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JP2961073B2 - Gas turbine exhaust reburn complex plant - Google Patents
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JP2961073B2 - Gas turbine exhaust reburn complex plant - Google Patents

Gas turbine exhaust reburn complex plant

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Publication number
JP2961073B2
JP2961073B2 JP20433895A JP20433895A JP2961073B2 JP 2961073 B2 JP2961073 B2 JP 2961073B2 JP 20433895 A JP20433895 A JP 20433895A JP 20433895 A JP20433895 A JP 20433895A JP 2961073 B2 JP2961073 B2 JP 2961073B2
Authority
JP
Japan
Prior art keywords
gas
feed water
feedwater
heater
low
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
JP20433895A
Other languages
Japanese (ja)
Other versions
JPH0953415A (en
Inventor
浩史 三島
得志 丸田
康裕 竹井
康子 大沢
正俊 柴田
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
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Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP20433895A priority Critical patent/JP2961073B2/en
Publication of JPH0953415A publication Critical patent/JPH0953415A/en
Application granted granted Critical
Publication of JP2961073B2 publication Critical patent/JP2961073B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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、ガスタービン排気
をボイラ火炉の燃焼用空気として用いるガスタービン排
気再燃複合プラントに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a combined gas turbine exhaust reburning plant using gas turbine exhaust as combustion air for a boiler furnace.

【0002】[0002]

【従来の技術】図5は従来のガスタービン排気再燃複合
プラントの一例を示す概略系統図である。
2. Description of the Related Art FIG. 5 is a schematic system diagram showing an example of a conventional gas turbine exhaust reburning combined plant.

【0003】空気(大気)(101)はコンプレッサ(2
0)により昇圧され、加圧空気(121)としてコンバスタ
(21)へ送られる。コンバスタ(21)にはガスター
ビン燃料(120)も供給されて燃焼し、高温高圧のガスタ
ービン入口ガス(122)が発生する。ガスタービン入口ガ
ス(122)はガスタービン(22)を駆動し、ガスタービ
ン発電機(23)により電力を発生する。ガスタービン
(22)でエネルギを回収されたガスタービン排気(12
3)は、14%程度の酸素を含むので、ボイラ(4)の
火炉燃焼用空気として燃料(104)と共に風箱(3)より
ボイラ(4)火炉へ投入される。ボイラ(4)の火炉か
ら排出されたボイラ出口排ガス(105)は、ガス高圧給水
加熱器(25)およびガス低圧給水加熱器(26)で給
水,復水と熱交換し、排ガス(106)となって煙突(5)
から大気へ排出される。
The air (atmosphere) (101) is a compressor (2)
0) and is sent to the combustor (21) as pressurized air (121). The gas turbine fuel (120) is also supplied to the combustor (21) and burns to generate a gas turbine inlet gas (122) having a high temperature and a high pressure. The gas turbine inlet gas (122) drives the gas turbine (22) and generates electric power by a gas turbine generator (23). The gas turbine exhaust (12) whose energy has been recovered by the gas turbine (22)
Since 3) contains about 14% oxygen, it is put into the boiler (4) furnace from the wind box (3) together with the fuel (104) as furnace combustion air for the boiler (4). The boiler outlet exhaust gas (105) discharged from the furnace of the boiler (4) exchanges heat with feed water and condensate in a gas high-pressure feed water heater (25) and a gas low-pressure feed water heater (26) and exchanges with the exhaust gas (106). Become a chimney (5)
Is released into the atmosphere from

【0004】一方給水糸では、低圧タービン排気(107)
が復水器(6)により復水(108)となり、復水ポンプ
(7)で昇圧される。この復水ポンプ出口給水(109)
は、低圧給水加熱器(8)で蒸気により加熱され、ガス
低圧給水加熱器給水(225)として、ガス低圧給水加熱器
(26)へ導入される。ガス低圧給水加熱器(26)で
再び加熱されたガス低圧給水加熱器出口給水(132)は、
脱気器(9)を経て脱気器出口給水(111)となり、給水
ポンプ(10)で更に昇圧され、ガス高圧給水加熱器給
水(233)となる。ガス高圧給水加熱器(25)で更に加
熱されたボイラ給水(139)は、節炭器(12)を介して
ボイラ(4)へ導入される。
On the other hand, in the case of a water supply line, a low-pressure turbine exhaust (107)
Is condensed (108) by the condenser (6) and is pressurized by the condensate pump (7). This condensate pump outlet water supply (109)
Is heated by steam in the low-pressure feedwater heater (8), and is introduced into the low-pressure gas feedwater heater (26) as the low-pressure feedwater heater water supply (225). The gas low pressure feed water heater outlet feed water (132) heated again by the gas low pressure feed water heater (26)
Water is supplied to the deaerator outlet water supply (111) through the deaerator (9), and the pressure is further increased by the water supply pump (10) to become a gas high-pressure water supply heater water supply (233). The boiler feedwater (139) further heated by the gas high-pressure feedwater heater (25) is introduced into the boiler (4) via the economizer (12).

【0005】[0005]

【発明が解決しようとする課題】前記従来のプラントで
は次のような解決すべき課題があった。
The conventional plant has the following problems to be solved.

