JPH06108877A - Gas turbine single power generation system - Google Patents

Gas turbine single power generation system

Info

Publication number
JPH06108877A
JPH06108877A JP28050392A JP28050392A JPH06108877A JP H06108877 A JPH06108877 A JP H06108877A JP 28050392 A JP28050392 A JP 28050392A JP 28050392 A JP28050392 A JP 28050392A JP H06108877 A JPH06108877 A JP H06108877A
Authority
JP
Japan
Prior art keywords
gas turbine
power generation
generation system
denitration device
gas
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.)
Withdrawn
Application number
JP28050392A
Other languages
Japanese (ja)
Inventor
Isao Nishimura
功 西村
Takafuru Kobayashi
敬古 小林
Toshikazu Ikegami
寿和 池上
Kenichi Irie
健一 入江
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP28050392A priority Critical patent/JPH06108877A/en
Publication of JPH06108877A publication Critical patent/JPH06108877A/en
Withdrawn legal-status Critical Current

Links

Abstract

PURPOSE:To reduce the amount of exhausted NOX, and to provide high output and high efficiency even when a gas turbine is provided in a single manner. CONSTITUTION:In a gas turbine single power generation system provided with a denitration device 7 for removing NOX out of a combustion exhaust gas exhausted from a singly provided gas turbine 4, an exhaust heat recovery boiler 6 for cooling the exhaust gas is provided between the gas turbine 4 and the denitration device 7. A steam injection system 8 for injecting all of the steam generated by the exhaust heat recovery boiler 6 into a gas turbine combustor 3, is provided. Denitration is carried out by means of high temperature catalyst by the denitration device 7.

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、ガスタービン単独発電
システムに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a gas turbine independent power generation system.

【0002】[0002]

【従来の技術】ガスタービン単独で発電を行うと、窒素
酸化物(以下NOという)量の問題や経済性の問題が
起こってくる。しかし、非常用などの発電がどうしても
必要になる場合があり、このような場合の対応策として
は比較的運用が容易なガスタービン単独発電システムを
採ることが望ましい。
2. Description of the Related Art When a gas turbine alone is used to generate electric power, problems such as the amount of nitrogen oxides (hereinafter referred to as NO X ) and economic problems arise. However, there is a case where it is absolutely necessary to generate power for emergency use, and it is desirable to adopt a gas turbine independent power generation system that is relatively easy to operate as a countermeasure in such cases.

【0003】[0003]

【発明が解決しようとする課題】しかし、ガスタービン
を単独で設置するときに問題となる1つに、前述した如
く、ガスタービンで生成されるNOによる環境問題が
ある。このため、NO量を低減させるための対策をと
る必要がある。そして、高効率のガスタービンを単独で
設置する場合に、NOを低減させる上で考慮する必要
がある事項として次の点がある。
However, one of the problems when the gas turbine is installed alone is an environmental problem due to NO X generated in the gas turbine as described above. Therefore, it is necessary to take measures to reduce the NO X amount. Then, when a high-efficiency gas turbine is independently installed, there are the following points that need to be considered in order to reduce NO X.

【0004】(1)排ガス温度が高い:ガスタービンか
ら排出される燃焼排ガス中からNOを除去する脱硝装
置を設置するにしても、脱硝装置の触媒の適用温度に制
限があり(通常300℃〜400℃)、したがって従来
一般的に用いられている触媒は使用できない。このた
め、改良形の高温触媒を使用するとしても、高脱硝率を
得るには、ガスタービンと脱硝装置との間で排ガスの温
度を数十℃〜数百℃程度低減する必要がある。
(1) Exhaust gas temperature is high: Even if a denitration device that removes NO X from the combustion exhaust gas discharged from the gas turbine is installed, there is a limit to the applicable temperature of the catalyst of the denitration device (usually 300 ° C.). ˜400 ° C.), and therefore the conventionally commonly used catalysts cannot be used. For this reason, even if the improved high-temperature catalyst is used, it is necessary to reduce the temperature of the exhaust gas between the gas turbine and the denitration device by several tens to several hundreds of degrees Celsius in order to obtain a high denitration rate.

【0005】なお、コンバインドプラントの場合は、触
媒の運用温度の問題を解決するために、排熱回収ボイラ
の適正温度域に脱硝装置を設置している。
In the case of a combined plant, in order to solve the problem of the operating temperature of the catalyst, a denitration device is installed in the proper temperature range of the exhaust heat recovery boiler.

