式空気予熱器11を通過して予熱さ
れた空気と熱交換を行い、又、それ以外の排ガスは、ボ
イラ排ガスダクト17からボイラ排ガス分岐ダクト23
へ分岐し、一次空気予熱器7へ導入され、該一次空気予
熱器7において前記一次通風機5から圧送された空気と
熱交換を行った後、前記ボイラ排ガスダクト17内を流
れる排ガスに合流し、図示していない電気集塵機を介し
て煙突から排出される。
Part of the exhaust gas after combustion of the pulverized coal is transferred from the boiler exhaust gas duct 17 to the gas cooler bypass duct 2
2 which flows through the gas cooler 9 and bypasses the gas cooler 9 and is introduced into the secondary air preheater 8 in which air is preheated from the forced draft fan 6 through the steam air preheater 11. Exhaust gas other than that exchanges heat from the boiler exhaust gas duct 17 to the boiler exhaust gas branch duct 23.
And is introduced into the primary air preheater 7, and after exchanging heat with the air pressure-fed from the primary air blower 5 in the primary air preheater 7, it joins the exhaust gas flowing in the boiler exhaust gas duct 17. , Is discharged from the chimney via an electric dust collector (not shown).

【0035】ここで、前記ミル4内で粉砕される石炭中
の水分量が少なく、一次空気の温度をあまり高める必要
がない場合には、一次空気予熱器バイパスダクト24の
ダンパ34の開度を調節することにより一次空気予熱器
7で加熱される前の空気の一部がミル4へ導かれ、一次
空気の温度調節が行われる。
Here, when the amount of water in the coal pulverized in the mill 4 is small and it is not necessary to raise the temperature of the primary air so much, the opening degree of the damper 34 of the primary air preheater bypass duct 24 is set. By adjusting, a part of the air before being heated by the primary air preheater 7 is guided to the mill 4, and the temperature of the primary air is adjusted.

【0036】一方、ボイラ1とガスタービン2とを同時
に駆動する、いわゆるコンバインド運転時には、ダンパ
32が閉じ且つダンパ31が開かれ、この状態で、押込
通風機6により二次空気ダクト16内に圧送された空気
は、蒸気式空気予熱器11を通過するだけで予熱されず
に二次空気予熱器8でボイラ1からの排ガスにより加熱
された後、二次空気ダクト16内を流れて燃焼用の二次
空気としてボイラ1へ供給される際、該二次空気にガス
タービン2からの排気が排気導入ダクト18を介して混
入される。
On the other hand, at the time of so-called combined operation in which the boiler 1 and the gas turbine 2 are simultaneously driven, the damper 32 is closed and the damper 31 is opened, and in this state, the forced draft fan 6 feeds the compressed air into the secondary air duct 16. The generated air is heated by the exhaust gas from the boiler 1 in the secondary air preheater 8 without passing through the steam type air preheater 11 and is not preheated, and then flows in the secondary air duct 16 for combustion. When the secondary air is supplied to the boiler 1, the exhaust air from the gas turbine 2 is mixed into the secondary air via the exhaust introduction duct 18.

【0037】同時に、一次通風機5により一次空気ダク
ト15内に圧送された空気は、一次空気予熱器7でボイ
ラ排ガス分岐ダクト23内を流れる排ガスにより加熱さ
れた後、燃料搬送用の一次空気としてミル4へ導入さ
れ、微粉炭を伴って燃料管14からボイラ1へ供給さ
れ、微粉炭の燃焼が行われる。
At the same time, the air pressure-fed by the primary fan 5 into the primary air duct 15 is heated by the exhaust gas flowing in the boiler exhaust gas branch duct 23 by the primary air preheater 7 and then used as primary air for fuel transportation. The pulverized coal is introduced into the mill 4 and is supplied from the fuel pipe 14 to the boiler 1 together with the pulverized coal, and the pulverized coal is burned.

【0038】前記微粉炭の燃焼後の排ガスの一部は、ボ
イラ排ガスダクト17を流れ、ガスクーラ9を通過する
際、ボイラ1へ送給される給水に熱を奪われて冷却さ
れ、この後、前記二次空気予熱器8へ導入され、該二次
空気予熱器8において前記押込通風機6から圧送され蒸
気式空気予熱器11を通過するだけで予熱されていない
空気と熱交換を行い、又、それ以外の排ガスは、ボイラ
排ガスダクト17からボイラ排ガス分岐ダクト23へ分
岐し、一次空気予熱器7へ導入され、該一次空気予熱器
7において前記一次通風機5から圧送された空気と熱交
換を行った後、前記ボイラ排ガスダクト17内を流れる
排ガスに合流し、図示していない電気集塵機を介して煙
突から排出される。
A part of the exhaust gas after combustion of the pulverized coal flows through the boiler exhaust gas duct 17 and, when passing through the gas cooler 9, the water supplied to the boiler 1 removes heat and is cooled. It is introduced into the secondary air preheater 8 and in the secondary air preheater 8, heat is exchanged with the air that is not preheated only by passing under pressure from the forced draft fan 6 and passing through the steam type air preheater 11. , The other exhaust gas branches from the boiler exhaust gas duct 17 to the boiler exhaust gas branch duct 23, is introduced into the primary air preheater 7, and exchanges heat with the air pressure-fed from the primary fan 5 in the primary air preheater 7. After that, it joins the exhaust gas flowing in the boiler exhaust gas duct 17, and is discharged from the chimney via an electric dust collector (not shown).