【0006】1)定格点で設計されたガス給水加熱器で
は、部分負荷時に給水温度・排ガス温度が十分に制御で
きない。そのため、図6中に破線で示されるように給水
温度が上がり過ぎて節炭器でスチーミングが発生した
り、図7中の破線のように排ガス温度が下がりすぎて、
ガス給水加熱器の低温腐食が生じたりする。
1) In a gas feed water heater designed at a rated point, the feed water temperature and the exhaust gas temperature cannot be sufficiently controlled at a partial load. Therefore, as shown by the broken line in FIG. 6, the feedwater temperature rises too much and steaming occurs in the economizer, or the exhaust gas temperature falls too much as shown by the broken line in FIG.
Low temperature corrosion of the gas feed water heater may occur.

【0007】2)ボイラの累積運転時間が長くなるにつ
れて、ガス給水加熱器器内がボイラ排ガスにより汚れて
いくため、図8に示されるように熱伝達が低下し、適性
な給水温度・排ガス温度が得られなくなる。
[0007] 2) As the cumulative operation time of the boiler becomes longer, the inside of the gas feed water heater becomes dirty with the boiler exhaust gas, so that heat transfer is reduced as shown in FIG. Can not be obtained.

【0008】[0008]

【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、ガスタービンの排気をボイラ火
炉の燃焼用空気として用いるとともに、タービン抽気で
加熱する給水加熱器の系統とは別に上記ボイラ火炉の排
ガスによってボイラ給水を加熱する複数のガス給水加熱
器を直列に設置したガスタービン排気再燃複合プラント
において、給水が上記ガス給水加熱器および給水加熱器
をそれぞれバイパスするバイパスラインと、上流側の上
記ガス給水加熱器の出口から入口へ給水の一部を戻す給
水循環ラインと、同給水循環ラインに設けられた給水循
環ポンプとを備えたことを特徴とするガスタービン排気
再燃複合プラント;ならびに、ガスタービンの排気をボ
イラ火炉の燃焼用空気として用いるとともに、タービン
抽気で加熱する給水加熱器の系統とは別に上記ボイラ火
炉の排ガスによってボイラ給水を加熱する複数のガス給
水加熱器を直列に設置したガスタービン排気再燃複合プ
ラントにおいて、上記複数のガス給水加熱器の間の給水
ラインに設けられた脱気器と、同脱気器の圧力を上記ガ
ス給水加熱器の入口温度が所要の温度になる圧力まで昇
圧して同脱気器の出口の給水の一部を上流側の上記ガス
給水加熱器の入口へ戻す脱気器循環ラインと、同脱気器
循環ラインに設けられた脱気器循環ポンプとを備えたこ
とを特徴とするガスタービン排気再燃複合プラントを提
案するものである。
In order to solve the above-mentioned conventional problems, the present inventor uses the exhaust gas of a gas turbine as combustion air for a boiler furnace, and also uses the turbine bleed air.
In a gas turbine exhaust reburning combined plant in which a plurality of gas feed water heaters for heating boiler feed water by exhaust gas from the boiler furnace separately from the feed water heater system to be heated are provided, the feed water is the gas feed water heater and the feed water heating. a bypass line for bypassing vessel <br/> respectively, a water supply circulation line from the outlet of the upstream side of the gas feed water heater returning part of the water supply to the inlet, and a water supply circulation pump provided in the water supply circulation line gas turbine repowering combined plant characterized by comprising; and with use of the exhaust gas turbine as combustion air of the boiler furnace, turbine
Separately from the feed water heater system that heats by bleeding, in a gas turbine exhaust reburn complex plant in which a plurality of gas feed water heaters that heat boiler feed water by exhaust gas from the boiler furnace are installed in series, the plurality of gas feed water heaters Between the deaerator and the pressure of the deaerator
The inlet temperature of the feed water heater rises to the pressure at which the required temperature is reached.
A deaerator circulation line that pressurizes and returns a part of the feedwater at the outlet of the deaerator to the inlet of the gas feedwater heater on the upstream side, and a deaerator circulation pump provided in the deaerator circulation line. It is intended to propose a gas turbine exhaust gas reburning combined plant characterized by comprising:

【0009】上記第1の解決手段においては、給水がガ
ス給水加熱器および給水加熱器をそれぞれバイパスする
バイパスラインが設けられているので、ボイラが部分負
荷で運転されている時は、バイパスラインのバルブを開
くことにより、ガス給水加熱器内へ流れる給水量を制御
できる。したがってボイラ入口給水温度が制御可能とな
り、節炭器のスチーミングを防止できる。またボイラの
累積運転時間が長くなるにつれてガス給水加熱器内はボ
イラ排ガスにより汚れてくるが、ボイラ運転当初はバイ
パス量を増しておき、運転が進んでガス給水加熱器内が
汚れていって熱吸収量が減少してきた時に、バイパス量
を減少させることにより、節炭器入口の給水温度を制御
できる。
In the first solution, the bypass line is provided for supplying water to the gas feed water heater and the feed water heater, respectively. Therefore, when the boiler is operated at a partial load, the bypass line is provided. By opening the valve, the amount of water flowing into the gas feed water heater can be controlled. Therefore, the boiler inlet feedwater temperature can be controlled, and steam saving of the economizer can be prevented. Also, as the cumulative operation time of the boiler becomes longer, the inside of the gas feedwater heater becomes contaminated with the boiler exhaust gas.However, at the beginning of the boiler operation, the bypass amount is increased, and the operation proceeds, and the inside of the gas feedwater heater becomes dirty and becomes hot. When the amount of absorption decreases, the supply water temperature at the economizer inlet can be controlled by reducing the amount of bypass.