【0006】(2)高脱硝率を必要とする:ガスタービ
ンの出力が大きいので、排ガス量が多い。したがって、
地域の環境保全上排出NO量を低く抑える必要があ
る。
(2) High denitrification rate is required: Since the output of the gas turbine is large, the amount of exhaust gas is large. Therefore,
It is necessary to keep the amount of NO X emitted low in order to protect the local environment.

【0007】本発明は、このようなガスタービン単独設
置の場合における問題を解決するためになされたもの
で、ガスタービンを単独で設置しても、NO排出量を
極めて少なくすることができ、しかも高出力・高効率が
得られる発電システムを提供することを目的とする。
The present invention has been made to solve the problem in the case of installing such a gas turbine alone. Even if the gas turbine is installed alone, the NO X emission amount can be extremely reduced, Moreover, it is an object of the present invention to provide a power generation system that can obtain high output and high efficiency.

【0008】[0008]

【課題を解決するための手段】上記の課題を解決するた
めに、本発明は、ガスタービンから排出される燃焼排ガ
ス中からNOを除去する脱硝装置を備えたガスタービ
ン単独発電システムにおいて、前記ガスタービンと前記
脱硝装置との間に排ガス冷却用の排熱回収ボイラを設置
すると共に、この排熱回収ボイラで発生した蒸気のすべ
てをガスタービン燃焼器内に噴射する蒸気噴射系統を設
けたものである。
In order to solve the above problems, the present invention provides a gas turbine single power generation system including a denitration device for removing NO x from combustion exhaust gas discharged from a gas turbine, wherein An exhaust heat recovery boiler for exhaust gas cooling is installed between the gas turbine and the denitration device, and a steam injection system for injecting all of the steam generated in the exhaust heat recovery boiler into the gas turbine combustor is provided. Is.

【0009】[0009]

【作用】上記の手段によれば、排熱回収ボイラで自己排
ガスの回収熱により蒸気を発生させ、その蒸気をガスタ
ービン燃焼器内に噴射することで、火炎温度が降下し、
NO生成量を抑えることができる。また、蒸気噴射分
だけ排ガス流量が増すので、ガスタービンの出力が増
す。更に、排ガスが持っている熱を有効に利用できるこ
とにより、高効率となる。
According to the above means, the exhaust heat recovery boiler generates steam by the heat of recovery of its own exhaust gas and injects the steam into the gas turbine combustor, whereby the flame temperature is lowered,
The amount of NO X produced can be suppressed. Moreover, since the exhaust gas flow rate increases by the amount of steam injection, the output of the gas turbine increases. Furthermore, the heat of the exhaust gas can be effectively used, resulting in high efficiency.

【0010】[0010]

【実施例】以下、図面を参照して本発明の実施例につい
て詳細に説明する。図1は本発明に係るガスタービン単
独発電システムの一実施例を示す系統図である。
Embodiments of the present invention will now be described in detail with reference to the drawings. FIG. 1 is a system diagram showing an embodiment of a gas turbine single power generation system according to the present invention.

【0011】図1において、1は単独設置のガスタービ
ン発電装置であり、空気圧縮機2、ガスタービン燃焼器
3、ガスタービン4及び発電機5により構成される。す
なわち、ガスタービン燃焼器3には燃料と圧縮機2で圧
縮された空気とが供給されて燃焼し、その燃焼ガスがガ
スタービン4に導入され、これにより発電機5が駆動さ
れるようになっている。
In FIG. 1, reference numeral 1 is a gas turbine power generator installed independently, and is composed of an air compressor 2, a gas turbine combustor 3, a gas turbine 4 and a generator 5. That is, the fuel and the air compressed by the compressor 2 are supplied to the gas turbine combustor 3 and burned, and the combustion gas is introduced into the gas turbine 4, whereby the generator 5 is driven. ing.

【0012】また、ガスタービン4からの排ガスを脱硝
装置入口適温まで冷却するための排熱回収ボイラ6が、
ガスタービン4と高温触媒による脱硝装置7との間に設
置されている。そして、この排熱回収ボイラ6で発生し
た蒸気のすべてをガスタービン燃焼器3内に噴射する蒸
気噴射系統8が設けられている。なお、9は煙突であ
る。
Further, an exhaust heat recovery boiler 6 for cooling the exhaust gas from the gas turbine 4 to a proper temperature at the inlet of the denitration device,
It is installed between the gas turbine 4 and the denitration device 7 using a high temperature catalyst. A steam injection system 8 for injecting all of the steam generated in the exhaust heat recovery boiler 6 into the gas turbine combustor 3 is provided. In addition, 9 is a chimney.