【0039】ここで、前記ミル4内で粉砕される石炭中
の水分量が少なく、一次空気の温度をあまり高める必要
がない場合には、一次空気予熱器バイパスダクト24の
ダンパ34の開度を調節することにより一次空気予熱器
7で加熱される前の空気の一部がミル4へ導かれ、一次
空気の温度調節が行われ、又、前記石炭中の水分量が非
常に多く一次空気の温度を更に高める必要がある場合に
は、前記ダンパ34を閉じ且つボイラバイパス排気ダク
ト20のダンパ30を開きガスタービン2の排気の一部
をボイラ排ガスダクト17へ導くことにより、ボイラ排
ガス分岐ダクト23内を流れ一次空気予熱器7へ導入さ
れる排ガスの温度が高められる。
Here, when the amount of water in the coal pulverized in the mill 4 is small and it is not necessary to raise the temperature of the primary air so much, the opening degree of the damper 34 of the primary air preheater bypass duct 24 is adjusted. By adjusting, a part of the air before being heated by the primary air preheater 7 is guided to the mill 4, the temperature of the primary air is adjusted, and the amount of water in the coal is very large, When it is necessary to raise the temperature further, the damper 34 is closed and the damper 30 of the boiler bypass exhaust duct 20 is opened to guide a part of the exhaust gas of the gas turbine 2 to the boiler exhaust gas duct 17, thereby making the boiler exhaust gas branch duct 23 The temperature of the exhaust gas flowing inside and introduced into the primary air preheater 7 is increased.

【0040】本実施例においては、コンバインド運転時
にミル4内で粉砕される石炭中の水分量が多い場合に
も、一次空気としてガスタービン2からの排気が直接使
用されるのではなく常に新鮮な空気が用いられるため、
一次空気の酸素濃度が下がるようなことはなく、燃焼安
定性が高い。
In this embodiment, even when the amount of water in the coal crushed in the mill 4 during the combined operation is large, the exhaust gas from the gas turbine 2 is not directly used as the primary air but is always fresh. Because air is used,
The oxygen concentration of the primary air does not decrease, and the combustion stability is high.

【0041】又、一次通風機5を一次空気予熱器7の上
流側即ち低温側に設置してあるため、一次通風機5を通
過する一次空気の体積流量が増大せず、ミル4が複数台
設けられる場合にもそれと同数の一次通風機5は不要と
なり必要最低限(一台か二台)で済み、設備の簡素化並
びに設備費低減に役立つと共に、消費電力も削減可能と
なる。
Further, since the primary air blower 5 is installed upstream of the primary air preheater 7, that is, on the low temperature side, the volumetric flow rate of the primary air passing through the primary air blower 5 does not increase, and a plurality of mills 4 are provided. Even when provided, the same number of primary fans 5 are not required, and the required minimum number (one or two) is sufficient, which simplifies the equipment and reduces the equipment cost, and the power consumption can be reduced.

【0042】更に又、汽力単独運転時にはガスクーラ9
を使用しないことから二次空気予熱器8の排ガス入口温
度が高くなるが、二次空気予熱器8に導入される二次空
気は蒸気式空気予熱器11により予熱され、二次空気予
熱器8の空気入口温度が高められているため、二次空気
予熱器8の排ガス入口温度と空気入口温度との差が小さ
くなり、汽力単独運転とコンバインド運転の切り換えに
伴って二次空気予熱器8に生ずる熱歪が小さくなり、二
次空気予熱器8のリーク率を低下させることができる。
尚、汽力単独運転時の場合コンバインド運転時に比べ二
次空気予熱器8を通過する空気量が増加するので、蒸気
式空気予熱器11を使用して二次空気予熱器8の空気入
口温度を高めても、二次空気予熱器8の排ガス出口温度
はコンバインド運転時と同等とすることができる。
Furthermore, the gas cooler 9 is used when the steam power is independently operated.
However, since the exhaust gas inlet temperature of the secondary air preheater 8 becomes high, the secondary air introduced into the secondary air preheater 8 is preheated by the steam type air preheater 11 and the secondary air preheater 8 Since the air inlet temperature of the secondary air preheater 8 is increased, the difference between the exhaust gas inlet temperature of the secondary air preheater 8 and the air inlet temperature becomes small, and the secondary air preheater 8 is switched to the secondary air preheater 8 with the switching between the steam alone operation and the combined operation. The generated thermal strain is reduced, and the leak rate of the secondary air preheater 8 can be reduced.
In addition, since the amount of air passing through the secondary air preheater 8 in the case of steam power alone operation is larger than that in the case of combined operation, the steam inlet air preheater 11 is used to increase the air inlet temperature of the secondary air preheater 8. However, the exhaust gas outlet temperature of the secondary air preheater 8 can be made equal to that in the combined operation.