【0010】更に上流側の上記ガス給水加熱器の出口か
ら入口へ給水の一部を戻す給水循環ラインと、同給水循
環ラインに設けられた給水循環ポンプとを備えているの
で、プラントの部分負荷時にボイラ排ガスの流量と温度
が低下した場合、給水循環ラインのバルブを開き給水循
環ポンプを駆動することにより、ガス給水加熱器出口の
排ガス温度も制御可能となり、ガス給水加熱器の低温腐
食を防止できる。
[0010] Further, since there is provided a feed water circulation line for returning a part of the feed water from the outlet to the inlet of the gas feed water heater on the upstream side, and a feed water circulation pump provided in the feed water circulation line, the plant has a partial load. When the flow rate and temperature of the boiler exhaust gas decrease, the exhaust gas temperature at the outlet of the gas feed water heater can be controlled by opening the valve of the feed water circulation line and driving the feed water circulation pump, preventing low temperature corrosion of the gas feed water heater. it can.

【0011】極低負荷帯では低圧給水加熱器器内圧が著
しく低く、たとえ上記給水循環ラインに給水を循環させ
ても所要の温度まで昇温できない懸念があるが、上記第
2の解決手段では、同脱気器の圧力を上記ガス給水加熱
器の入口温度が所要の温度になる圧力まで昇圧して同脱
気器の出口の給水の一部を上流側の上記ガス給水加熱器
の入口へ戻す脱気器循環ラインと、同脱気器循環ライン
に設けられた脱気器循環ポンプとを備えているので、脱
気器循環ラインのバルブを開き脱気器循環ポンプを駆動
することにより、極低負荷帯においても、ガス給水加熱
器の入口給水温度を硫酸腐食を発生しない温度まで昇温
することができる。すなわち、低負荷帯において上流側
のガス給水加熱器よりも圧力の高い脱気器貯槽の保有水
であれば、上流側のガス給水加熱器入口水を昇温し易
く、かつ脱気器器内圧を補助蒸気で加圧することによ
り、確実に所要温度に上昇させることができる。そし
て、汽力単独運転時も複合運転時も同一装置で対応でき
る。
In the extremely low load zone, the internal pressure of the low-pressure feed water heater is extremely low, and there is a concern that the temperature cannot be increased to a required temperature even if the feed water is circulated through the feed water circulation line. Heat the gas supply water with the pressure of the deaerator
A deaerator circulation line for raising the inlet temperature of the deaerator to a required temperature and returning a part of the feed water at the outlet of the deaerator to the inlet of the gas feed water heater on the upstream side; Since it has a deaerator circulation pump provided in the circulation line, by opening the valve of the deaerator circulation line and driving the deaerator circulation pump, even in an extremely low load zone, the gas feed water heater The inlet feedwater temperature can be raised to a temperature at which sulfuric acid corrosion does not occur. In other words, if the water in the deaerator storage tank has a higher pressure than the upstream gas feed water heater in the low load zone, the temperature of the upstream gas feed water heater inlet water can be easily raised, and the deaerator internal pressure can be increased. Is pressurized with auxiliary steam, the temperature can be reliably raised to the required temperature. In addition, the same device can cope with both the steam alone operation and the combined operation.

【0012】[0012]

【発明の実施の形態】図1は本発明の実施の第1の形態
を示す概略系統図である。この図において、前記図5に
より説明した従来のものと同様の部分については、同一
の符号が付けられている。
FIG. 1 is a schematic system diagram showing a first embodiment of the present invention. In this figure, the same parts as those of the conventional one described with reference to FIG. 5 are denoted by the same reference numerals.

【0013】本実施形態においても従来の技術と同様、
空気(大気)(101)はコンプレッサ(20)により昇圧
され、加圧空気(121)としてコンバスタ(21)へ送ら
れる。コンバスタ(21)にはガスタービン燃料(120)
も供給されて燃焼し、高温高圧のガスタービン入口ガス
(122)が発生する。ガスタービン入口ガス(122)はガス
タービン(22)を駆動し、ガスタービン発電機(2
3)により電力を発生する。ガスタービン(22)でエ
ネルギを回収されたガスタービン排気(123)は、ボイラ
(4)火炉の燃焼用空気として燃料(104)とともに風箱
(3)からボイラ(4)へ投入される。燃料(104)の燃
焼によって発生した排ガス(105)は、ガス高圧給水加熱
器(25)およびガス低圧給水加熱器(26)で熱回収
された後、煙突(5)から排ガス(106)として排出され
る。
In this embodiment, as in the prior art,
The air (atmosphere) (101) is pressurized by the compressor (20) and sent to the combustor (21) as pressurized air (121). Gas turbine fuel (120) for combustor (21)
Also supplied and burned, high temperature and high pressure gas turbine inlet gas
(122) occurs. The gas turbine inlet gas (122) drives the gas turbine (22) and the gas turbine generator (2).
3) generates electric power. The gas turbine exhaust (123) whose energy has been recovered by the gas turbine (22) is fed into the boiler (4) from the wind box (3) together with the fuel (104) as combustion air for the boiler (4) furnace. The exhaust gas (105) generated by the combustion of the fuel (104) is recovered as heat by the gas high-pressure feed water heater (25) and the gas low-pressure feed water heater (26), and then discharged from the chimney (5) as the exhaust gas (106). Is done.