【0013】このように、単独設置のガスタービン4と
脱硝装置7との間に排熱回収ボイラ6を設け、この部分
で自己排ガス回収熱により給水を加熱して蒸気を発生さ
せ、その蒸気をガスタービン燃焼器3内に噴射すること
で、火炎温度が降下し、NO生成量を抑えることがで
きる。また、蒸気噴射分だけ排ガス流量が増すので、ガ
スタービン4の出力が増す。更に、排ガスが持っている
熱を有効に利用できることにより、高効率となる。
As described above, the exhaust heat recovery boiler 6 is provided between the independently installed gas turbine 4 and the denitration device 7, and in this portion, the feed water is heated by the heat of recovery of the self-exhaust gas to generate steam, and the steam is generated. By injecting into the gas turbine combustor 3, the flame temperature drops and the NO X production amount can be suppressed. Further, since the exhaust gas flow rate increases by the amount of steam injection, the output of the gas turbine 4 increases. Furthermore, the heat of the exhaust gas can be effectively used, resulting in high efficiency.

【0014】そして、脱硝装置7で高温触媒により脱硝
を行うことにより、排ガスからの熱回収量が少ないの
で、排熱回収ボイラ6での水使用量がほぼガスタービン
燃焼器3への蒸気噴射分でよく、かつ極めて少ないNO
量にすることができる。
Since the amount of heat recovered from the exhaust gas is small by performing denitration by the high temperature catalyst in the denitration device 7, the amount of water used in the exhaust heat recovery boiler 6 is almost the same as the amount of steam injected to the gas turbine combustor 3. Good and very little NO
It can be an X amount.

【0015】次に、下記の表1は、図1に示した如く本
発明にしたがって排熱回収ボイラ6で発生した蒸気をガ
スタービン燃焼器3内へ噴射したケース、また本発明の
比較して、図2に示すようにガスタービン燃焼器3内へ
蒸気も水も噴射しないケース、及び図3に示すように水
をガスタービン燃焼器3内へ噴射したケースの3ケース
において、それぞれ、出力、効率、NO濃度、脱硝装
置入口NO量、脱硝装置出口NO量、燃料使用量及
び水使用量を比較して表す。なお、図2、図3におい
て、図1に示したものと同一の部分には同一の符号を付
して、重複する説明は省略する。
Next, Table 1 below shows a case in which steam generated in the exhaust heat recovery boiler 6 is injected into the gas turbine combustor 3 according to the present invention as shown in FIG. 1, and a comparison of the present invention. In the case where neither steam nor water is injected into the gas turbine combustor 3 as shown in FIG. 2, and in the case where water is injected into the gas turbine combustor 3 as shown in FIG. efficiency, NO X concentration, denitration unit inlet amount of NO X, denitrator outlet amount of NO X represents by comparing the fuel consumption and water consumption. 2 and 3, the same parts as those shown in FIG. 1 are designated by the same reference numerals, and the duplicated description will be omitted.

【0016】ただし、どのケースについても、大気温度
は35℃、燃料はLNG、排熱回収ボイラ6への給水温
度は30℃とした。また、排熱回収ボイラ6によってガ
スタービン4からの排ガスを500℃まで冷却し、30
kg/cm、350℃の蒸気を発生させるようにし
た。更に、脱硝装置7での脱硝率は90%とした。
However, in all cases, the atmospheric temperature was 35 ° C., the fuel was LNG, and the feed water temperature to the exhaust heat recovery boiler 6 was 30 ° C. Further, the exhaust gas from the gas turbine 4 is cooled to 500 ° C. by the exhaust heat recovery boiler 6,
It was made to generate vapor of kg / cm 2 and 350 ° C. Further, the denitration rate in the denitration device 7 was set to 90%.

【0017】[0017]

【表1】 [Table 1]

【0018】この表1に示す結果より定性的に分かるこ
とは、出力、効率とも蒸気噴射が最も良いこと、及び
水、蒸気を噴射させることでNO生成量は減り、さら
に蒸気噴射の場合は燃料消費量が減るので水噴射よりも
NO生成量は減ることである。したがって、これらの
結果より、蒸気噴射のケースが最も良いシステムである
ことが分かる。
It can be qualitatively understood from the results shown in Table 1 that steam injection has the best output and efficiency, and that the amount of NO X produced decreases by injecting water and steam. Since the fuel consumption amount is reduced, the NO X production amount is reduced as compared with the water injection. Therefore, these results show that the case of steam injection is the best system.