【0043】図2は本発明の他の実施例を示すもので、
図中、図1と同一の符号を付した部分は同一物を表わし
ており、一次空気予熱器バイパスダクト24の分岐位置
と一次空気予熱器7との間における一次空気ダクト15
途中に蒸気式空気予熱器12を設け、ボイラバイパス排
気ダクト20の分岐位置より上流側の排気導入ダクト1
8途中に、ボイラ1へ送給される給水を加熱し且つガス
タービン2の排気を冷却するためのガスクーラ10を設
け、ボイラバイパス排気ダクト20の接続位置より下流
側で且つガスクーラバイパスダクト22及びボイラ排ガ
ス分岐ダクト23の分岐位置より上流側のボイラ排ガス
ダクト17途中に脱硝装置13を設け、ガスクーラ9と
ガスクーラバイパスダクト22の接続位置との間のボイ
ラ排ガスダクト17途中から分岐し且つ一次空気予熱器
7より上流側のボイラ排ガス分岐ダクト23途中に接続
されるボイラ排ガス分岐補助ダクト25を形成し、該ボ
イラ排ガス分岐補助ダクト25途中にダンパ38を設け
ると共に、前記ボイラ排ガス分岐補助ダクト25の接続
位置より上流側のボイラ排ガス分岐ダクト23途中にダ
ンパ37を設けたものである。
FIG. 2 shows another embodiment of the present invention.
In the figure, the parts denoted by the same reference numerals as in FIG. 1 represent the same things, and the primary air duct 15 between the branch position of the primary air preheater bypass duct 24 and the primary air preheater 7.
A steam type air preheater 12 is provided on the way, and the exhaust gas introduction duct 1 upstream of the branch position of the boiler bypass exhaust duct 20 is provided.
A gas cooler 10 for heating the feed water sent to the boiler 1 and cooling the exhaust gas of the gas turbine 2 is provided in the middle of 8, and is located on the downstream side of the connection position of the boiler bypass exhaust duct 20 and the gas cooler bypass duct 22 and the boiler. A denitration device 13 is provided in the middle of the boiler exhaust gas duct 17 upstream of the branch position of the exhaust gas branch duct 23 to branch from the middle of the boiler exhaust gas duct 17 between the connection position of the gas cooler 9 and the gas cooler bypass duct 22 and to the primary air preheater. 7. A boiler exhaust gas branch auxiliary duct 25 connected to the boiler exhaust gas branch duct 23 upstream of 7 is formed, a damper 38 is provided in the boiler exhaust gas branch auxiliary duct 25, and a connection position of the boiler exhaust gas branch auxiliary duct 25. A damper 37 is provided in the middle of the boiler exhaust gas branch duct 23 on the upstream side. Than it is.

【0044】図2に示す実施例の場合、汽力単独運転時
には、ダンパ31,38が閉じ且つダンパ32,37が
開かれ、この状態で、押込通風機6により二次空気ダク
ト16内に圧送された空気が、蒸気式空気予熱器11に
より予熱されてから二次空気予熱器8でボイラ1からの
排ガスにより加熱された後、二次空気ダクト16内を流
れて燃焼用の二次空気としてボイラ1へ供給されると共
に、一次通風機5により一次空気ダクト15内に圧送さ
れた空気が、蒸気式空気予熱器12により予熱されてか
ら一次空気予熱器7でボイラ排ガス分岐ダクト23内を
流れる排ガスにより加熱された後、燃料搬送用の一次空
気としてミル4へ導入され、微粉炭を伴って燃料管14
からボイラ1へ供給され、微粉炭の燃焼が行われる。
In the case of the embodiment shown in FIG. 2, the dampers 31 and 38 are closed and the dampers 32 and 37 are opened during the steam alone operation, and in this state, the forced draft fan 6 feeds the secondary air duct 16 under pressure. The air is preheated by the steam type air preheater 11 and then heated by the exhaust gas from the boiler 1 by the secondary air preheater 8 and then flows through the secondary air duct 16 to serve as secondary air for combustion as a boiler. Exhaust gas that flows into the boiler exhaust gas branch duct 23 by the primary air preheater 7 after the air that has been supplied to No. 1 and is pressure-fed by the primary air blower 5 into the primary air duct 15 is preheated by the steam air preheater 12. After being heated by the fuel pipe 14, it is introduced into the mill 4 as primary air for fuel transportation, and the fuel pipe 14 is accompanied by pulverized coal.
Is supplied to the boiler 1 and the pulverized coal is burned.