【0014】一方給水糸では、低圧タービン排気(107)
が復水器(6)により復水(108)となり、復水ポンプ
(7)で昇圧される。この復水ポンプ出口給水(109)
は、低圧給水加熱器(8)とガス低圧給水加熱器(2
6)向けに分岐される。低圧給水加熱器(8)では、蒸
気タービンの抽気蒸気により加熱されて低圧給水加熱器
出口給水(110)となる。またガス低圧給水加熱器(2
6)向けの給水は、更に低温ガス低圧給水加熱器給水(1
25)と低温ガス低圧給水加熱器バイパス給水(126)とに
分岐する。低温ガス低圧給水加熱器給水(125)は、ガス
低圧給水加熱器(26)の低温部で熱交換後、低温ガス
低圧給水加熱器バイパス給水(126)と合流して低温ガス
低圧給水加熱器出口給水(127)となり、更に、高温ガス
低圧給水加熱器給水(128)と高温ガス低圧給水加熱器バ
イパス給水(129)に再び分岐する。高温ガス低圧給水加
熱器給水(128)は、ガス低圧給水加熱器(26)の高温
部で熱交換後、高温ガス低圧給水加熱器バイパス給水(1
29)と合流して高温ガス低圧給水加熱器出口給水(130)
となる。高温ガス低圧給水加熱器出口給水(130)のライ
ンには、復水ポンプ出口給水(109)への再循環ラインが
設けられており、再循環ポンプ(27)によって、ガス
低圧給水加熱器再循環水(131)が流れるようになってい
る。
On the other hand, in the case of the water supply thread, the low-pressure turbine exhaust (107)
Is condensed (108) by the condenser (6) and is pressurized by the condensate pump (7). This condensate pump outlet water supply (109)
Is a low pressure feed water heater (8) and a gas low pressure feed water heater (2
It branches to 6). In the low-pressure feedwater heater (8), the water is heated by the extracted steam of the steam turbine and becomes the low-pressure feedwater heater outlet feedwater (110). In addition, gas low pressure feed water heater (2
6) Water supply for low-temperature gas low-pressure feedwater heater water supply (1)
25) and a low-temperature gas low-pressure feed water heater bypass feed water (126). The low-temperature gas low-pressure feedwater heater feedwater (125) exchanges heat with the low-temperature part of the low-temperature gas low-pressure feedwater heater (26), then merges with the low-temperature gas low-pressure feedwater heater bypass feedwater (126) and exits at the low-temperature gas low-pressure feedwater heater. The feed water (127) is then branched again into a hot gas low pressure feed water heater feed water (128) and a hot gas low pressure feed water heater bypass feed water (129). The high-temperature gas low-pressure feedwater heater feedwater (128) is heat-exchanged in the high-temperature portion of the gas low-pressure feedwater heater (26), and then is passed through the hot gas low-pressure feedwater heater bypass feedwater (1).
29) Merge with high temperature gas low pressure feed water heater outlet water supply (130)
Becomes The recirculation line to the condensate pump outlet water supply (109) is provided in the line of the high temperature gas low pressure water heater outlet water supply (130), and the gas low pressure water heater recirculation is performed by the recirculation pump (27). The water (131) flows.

【0015】低圧給水加熱器(8)で加熱された低圧給
水加熱器出口給水(110)は、ガス低圧給水加熱器(2
6)で加熱された高温ガス低圧給水加熱器出口給水(13
0)と合流して、ガス低圧給水加熱器出口給水(132)と
なる。そして脱気器(9)を通過して脱気器出口給水(1
11)となり、更に給水ポンプ(10)で昇圧された後、
給水ポンプ出口給水(112)となる。この給水ポンプ出口
給水(112)は、高圧給水加熱器(11)とガス高圧給水
加熱器(25)向けに分岐され、高圧給水加熱器(1
1)では蒸気タービンの抽気蒸気により加熱されて高圧
給水加熱器出口給水(113)となる。またガス高圧給水加
熱器(25)向けの給水は、更に低温ガス高圧給水加熱
器給水(133)と低温ガス高圧給水加熱器バイパス給水(1
34)とに分岐する。そして低温ガス高圧給水加熱器給水
(133)は、ガス高圧給水加熱器(25)の低温部で熱交
換後、低温ガス高圧給水加熱器バイパス給水(134)と合
流して低温ガス高圧給水加熱器出口給水(135)となり、
更に高温ガス高圧給水加熱器給水(136)と高温ガス高圧
給水加熱器バイパス給水(137)に再び分岐する。高温ガ
ス高圧給水加熱器給水(136)は、ガス高圧給水加熱器
(25)の高温部で熱交換後、高温ガス高圧給水加熱器
バイパス給水(137)と合流してガス高圧給水加熱器出口
給水(138)となる。
The low-pressure feed water heater outlet feed water (110) heated by the low-pressure feed water heater (8) is supplied to the gas low-pressure feed water heater (2).
6) High-temperature gas low-pressure feed water heated at the outlet of the heater (13
0) and becomes the water supply (132) at the outlet of the gas low-pressure water heater. After passing through the deaerator (9), the deaerator outlet water supply (1
11), and after the pressure is increased by the water supply pump (10),
Water supply pump outlet water supply (112). This feedwater pump outlet feedwater (112) is branched to a high-pressure feedwater heater (11) and a gas high-pressure feedwater heater (25).
In 1), the steam is heated by the extracted steam of the steam turbine and becomes high-pressure feed water heater outlet feed water (113). In addition, the feed water for the gas high-pressure feed water heater (25) further includes low-temperature gas high-pressure feed water heater feed water (133) and low-temperature gas high-pressure feed water heater bypass feed water (1).
Branch to 34). And low temperature gas high pressure feed water heater feed water
(133) heat-exchanges in the low temperature part of the gas high pressure feed water heater (25), and then joins with the low temperature gas high pressure feed water heater bypass feed water (134) to become the low temperature gas high pressure feed water heater outlet feed water (135);
The hot water high-pressure feed water heater feed water (136) and the hot gas high-pressure feed water heater bypass feed water (137) are branched again. The high-temperature gas high-pressure feed water heater feed water (136) exchanges heat with the high-temperature portion of the high-pressure gas high-pressure feed water heater (25), and then merges with the high-temperature gas high-pressure feed water heater bypass feed water (137) to supply the gas high-pressure feed water heater outlet water. (138).