【0019】[0019]

【発明の効果】以上述べたように、本発明によれば、ガ
スタービン単独設置の場合における問題、すなわち排ガ
ス温度が高い及び高脱硝率を必要とする問題を解決し、
ガスタービンを単独で設置しても、NO排出量を極め
て少なくすることができ、しかも高出力・高効率が得ら
れる発電システムを提供することができる。
As described above, according to the present invention, the problems in the case where the gas turbine is installed alone, that is, the problems that the exhaust gas temperature is high and the high denitration rate is required, are solved,
Even if the gas turbine is installed alone, it is possible to provide a power generation system that can significantly reduce the NO X emission amount and can obtain high output and high efficiency.

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

【図1】本発明に係るガスタービン単独発電システムの
一例を示す系統図である。
FIG. 1 is a system diagram showing an example of a gas turbine single power generation system according to the present invention.

【図2】本発明と比較されるガスタービン単独発電シス
テムの一例を示す系統図である。
FIG. 2 is a system diagram showing an example of a gas turbine independent power generation system compared with the present invention.

【図3】本発明と比較されるガスタービン単独発電シス
テムの他の例を示す系統図である。
FIG. 3 is a system diagram showing another example of a gas turbine independent power generation system compared with the present invention.

【符号の説明】[Explanation of symbols]

1 ガスタービン発電装置 2 空気圧縮機 3 ガスタービン燃焼器 4 ガスタービン 5 発電機 6 排熱回収ボイラ 7 脱硝装置 8 蒸気噴射系統 9 煙突 1 gas turbine power generator 2 air compressor 3 gas turbine combustor 4 gas turbine 5 generator 6 exhaust heat recovery boiler 7 denitration device 8 steam injection system 9 chimney

───────────────────────────────────────────────────── フロントページの続き (72)発明者 入江 健一 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 ─────────────────────────────────────────────────── ─── Continued Front Page (72) Inventor Kenichi Irie 2-5-1, Marunouchi, Chiyoda-ku, Tokyo Sanryo Heavy Industries Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】ガスタービンから排出される燃焼排ガス中
から窒素酸化物を除去する脱硝装置を備えたガスタービ
ン単独発電システムにおいて、前記ガスタービンと前記
脱硝装置との間に排ガス冷却用の排熱回収ボイラを設置
すると共に、この排熱回収ボイラで発生した蒸気のすべ
てをガスタービン燃焼器内に噴射する蒸気噴射系統を設
けたことを特徴とするガスタービン単独発電システム。
1. A gas turbine single power generation system comprising a denitration device for removing nitrogen oxides from combustion exhaust gas discharged from a gas turbine, wherein exhaust heat for exhaust gas cooling is provided between the gas turbine and the denitration device. A gas turbine independent power generation system comprising a recovery boiler and a steam injection system for injecting all of the steam generated in the exhaust heat recovery boiler into the gas turbine combustor.
JP28050392A 1992-09-25 1992-09-25 Gas turbine single power generation system Withdrawn JPH06108877A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28050392A JPH06108877A (en) 1992-09-25 1992-09-25 Gas turbine single power generation system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28050392A JPH06108877A (en) 1992-09-25 1992-09-25 Gas turbine single power generation system

Publications (1)

Publication Number Publication Date
JPH06108877A true JPH06108877A (en) 1994-04-19

Family

ID=17626002

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28050392A Withdrawn JPH06108877A (en) 1992-09-25 1992-09-25 Gas turbine single power generation system

Country Status (1)

Country Link
JP (1) JPH06108877A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6502403B1 (en) 2000-04-05 2003-01-07 Kawasaki Jukogyo Kabushiki Kaisha Steam-injection type gas turbine
JP2010025108A (en) * 2008-07-18 2010-02-04 General Electric Co <Ge> Heat pipe for removing thermal energy from exhaust gas
JP2010077930A (en) * 2008-09-26 2010-04-08 Toyota Motor Corp Bleed type gas turbine engine

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6502403B1 (en) 2000-04-05 2003-01-07 Kawasaki Jukogyo Kabushiki Kaisha Steam-injection type gas turbine
JP2010025108A (en) * 2008-07-18 2010-02-04 General Electric Co <Ge> Heat pipe for removing thermal energy from exhaust gas
JP2010077930A (en) * 2008-09-26 2010-04-08 Toyota Motor Corp Bleed type gas turbine engine

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