【0045】前記微粉炭の燃焼後の排ガスは脱硝装置1
3を通過して脱硝が行われ、そのうちの一部は、ボイラ
排ガスダクト17からガスクーラバイパスダクト22を
流れ、ガスクーラ9を迂回して二次空気予熱器8へ導入
され、該二次空気予熱器8において前記押込通風機6か
ら圧送され蒸気式空気予熱器11を通過して予熱された
空気と熱交換を行い、又、それ以外の排ガスは、ボイラ
排ガスダクト17からボイラ排ガス分岐ダクト23へ分
岐し、一次空気予熱器7へ導入され、該一次空気予熱器
7において前記一次通風機5から圧送された空気と熱交
換を行った後、前記ボイラ排ガスダクト17内を流れる
排ガスに合流し、図示していない電気集塵機を介して煙
突から排出される。
Exhaust gas after combustion of the pulverized coal is denitration device 1
3 through which denitration is performed, a part of which flows from the boiler exhaust gas duct 17 through the gas cooler bypass duct 22, bypasses the gas cooler 9 and is introduced into the secondary air preheater 8, and the secondary air preheater In 8, heat exchange is performed with the air that has been pressure-fed from the forced draft fan 6 and has passed through the steam type air preheater 11 and has been preheated, and the other exhaust gas is branched from the boiler exhaust gas duct 17 to the boiler exhaust gas branch duct 23. Then, after heat exchange with the air introduced into the primary air preheater 7 and being pressure-fed from the primary air blower 5 in the primary air preheater 7, it joins the exhaust gas flowing in the boiler exhaust gas duct 17, Exhaust from the chimney via an electrostatic precipitator not shown.

【0046】ここで、前記ミル4内で粉砕される石炭中
の水分量が少なく、一次空気の温度をあまり高める必要
がない場合には、一次空気予熱器バイパスダクト24の
ダンパ34の開度を調節することにより一次空気予熱器
7で加熱される前の空気の一部がミル4へ導かれ、一次
空気の温度調節が行われる。
Here, when the amount of water in the coal pulverized in the mill 4 is small and it is not necessary to raise the temperature of the primary air so much, the opening degree of the damper 34 of the primary air preheater bypass duct 24 is adjusted. By adjusting, a part of the air before being heated by the primary air preheater 7 is guided to the mill 4, and the temperature of the primary air is adjusted.

【0047】一方、コンバインド運転時には、ダンパ3
2,37が閉じ且つダンパ31,38が開かれ、この状
態で、押込通風機6により二次空気ダクト16内に圧送
された空気は、蒸気式空気予熱器11を通過するだけで
予熱されずに二次空気予熱器8でボイラ1からの排ガス
により加熱された後、二次空気ダクト16内を流れて燃
焼用の二次空気としてボイラ1へ供給される際、ガスタ
ービン2から排出されガスクーラ10でボイラ1へ送給
される給水に熱を奪われて冷却された排気が排気導入ダ
クト18を介して前記二次空気に混入される。
On the other hand, during combined operation, the damper 3
2, 37 are closed and the dampers 31, 38 are opened. In this state, the air forced into the secondary air duct 16 by the forced draft fan 6 only passes through the steam air preheater 11 and is not preheated. After being heated by the exhaust gas from the boiler 1 in the secondary air preheater 8 and then supplied to the boiler 1 as secondary air for combustion flowing in the secondary air duct 16, the gas cooler is discharged from the gas turbine 2. The exhaust gas, which is deprived of heat by the water supplied to the boiler 1 at 10 and cooled, is mixed into the secondary air through the exhaust introduction duct 18.

【0048】同時に、一次通風機5により一次空気ダク
ト15内に圧送された空気は、蒸気式空気予熱器12を
通過するだけで予熱されずに一次空気予熱器7でボイラ
排ガス分岐ダクト23内を流れる排ガスにより加熱され
た後、燃料搬送用の一次空気としてミル4へ導入され、
微粉炭を伴って燃料管14からボイラ1へ供給され、微
粉炭の燃焼が行われる。
At the same time, the air pressure-fed into the primary air duct 15 by the primary air blower 5 passes through the steam type air preheater 12 only and is not preheated. After being heated by the flowing exhaust gas, it is introduced into the mill 4 as primary air for fuel transportation,
The pulverized coal is supplied from the fuel pipe 14 to the boiler 1 and is burned.