【0016】高圧給水加熱器(11)で加熱された高圧
給水加熱器出口給水(113)は、ガス高圧給水加熱器(2
5)で加熱されたガス高圧給水加熱器出口給水(138)と
合流してボイラ給水(139)となり、節炭器(12)へ供
給される。
The high-pressure feed water heater outlet water (113) heated by the high-pressure feed water heater (11) is supplied to the gas high-pressure feed water heater (2).
It joins with the high-pressure gas supply water heater outlet water supply (138) heated in 5) to become boiler water supply (139) and is supplied to the economizer (12).

【0017】以上の系統において、部分負荷時には、ガ
ス低圧給水加熱器(26)とガス高圧給水加熱器(2
5)にそれぞれ設けられているバイパスラインに給水の
一部を流すことにより、節炭器(12)へ供給される給
水の温度を制御するとともに、ガス低圧給水加熱器(2
6)の給水再循環ラインに再循環水(131)を流すことに
より、ガス低圧給水加熱器(26)出口の排ガス(106)
の温度を制御する。またボイラ運転当初は、ガス低圧給
水加熱器(26)とガス高圧給水加熱器(25)の内部
がまだ汚れていないので、各バイパスラインのバルブを
若干開いておき、運転年月の経過に伴ってガス低圧・高
圧給水加熱器(25),(26)の内部が汚れてきたな
らばバイパスラインのバルブを次第に閉じていくことに
より、ガス低圧・高圧給水加熱器(25),(26)の
熱吸収量を制御する。
In the above system, at the time of partial load, the gas low pressure feed water heater (26) and the gas high pressure feed water heater (2)
5) Controlling the temperature of the feedwater supplied to the economizer (12) by flowing a part of the feedwater through the bypass lines provided in each of the bypass lines, the gas low-pressure feedwater heater (2)
The exhaust gas (106) at the outlet of the gas low-pressure feed water heater (26) by flowing the recirculated water (131) through the feed water recirculation line of 6)
Control the temperature of the Also, at the beginning of the boiler operation, since the insides of the gas low-pressure feed water heater (26) and the gas high-pressure feed water heater (25) have not been contaminated yet, the valves of each bypass line are slightly opened, and as the operation date elapses. If the inside of the gas low pressure / high pressure feed water heaters (25) and (26) becomes dirty, the valve of the gas low pressure / high pressure feed water heaters (25) and (26) is gradually closed by gradually closing the valve of the bypass line. Control the heat absorption.

【0018】上記のとおり本実施形態においては、ガス
給水加熱器(25),(26)に設けられたバイパスラ
インの給水流量を制御することにより、節炭器(12)
に供給される給水の温度を制御できるので、図6中に実
線で示されるように、プラントの部分負荷時やプラント
運転当初でも節炭器のスチーミングが防止できる。ま
た、ガス低圧給水加熱器(26)に設けられた給水循環
ラインの循環水流量を制御することにより、ガス低圧給
水加熱器(26)の出口排ガス温度を制御できるので、
図7中の実線のように、プラントの部分負荷時において
ガス低圧給水加熱器(26)の低温腐食が防止できる。
As described above, in the present embodiment, by controlling the feedwater flow rate of the bypass lines provided in the gas feedwater heaters (25) and (26), the economizer (12) is used.
As shown by the solid line in FIG. 6, steaming of the economizer can be prevented even when the plant is partially loaded or at the beginning of the plant operation. Also, by controlling the circulating water flow rate of the feed water circulation line provided in the gas low pressure feed water heater (26), the exhaust gas temperature at the outlet of the gas low pressure feed water heater (26) can be controlled.
As shown by the solid line in FIG. 7, low-temperature corrosion of the gas low-pressure feedwater heater (26) can be prevented when the plant is partially loaded.

【0019】次に図2は本発明の実施の第2形態を示す
概略系統図である。
Next, FIG. 2 is a schematic system diagram showing a second embodiment of the present invention.