【0049】前記微粉炭の燃焼後の排ガスは脱硝装置1
3を通過して脱硝が行われ、ボイラ排ガスダクト17を
流れ、ガスクーラ9を通過する際、ボイラ1へ送給され
る給水に熱を奪われて冷却され、この後、前記排ガスの
一部が前記二次空気予熱器8へ導入され、該二次空気予
熱器8において前記押込通風機6から圧送され蒸気式空
気予熱器11を通過するだけで予熱されていない空気と
熱交換を行い、又、それ以外の排ガスは、ボイラ排ガス
ダクト17からボイラ排ガス分岐補助ダクト25へ分岐
し、一次空気予熱器7へ導入され、該一次空気予熱器7
において前記一次通風機5から圧送された空気と熱交換
を行った後、前記ボイラ排ガスダクト17内を流れる排
ガスに合流し、図示していない電気集塵機を介して煙突
から排出される。
The exhaust gas after the combustion of the pulverized coal is the denitration device 1
3, denitration is carried out, flows through the boiler exhaust gas duct 17, and when passing through the gas cooler 9, the water supplied to the boiler 1 removes heat and is cooled. It is introduced into the secondary air preheater 8 and in the secondary air preheater 8, heat is exchanged with the air that is not preheated only by passing under pressure from the forced draft fan 6 and passing through the steam type air preheater 11. The other exhaust gas branches from the boiler exhaust gas duct 17 to the boiler exhaust gas branching auxiliary duct 25 and is introduced into the primary air preheater 7, and the primary air preheater 7
In the above, the heat is exchanged with the air pressure-fed from the primary blower 5, and then the heat is exchanged with the exhaust gas flowing in the boiler exhaust gas duct 17, and is discharged from the chimney via an electric dust collector (not shown).

【0050】ここで、前記ミル4内で粉砕される石炭中
の水分量が少なく、一次空気の温度をあまり高める必要
がない場合には、一次空気予熱器バイパスダクト24の
ダンパ34の開度を調節することにより一次空気予熱器
7で加熱される前の空気の一部がミル4へ導かれ、一次
空気の温度調節が行われ、又、前記石炭中の水分量が多
く一次空気の温度を高める必要がある場合には、前記ダ
ンパ34を閉じることにより一次通風機5から圧送され
た空気が蒸気式空気予熱器12で予熱された後一次空気
予熱器7へ導かれると共に、ボイラ排ガス分岐補助ダク
ト25のダンパ38を閉じ且つボイラ排ガス分岐ダクト
23のダンパ37を開くことによりガスクーラ9を通過
する前の高温の排ガスの一部がボイラ排ガス分岐ダクト
23から一次空気予熱器7へ導かれる。前記石炭中の水
分量が更に多く一次空気の温度を更に高める必要がある
場合には、ボイラバイパス排気ダクト20のダンパ30
を開きガスタービン2の排気の一部をボイラ排ガスダク
ト17へ導くことにより、ボイラ排ガス分岐ダクト23
内を流れ一次空気予熱器7へ導入される排ガスの温度が
高められる。この結果、ミル4へ導入される一次空気の
温度を石炭中の水分量に応じてよりきめ細かく調整する
ことが可能となる。
Here, when the amount of water in the coal pulverized in the mill 4 is small and it is not necessary to raise the temperature of the primary air so much, the opening degree of the damper 34 of the primary air preheater bypass duct 24 is adjusted. By adjusting, a part of the air before being heated by the primary air preheater 7 is guided to the mill 4, the temperature of the primary air is adjusted, and the amount of water in the coal is large and the temperature of the primary air is adjusted. When it is necessary to increase the temperature, the air blown from the primary blower 5 is preheated by the steam type air preheater 12 by closing the damper 34, and then the air is guided to the primary air preheater 7, and the boiler exhaust gas branching assist is also provided. By closing the damper 38 of the duct 25 and opening the damper 37 of the boiler exhaust gas branch duct 23, a part of the high-temperature exhaust gas before passing through the gas cooler 9 is transferred from the boiler exhaust gas branch duct 23 to the primary air. It is guided to the heat unit 7. When the amount of water in the coal is large and it is necessary to further raise the temperature of the primary air, the damper 30 of the boiler bypass exhaust duct 20 is used.
By opening a part of the exhaust gas of the gas turbine 2 to the boiler exhaust gas duct 17,
The temperature of the exhaust gas flowing inside and introduced into the primary air preheater 7 is increased. As a result, the temperature of the primary air introduced into the mill 4 can be adjusted more finely according to the amount of water in the coal.

【0051】図2に示す実施例においても、図1に示す
実施例の場合と同様、コンバインド運転時にミル4内で
粉砕される石炭中の水分量が多い場合にも、一次空気と
してガスタービン2からの排気が直接使用されるのでは
なく常に新鮮な空気が用いられるため、一次空気の酸素
濃度が下がるようなことはなく、燃焼安定性が高く、
又、一次通風機5を一次空気予熱器7の上流側即ち低温
側に設置してあるため、一次通風機5を通過する一次空
気の体積流量が増大せず、ミル4が複数台設けられる場
合にもそれと同数の一次通風機5は不要となり必要最低
限(一台か二台)で済み、設備の簡素化並びに設備費低
減に役立つと共に、消費電力も削減可能となり、更に
又、汽力単独運転時にはガスクーラ9を使用しないこと
から二次空気予熱器8の排ガス入口温度が高くなるが、
二次空気予熱器8に導入される二次空気は蒸気式空気予
熱器11により予熱され、二次空気予熱器8の空気入口
温度が高められているため、二次空気予熱器8の排ガス
入口温度と空気入口温度との差が小さくなり、汽力単独
運転とコンバインド運転の切り換えに伴って二次空気予
熱器8に生ずる熱歪が小さくなり、二次空気予熱器8の
リーク率を低下させることができる。
In the embodiment shown in FIG. 2, as in the embodiment shown in FIG. 1, even when the amount of water in the coal pulverized in the mill 4 during the combined operation is large, the gas turbine 2 is used as the primary air. Since the exhaust air from is not used directly but fresh air is always used, the oxygen concentration of the primary air does not decrease, the combustion stability is high,
In addition, since the primary air blower 5 is installed upstream of the primary air preheater 7, that is, on the low temperature side, the volume flow of the primary air passing through the primary air blower 5 does not increase, and a plurality of mills 4 are provided. Moreover, the same number of primary ventilators 5 is not required, and the required minimum (1 or 2) is required, which helps simplify the equipment and reduces the equipment cost, and also reduces the power consumption. Sometimes the gas cooler 9 is not used, so the exhaust gas inlet temperature of the secondary air preheater 8 rises,
The secondary air introduced into the secondary air preheater 8 is preheated by the steam type air preheater 11 and the air inlet temperature of the secondary air preheater 8 is raised, so the exhaust gas inlet of the secondary air preheater 8 is increased. The difference between the temperature and the air inlet temperature becomes small, the thermal strain generated in the secondary air preheater 8 accompanying the switching between the steam power single operation and the combined operation becomes small, and the leak rate of the secondary air preheater 8 is reduced. You can

【0052】又、図2に示す実施例の場合、仮に蒸気式
空気予熱器12を設けていないとすると、コンバインド
運転時において、石炭中の水分量が少ない場合には一次
空気予熱器7にガスクーラ9を通過した後の排ガスを導
入することから一次空気予熱器7の排ガス入口温度が低
く空気入口温度との差が小さいのに対し、石炭中の水分
量が多い場合には一次空気予熱器7にガスクーラ9を通
過する前の排ガスを導入することから一次空気予熱器7
の排ガス入口温度が高く空気入口温度との差が大きくな
るため、石炭中の水分量の変化に伴って一次空気予熱器
7に生ずる熱歪が非常に大きくなり、一次空気予熱器7
のリーク率が高まることになるが、一次空気予熱器7の
排ガス入口温度が高いときには一次空気予熱器7に導入
される一次空気を蒸気式空気予熱器12により予熱し、
一次空気予熱器7の空気入口温度を高めらているため、
一次空気予熱器7の排ガス入口温度と空気入口温度との
差が小さくなり、石炭中の水分量の変化に伴って一次空
気予熱器7に生ずる熱歪が小さくなり、一次空気予熱器
7のリーク率を低下させることができる。
Further, in the case of the embodiment shown in FIG. 2, assuming that the steam type air preheater 12 is not provided, in the combined operation, when the amount of water in the coal is small, the primary air preheater 7 is provided with a gas cooler. Since the exhaust gas after passing through No. 9 is introduced, the exhaust gas inlet temperature of the primary air preheater 7 is low and the difference from the air inlet temperature is small, whereas when the water content in the coal is large, the primary air preheater 7 Since the exhaust gas before passing through the gas cooler 9 is introduced into the primary air preheater 7
Since the exhaust gas inlet temperature of the coal is high and the difference from the air inlet temperature is large, the thermal strain generated in the primary air preheater 7 with the change in the amount of water in the coal becomes very large, and the primary air preheater 7
However, when the exhaust gas inlet temperature of the primary air preheater 7 is high, the primary air introduced into the primary air preheater 7 is preheated by the steam air preheater 12,
Since the air inlet temperature of the primary air preheater 7 is raised,
The difference between the exhaust gas inlet temperature and the air inlet temperature of the primary air preheater 7 becomes small, the thermal strain generated in the primary air preheater 7 due to the change of the water content in the coal becomes small, and the leakage of the primary air preheater 7 The rate can be reduced.

【0053】更に、図2に示す実施例の場合、脱硝装置
13の上流側にガスタービン2の排気を適宜導入し得る
ため、脱硝装置13の排ガス入口温度を確保できる。
Further, in the case of the embodiment shown in FIG. 2, since the exhaust gas of the gas turbine 2 can be appropriately introduced to the upstream side of the denitration device 13, the exhaust gas inlet temperature of the denitration device 13 can be secured.