【0020】ボイラの排ガス(220)は、ガス高圧給水加
熱器(204)で給水と熱交換した後、ガス低圧給水加熱器
(203)で復水と熱交換して低温ガス(222)となり、電気
集塵器を経て煙突から大気へ放出される。一方水系統
は、復水器で凝縮した復水が低圧給水加熱器(201)によ
り加熱されて低圧加熱器出口給水となり、ガス低圧給水
加熱器(203)へ導入される。この給水はガス低圧給水加
熱器(203)が硫酸腐食を生じない温度以上であらねばな
らない。
The boiler exhaust gas (220) exchanges heat with feed water in a gas high-pressure feed water heater (204), and then exchanges heat with the gas low-pressure feed water heater.
At (203), heat exchange occurs with condensate to become low-temperature gas (222), which is released from the chimney to the atmosphere via an electric dust collector. On the other hand, in the water system, the condensed water condensed in the condenser is heated by the low-pressure feed water heater (201) to become the low-pressure heater outlet feed water, and is introduced into the gas low-pressure feed water heater (203). This water supply must be at a temperature above which the gas low pressure feed water heater (203) does not cause sulfuric acid corrosion.

【0021】部分負荷においては、ガス低圧給水加熱器
(203)の出口給水(212)をガス低圧給水加熱器循環ポン
プ(205)により再循環させ、図3に示されるように、入
口給水温度を所要温度まで加熱することができる。また
低負荷帯においては、図4に示されるように、脱気器(2
02)の圧力をガス低圧給水加熱器(203)の入口温度が所
要の温度になる圧力まで昇圧し、脱気器循環ポンプ(20
6)によって再循環させることにより、対応することが
できる。汽力単独運転でも、同上方式により対応可能と
なる。
At partial load, gas low pressure feed water heater
The outlet water supply (212) of (203) can be recirculated by the gas low pressure feed water heater circulation pump (205) to heat the inlet water supply temperature to the required temperature as shown in FIG. In the low load zone, as shown in FIG.
02), the pressure of the gas low-pressure feed water heater (203) is increased to the required temperature, and the deaerator circulation pump (20)
By recirculating according to 6), it is possible to respond. The same method can also be applied to steam-only operation.

【0022】上記のとおり本実施形態によれば、低負荷
においてもガス低圧給水加熱器の入口給水温度を硫酸腐
食の発生する露点温度以上に保つことができる。また、
汽力単独運転においても、ボイラ排ガス量が減少し、ガ
ス低圧給水加熱器入口給水温度が上昇しにくい状態とな
るが、更に加圧された脱気器貯槽の保有水を循環させる
ことにより、部分負荷においても露点温度以上に保つこ
とができる。
As described above, according to the present embodiment, even at a low load, the inlet feedwater temperature of the gas low-pressure feedwater heater can be maintained at a temperature equal to or higher than the dew point at which sulfuric acid corrosion occurs. Also,
Even in steam alone operation, the boiler exhaust gas volume decreases and the temperature of the feedwater at the inlet of the gas low-pressure feedwater heater becomes difficult to rise.However, by circulating the pressurized water in the deaerator storage tank, the partial load is reduced. Can be maintained at a temperature equal to or higher than the dew point.

【0023】[0023]

【発明の効果】本発明によれば、ガス給水加熱器に設け
られたバイパスラインの給水流量を制御することによ
り、節炭器に供給される給水の温度を制御できるので、
プラントの部分負荷時や、プラント運転当初時にも節炭
器のスチーミングが防止できる。また、上流側のガス給
水加熱器に設けられた給水循環ラインの循環水流量を制
御することにより、上流側のガス給水加熱器の出口排ガ
ス温度を制御できるので、プラントの部分負荷時におい
てガス給水加熱器の低温腐食が防止できる。
According to the present invention, the temperature of the feedwater supplied to the economizer can be controlled by controlling the feedwater flow rate of the bypass line provided in the gas feedwater heater.
Steaming of the economizer can be prevented even during partial load of the plant or at the beginning of plant operation. Also, by controlling the circulating water flow rate of the feed water circulation line provided in the upstream gas feed water heater, the temperature of the exhaust gas at the outlet of the upstream gas feed water heater can be controlled. Low temperature corrosion of the heater can be prevented.

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

【図1】図1は本発明の実施の第1形態を示す概略系統
図である。
FIG. 1 is a schematic system diagram showing a first embodiment of the present invention.

【図2】図2は本発明の実施の第2形態を示す概略系統
図である。
FIG. 2 is a schematic system diagram showing a second embodiment of the present invention.

【図3】図3はガス低圧給水加熱器入口給水温度を一定
とするための脱気器飽和水温度と脱気器再循環流量の関
係を示す図である。
FIG. 3 is a diagram showing a relationship between a deaerator saturated water temperature and a deaerator recirculation flow rate for keeping a gas low-pressure feedwater heater inlet feedwater temperature constant.

【図4】図4は蒸気タービン負荷と脱気器圧力の関係を
示す図である。
FIG. 4 is a diagram showing a relationship between a steam turbine load and a deaerator pressure.

【図5】図5は従来のガスタービン排気再燃複合プラン
トの一例を示す概略系統図である。
FIG. 5 is a schematic system diagram showing an example of a conventional gas turbine exhaust reburn combined plant.

【図6】図6はプラント負荷と節炭器入口給水エンタル
ピの関係を示す図である。
FIG. 6 is a diagram showing a relationship between plant load and enthalpy of water supply at the inlet of the economizer.

【図7】図7はプラント負荷とガス給水加熱器出口ガス
温度の関係を示す図である。
FIG. 7 is a diagram showing a relationship between a plant load and a gas feed water heater outlet gas temperature.

【図8】図8はボイラの累計運転時間とガス給水加熱器
熱吸収量の関係を示す図である。
FIG. 8 is a diagram showing the relationship between the cumulative operation time of the boiler and the heat absorption of the gas feed water heater.

【符号の説明】[Explanation of symbols]

(3) 風箱 (4) ボイラ (5) 煙突 (6) 復水器 (7) 復水ポンプ (8) 低圧給水加熱器 (9) 脱気器 (10) 給水ポンプ (11) 高圧給水加熱器 (12) 節炭器 (20) コンプレッサ (21) コンバスタ (22) ガスタービン (23) ガスタービン発電機 (25) ガス高圧給水加熱器 (26) ガス低圧給水加熱器 (27) 再循環ポンプ (101) 空気(大気) (104) ボイラ燃料 (105) ボイラ出口排ガス (106) 排ガス (107) 低圧タービン排気 (108) 復水 (109) 復水ポンプ出口給水 (110) 低圧給水加熱器出口給水 (111) 脱気器出口給水 (112) 給水ポンプ出口給水 (113) 高圧給水加熱器出口給水 (120) ガスタービン燃料 (121) 加圧空気 (122) ガスタービン入口ガス (123) ガスタービン排気 (125) 低温ガス低圧給水加熱器給水 (126) 低温ガス低圧給水加熱器バイパス給水 (127) 低温ガス低圧給水加熱器出口給水 (128) 高温ガス低圧給水加熱器給水 (129) 高温ガス低圧給水加熱器バイパス給水 (130) 高温ガス低圧給水加熱器出口給水 (131) ガス低圧給水加熱器再循環水 (132) ガス低圧給水加熱器出口給水 (133) 低温ガス高圧給水加熱器給水 (134) 低温ガス高圧給水加熱器バイパス給水 (135) 低温ガス高圧給水加熱器出口給水 (136) 高温ガス高圧給水加熱器給水 (137) 高温ガス高圧給水加熱器バイパス給水 (138) ガス高圧給水加熱器出口給水 (139) ボイラ給水 (201) 低圧給水加熱器 (202) 脱気器 (203) ガス低圧給水加熱器 (204) ガス高圧給水加熱器 (205) ガス低圧給水加熱器循環ポンプ (206) 脱気器循環ポンプ (211) 低圧給水加熱器出口給水 (212) 低圧ガス給水加熱器出口給水 (213) 低圧ガス給水加熱器循環水 (214) 脱気器循環水 (220) ボイラ排ガス (221) ガス高圧給水加熱器出口ガス (222) ガス低圧給水加熱器出口ガス (225) ガス低圧給水加熱器給水 (233) ガス高圧給水加熱器給水 (3) Wind box (4) Boiler (5) Chimney (6) Condenser (7) Condenser pump (8) Low-pressure feedwater heater (9) Deaerator (10) Feedwater pump (11) High-pressure feedwater heater (12) Economizer (20) Compressor (21) Combustor (22) Gas turbine (23) Gas turbine generator (25) Gas high pressure feed water heater (26) Gas low pressure feed water heater (27) Recirculation pump (101) ) Air (atmosphere) (104) Boiler fuel (105) Exhaust gas from boiler (106) Exhaust gas (107) Low pressure turbine exhaust (108) Condensate water (109) Condensate pump outlet water supply (110) Low pressure feedwater heater outlet water supply (111) ) Deaerator outlet feedwater (112) Feedwater pump outlet feedwater (113) High-pressure feedwater heater outlet feedwater (120) Gas turbine fuel (121) Pressurized air (122) Gas turbine inlet gas (123) Gas turbine exhaust (125) Low-temperature gas low-pressure feed water heater feed water ( 126) Low-temperature gas low-pressure feedwater heater bypass feedwater (127) Low-temperature gas low-pressure feedwater heater outlet feedwater (128) High-temperature gas low-pressure feedwater heater feedwater (129) High-temperature gas low-pressure feedwater heater bypass feedwater (130) High-temperature gas low-pressure feedwater heating Unit outlet water supply (131) Gas low pressure feed water heater recirculating water (132) Gas low pressure feed water heater outlet water supply (133) Low temperature gas high pressure feed water heater feed water (134) Low temperature gas high pressure feed water heater bypass feed water (135) Low temperature gas High pressure feed water heater outlet water supply (136) High temperature gas high pressure feed water heater water supply (137) High temperature gas high pressure feed water heater bypass water supply (138) Gas high pressure feed water heater outlet water supply (139) Boiler feed water (201) Low pressure feed water heater ( 202) Deaerator (203) Gas low pressure feed water heater (204) Gas high pressure feed water heater (205) Gas low pressure feed water heater circulation pump (206) Deaerator circulation pump (211) Low pressure feed water heater outlet water supply (212 ) Low pressure gas feed water heater outlet Water (213) Circulating water for low-pressure gas feed water heater (214) Circulating water for deaerator (220) Boiler exhaust gas (221) Gas high-pressure feed water heater outlet gas (222) Gas low-pressure feed water heater outlet gas (225) Gas low-pressure feed water Heater water supply (233) Gas high pressure water heater water supply