【0054】尚、本発明の石炭焚排気再燃コンバインド
サイクルプラントは、上述の実施例にのみ限定されるも
のではなく、一次空気予熱器と二次空気予熱器は一体型
ツインフロー式の空気予熱器としてもよいこと、一次通
風機を押込通風機の下流側に設置し、押込通風機から圧
送された空気の一部を一次通風機により更にブーストア
ップし一次空気とするようにしてもよいこと等、その
他、本発明の要旨を逸脱しない範囲内において種々変更
を加え得ることは勿論である。
The coal-fired exhaust gas re-combustion combined cycle plant of the present invention is not limited to the above-mentioned embodiment, and the primary air preheater and the secondary air preheater are integrated twin-flow type air preheaters. It is also possible to install a primary air blower on the downstream side of the forced draft fan, and a part of the air pressure-fed from the forced draft fan may be further boosted by the primary draft fan to be the primary air, etc. Of course, various changes can be made without departing from the scope of the present invention.

【0055】[0055]

【発明の効果】以上、説明したように本発明の請求項1
記載の石炭焚排気再燃コンバインドサイクルプラントに
よれば、燃焼安定性に優れ、設備の簡素化並びに設備費
低減を図り得ると共に消費電力を削減し得、空気予熱器
の二次空気側のリーク率低下を図り得るという優れた効
果を奏し、又、本発明の請求項2記載の石炭焚排気再燃
コンバインドサイクルプラントによれば、上記効果に加
え更に、ミルへ導入される一次空気の温度を石炭中の水
分量に応じてよりきめ細かく調整することが可能とな
り、且つ空気予熱器の一次空気側のリーク率低下を図る
ことができ、脱硝装置の上流側にガスタービンの排気を
適宜導入し得、脱硝装置の排ガス入口温度を確保できる
という優れた効果を奏し得る。
As described above, the first aspect of the present invention is as described above.
According to the coal-fired exhaust gas re-combustion combined cycle plant described, the combustion stability is excellent, the facility can be simplified and the facility cost can be reduced and the power consumption can be reduced, and the leakage rate on the secondary air side of the air preheater can be reduced. In addition to the above effects, according to the coal-fired exhaust gas re-combustion combined cycle plant of claim 2 of the present invention, the temperature of the primary air introduced into the mill is It is possible to make finer adjustments according to the amount of water, reduce the leak rate on the primary air side of the air preheater, and appropriately introduce the exhaust gas of the gas turbine to the upstream side of the denitration device. The excellent effect that the exhaust gas inlet temperature can be secured can be obtained.

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

【図1】本発明の一実施例のガス系統を表わすブロック
図である。
FIG. 1 is a block diagram showing a gas system according to an embodiment of the present invention.

【図2】本発明の他の実施例のガス系統を表わすブロッ
ク図である。
FIG. 2 is a block diagram showing a gas system according to another embodiment of the present invention.

【図3】従来例のガス系統を表わすブロック図である。FIG. 3 is a block diagram showing a gas system of a conventional example.

【符号の説明】[Explanation of symbols]

1 ボイラ 2 ガスタービン 4 ミル 5 一次通風機 6 押込通風機 7 一次空気予熱器(空気予熱器) 8 二次空気予熱器(空気予熱器) 9 ガスクーラ 10 ガスクーラ 11 蒸気式空気予熱器 12 蒸気式空気予熱器 13 脱硝装置 14 燃料管 15 一次空気ダクト 16 二次空気ダクト 17 ボイラ排ガスダクト 18 排気導入ダクト 20 ボイラバイパス排気ダクト 22 ガスクーラバイパスダクト 23 ボイラ排ガス分岐ダクト 24 一次空気予熱器バイパスダクト(空気予熱器バイ
パスダクト) 25 ボイラ排ガス分岐補助ダクト
1 Boiler 2 Gas turbine 4 Mill 5 Primary air blower 6 Pushing air blower 7 Primary air preheater (air preheater) 8 Secondary air preheater (air preheater) 9 Gas cooler 10 Gas cooler 11 Steam type air preheater 12 Steam type air Preheater 13 Denitration device 14 Fuel pipe 15 Primary air duct 16 Secondary air duct 17 Boiler exhaust gas duct 18 Exhaust introduction duct 20 Boiler bypass exhaust duct 22 Gas cooler bypass duct 23 Boiler exhaust gas branch duct 24 Primary air preheater bypass duct (Air preheater Bypass duct) 25 Boiler exhaust gas branching auxiliary duct

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 ボイラに、燃料としての微粉炭を供給す
るための燃料管と、燃焼用の二次空気を供給するための
二次空気ダクトと、燃焼排ガスを排出するためのボイラ
排ガスダクトとを接続し、前記燃料管に石炭粉砕用のミ
ルを接続すると共に、該ミルに燃料搬送用の一次空気を
供給するための一次空気ダクトを接続し、該一次空気ダ
クト並びに二次空気ダクト途中に、ボイラ排ガスダクト
から分岐せしめたボイラ排ガス分岐ダクト内を流れる排
ガスの熱により一次空気を予熱し且つボイラ排ガスダク
ト内を流れる排ガスの熱により二次空気を予熱するため
の空気予熱器を設け、該空気予熱器より上流側の一次空
気ダクトに一次通風機を、前記空気予熱器より上流側の
二次空気ダクトに押込通風機を夫々接続し、前記空気予
熱器の上下流位置の一次空気ダクトを結ぶ空気予熱器バ
イパスダクトを設け、前記押込通風機と空気予熱器との
間の二次空気ダクト途中に蒸気式空気予熱器を設け、前
記空気予熱器より上流側のボイラ排ガスダクト途中に、
ボイラへ送給される給水を加熱し且つ排ガスを冷却する
ためのガスクーラを設け、前記ガスクーラの上下流位置
のボイラ排ガスダクトを結ぶガスクーラバイパスダクト
を設け、前記空気予熱器より下流側の二次空気ダクト途
中に、ガスタービンの排気を導入するための排気導入ダ
クトを接続し、該排気導入ダクトから分岐し且つボイラ
をバイパスするボイラバイパス排気ダクトを前記ガスク
ーラより上流側のボイラ排ガスダクト途中に接続したこ
とを特徴とする石炭焚排気再燃コンバインドサイクルプ
ラント。
1. A fuel pipe for supplying pulverized coal as a fuel to a boiler, a secondary air duct for supplying secondary air for combustion, and a boiler exhaust gas duct for discharging combustion exhaust gas. And a mill for coal crushing is connected to the fuel pipe, and a primary air duct for supplying primary air for fuel transportation to the mill is connected to the primary air duct and the secondary air duct midway. An air preheater for preheating the primary air with the heat of the exhaust gas flowing in the boiler exhaust gas branch duct branched from the boiler exhaust gas duct and for preheating the secondary air with the heat of the exhaust gas flowing in the boiler exhaust gas duct, A primary air blower is connected to the primary air duct upstream of the air preheater, and a forced draft fan is connected to the secondary air duct upstream of the air preheater. An air preheater bypass duct connecting the primary air ducts is provided, a steam type air preheater is provided in the middle of the secondary air duct between the forced draft fan and the air preheater, and a boiler exhaust gas duct upstream of the air preheater is provided. On the way
A gas cooler is provided for heating the feed water sent to the boiler and cooling the exhaust gas, and a gas cooler bypass duct connecting the boiler exhaust gas ducts at the upstream and downstream positions of the gas cooler is provided, and the secondary air downstream of the air preheater is provided. An exhaust gas introduction duct for introducing exhaust gas of the gas turbine is connected in the middle of the duct, and a boiler bypass exhaust duct that branches from the exhaust gas introduction duct and bypasses the boiler is connected to the boiler exhaust gas duct upstream of the gas cooler. A coal-fired exhaust gas re-combustion combined cycle plant characterized by the above.
【請求項2】 空気予熱器バイパスダクトの分岐位置と
空気予熱器との間における一次空気ダクト途中に蒸気式
空気予熱器を設け、ボイラバイパス排気ダクトの分岐位
置より上流側の排気導入ダクト途中に、ボイラへ送給さ
れる給水を加熱し且つガスタービンの排気を冷却するた
めのガスクーラを設け、ボイラバイパス排気ダクトの接
続位置より下流側で且つガスクーラバイパスダクト及び
ボイラ排ガス分岐ダクトの分岐位置より上流側のボイラ
排ガスダクト途中に脱硝装置を設け、ガスクーラとガス
クーラバイパスダクトの接続位置との間のボイラ排ガス
ダクト途中から分岐し且つ空気予熱器より上流側のボイ
ラ排ガス分岐ダクト途中に接続されるボイラ排ガス分岐
補助ダクトを形成した請求項1記載の石炭焚排気再燃コ
ンバインドサイクルプラント。
2. A steam type air preheater is provided in the middle of the primary air duct between the branch position of the air preheater bypass duct and the air preheater, and in the middle of the exhaust introduction duct upstream of the branch position of the boiler bypass exhaust duct. Provide a gas cooler for heating the feed water sent to the boiler and cooling the exhaust gas of the gas turbine, downstream of the connection position of the boiler bypass exhaust duct and upstream of the branch position of the gas cooler bypass duct and the boiler exhaust gas branch duct. Boiler exhaust gas that is installed in the middle of the boiler exhaust gas duct on the side of The coal-fired exhaust gas reburn combined cycle according to claim 1, wherein a branch auxiliary duct is formed. plant.
JP4115498A 1992-04-08 1992-04-08 Coal firing discharged gas re-igniting combined cycle plant Pending JPH05288301A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4115498A JPH05288301A (en) 1992-04-08 1992-04-08 Coal firing discharged gas re-igniting combined cycle plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4115498A JPH05288301A (en) 1992-04-08 1992-04-08 Coal firing discharged gas re-igniting combined cycle plant

Publications (1)

Publication Number Publication Date
JPH05288301A true JPH05288301A (en) 1993-11-02

Family

ID=14664003

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4115498A Pending JPH05288301A (en) 1992-04-08 1992-04-08 Coal firing discharged gas re-igniting combined cycle plant

Country Status (1)

Country Link
JP (1) JPH05288301A (en)

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