───────────────────────────────────────────────────── フロントページの続き (72)発明者 大沢 康子 東京都千代田区丸の内二丁目5番1号 三菱重工業株式会社内 (72)発明者 柴田 正俊 東京都千代田区丸の内二丁目5番1号 三菱重工業株式会社内 (56)参考文献 特開 平8−312905(JP,A) 特開 平6−10621(JP,A) 特開 平6−82003(JP,A) 特開 平4−116306(JP,A) 特開 昭62−196506(JP,A) 実開 昭61−128510(JP,U) 実開 平1−119803(JP,U) (58)調査した分野(Int.Cl.6,DB名) F01K 23/10 F02C 6/18 F22D 11/00 ────────────────────────────────────────────────── ─── Continued on the front page (72) Inventor Yasuko Osawa 2-5-1 Marunouchi, Chiyoda-ku, Tokyo Inside Mitsubishi Heavy Industries, Ltd. (72) Inventor Masatoshi Shibata 2-5-1 Marunouchi, Chiyoda-ku, Tokyo Mitsubishi Heavy Industries (56) References JP-A-8-312905 (JP, A) JP-A-6-10621 (JP, A) JP-A-6-82003 (JP, A) JP-A-4-116306 (JP, A) A) JP-A-62-196506 (JP, A) JP-A-61-128510 (JP, U) JP-A-1-119803 (JP, U) (58) Fields investigated (Int. Cl. 6 , DB name) ) F01K 23/10 F02C 6/18 F22D 11/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ガスタービンの排気をボイラ火炉の燃焼
用空気として用いるとともに、タービン抽気で加熱する
給水加熱器の系統とは別に上記ボイラ火炉の排ガスによ
ってボイラ給水を加熱する複数のガス給水加熱器を直列
に設置したガスタービン排気再燃複合プラントにおい
て、給水が上記ガス給水加熱器および給水加熱器をそれ
ぞれバイパスするバイパスラインと、上流側の上記ガス
給水加熱器の出口から入口へ給水の一部を戻す給水循環
ラインと、同給水循環ラインに設けられた給水循環ポン
プとを備えたことを特徴とするガスタービン排気再燃複
合プラント。
An exhaust gas from a gas turbine is used as combustion air for a boiler furnace and heated by turbine bleed.
Separately from the feedwater heater system, in a gas turbine exhaust reburning combined plant in which a plurality of gas feedwater heaters for heating boiler feedwater by the exhaust gas from the boiler furnace are installed in series, the feedwater uses the gas feedwater heater and the feedwater heater. A bypass line for bypassing, a feedwater circulation line for returning a part of feedwater from an outlet of the gas feedwater heater on the upstream side to an inlet, and a feedwater circulation pump provided in the feedwater circulation line. Gas turbine exhaust reburn complex plant.
【請求項2】 ガスタービンの排気をボイラ火炉の燃焼
用空気として用いるとともに、タービン抽気で加熱する
給水加熱器の系統とは別に上記ボイラ火炉の排ガスによ
ってボイラ給水を加熱する複数のガス給水加熱器を直列
に設置したガスタービン排気再燃複合プラントにおい
て、上記複数のガス給水加熱器の間の給水ラインに設け
られた脱気器と、同脱気器の圧力を上記ガス給水加熱器
の入口温度が所要の温度になる圧力まで昇圧して同脱気
器の出口の給水の一部を上流側の上記ガス給水加熱器の
入口へ戻す脱気器循環ラインと、同脱気器循環ラインに
設けられた脱気器循環ポンプとを備えたことを特徴とす
るガスタービン排気再燃複合プラント。
2. The exhaust gas of a gas turbine is used as combustion air for a boiler furnace and is heated by turbine extraction.
In a gas turbine exhaust reburn complex plant in which a plurality of gas feed water heaters for heating boiler feed water by exhaust gas from the boiler furnace separately from the feed water heater system, a feed line between the plurality of gas feed water heaters A deaerator provided in the gas supply water heater and the pressure of the deaerator
A deaerator circulation line that raises the inlet temperature of the gas to a required temperature and returns a part of the feedwater at the outlet of the deaerator to the inlet of the gas feedwater heater on the upstream side; A combined gas turbine exhaust reburn plant comprising a deaerator circulation pump provided in a line.
JP20433895A 1995-08-10 1995-08-10 Gas turbine exhaust reburn complex plant Expired - Fee Related JP2961073B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20433895A JP2961073B2 (en) 1995-08-10 1995-08-10 Gas turbine exhaust reburn complex plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20433895A JP2961073B2 (en) 1995-08-10 1995-08-10 Gas turbine exhaust reburn complex plant

Publications (2)

Publication Number Publication Date
JPH0953415A JPH0953415A (en) 1997-02-25
JP2961073B2 true JP2961073B2 (en) 1999-10-12

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP20433895A Expired - Fee Related JP2961073B2 (en) 1995-08-10 1995-08-10 Gas turbine exhaust reburn complex plant

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