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JPH0331899B2 - - Google Patents
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JPH0331899B2 - - Google Patents

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Publication number
JPH0331899B2
JPH0331899B2 JP59155197A JP15519784A JPH0331899B2 JP H0331899 B2 JPH0331899 B2 JP H0331899B2 JP 59155197 A JP59155197 A JP 59155197A JP 15519784 A JP15519784 A JP 15519784A JP H0331899 B2 JPH0331899 B2 JP H0331899B2
Authority
JP
Japan
Prior art keywords
gas turbine
air
load
compressor
combustion
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP59155197A
Other languages
Japanese (ja)
Other versions
JPS6134322A (en
Inventor
Isao Sato
Yoji Ishibashi
Takashi Oomori
Shigeyuki Akatsu
Katsuo Wada
Fumio Kato
Yorihide Segawa
Yoshihiro Uchama
Michio Kuroda
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP15519784A priority Critical patent/JPS6134322A/en
Publication of JPS6134322A publication Critical patent/JPS6134322A/en
Publication of JPH0331899B2 publication Critical patent/JPH0331899B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02CGAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
    • F02C9/00Controlling gas-turbine plants; Controlling fuel supply in air- breathing jet-propulsion plants
    • F02C9/48Control of fuel supply conjointly with another control of the plant
    • F02C9/50Control of fuel supply conjointly with another control of the plant with control of working fluid flow

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Exhaust Gas After Treatment (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明はガスタービン装置に関する。特にガス
タービン排ガス中に含有する窒素酸化物(NOx)
や一酸化炭素(CO)、炭化水素(HC)などの未
燃焼成分の発生を抑えた、低公害で、高燃焼効率
のガスタービン装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a gas turbine device. Especially nitrogen oxides (NOx) contained in gas turbine exhaust gas.
This relates to low-pollution, high-combustion efficiency gas turbine equipment that suppresses the generation of unburned components such as carbon monoxide (CO) and hydrocarbons (HC).

〔発明の背景〕[Background of the invention]

ガスタービンは高温、高圧力化を図ることによ
り高効率化の傾向にあると同時に、低公害、高燃
焼効率化を得ることが必須条件となつている。こ
の場合、ガスタービン排ガス中に含まれる物質の
内、NOxやCOが大気汚染公害の対象となり、一
方、COやHCの抑制が、燃焼効率向上を大きく左
右する。したがつて、ガスタービンでは高効率化
とともに低公害、燃焼効率向上化を同時に行うこ
とが必要であるが、高温度、高圧力化に伴い
NOxの生成は多くなり、しかし一方、NOxの発
生を抑制しようとすればCO、HCの生成が多くな
る。このように矛盾した関係となつているので、
これらを同時に解消するのは非常にむずかしい技
術である。従来技術ではまず、燃焼器でのNOx
生成を抑える手段として、空気過剰による低温燃
焼を行ない、さらに排気ダクトにNOxの還元触
媒層を設置して排気されるNOx濃度を大幅に低
減している。しかしながらガスタービンでは、着
火から定格負荷までの広範囲にわたつて低NOx
化と高燃焼性能とを同時に維持することはむずか
しい。範囲が広いので各々条件が異なつているか
らである。とくに低負荷時における燃焼状態は、
過度の空気過剰となるため燃焼が阻害され、CO
やHCなどの未燃焼成分の生成が多くなる。さら
に低負荷時では排ガスの温度が低下するため脱硝
触媒の効率が低下し、したがつて大気中に排出さ
れるNOx濃度は低減されない。この様子を図を
用いて説明する。
Gas turbines tend to become more efficient by increasing the temperature and pressure, and at the same time, it is essential to achieve low pollution and high combustion efficiency. In this case, among the substances contained in gas turbine exhaust gas, NOx and CO are the targets of air pollution, and on the other hand, suppressing CO and HC has a large effect on improving combustion efficiency. Therefore, in gas turbines, it is necessary to simultaneously improve efficiency, reduce pollution, and improve combustion efficiency, but as temperatures and pressures increase,
The production of NOx increases, but on the other hand, if attempts are made to suppress the production of NOx, the production of CO and HC will increase. Because of this contradictory relationship,
It is a very difficult technique to solve these problems at the same time. In conventional technology, first, NOx in the combustor
As a means of suppressing generation, low-temperature combustion is performed using excess air, and a NOx reduction catalyst layer is installed in the exhaust duct to significantly reduce the concentration of NOx exhausted. However, gas turbines require low NOx over a wide range from ignition to rated load.
It is difficult to simultaneously maintain combustion efficiency and high combustion performance. This is because the range is wide and the conditions are different for each. In particular, the combustion state at low loads is
Combustion is inhibited due to excessive air excess, and CO
The generation of unburned components such as and HC increases. Furthermore, when the load is low, the temperature of the exhaust gas decreases, so the efficiency of the denitration catalyst decreases, and therefore the concentration of NOx emitted into the atmosphere is not reduced. This situation will be explained using a diagram.

第1図にガスタービンの主要構成を示す。ガス
タービンは空気圧縮機1、燃焼器2およびタービ
ン3から成り、タービン3を通過した排ガス4は
触媒層5を通過し、あるいは場合によつてはこの
後に排熱回収用のボイラが取付られて、大気中に
放出される。公害発生の要因となるNOxは燃焼
器2で生成されるものであり、その生成は燃焼時
のガス温度によつて大きく左右されるものである
から、燃焼領域6の温度を低く抑える過剰空気に
よる燃焼、いわゆる低温度燃焼法によつて低
NOx化を図つている。さらに大気中へ排出する
NOx量をさらに低く抑えるための触媒層5を設
置している。最終的にはガスタービンのすべての
運転負荷範囲において、NOx量を10〜15ppm以
下に抑えておくことが要求されている。しかしな
がら従来技術では、低負荷時にとくに問題があ
る。つまりガスタービン負荷に対するNOx濃度
は第2図のM線に示すようにガスタービン出口で
は負荷上昇とともに上昇するが、これはガスター
ビン出口において排ガスが空気で希釈される効果
が加わつたデータであるため、この効果をなくす
ため排ガスは一定の酸素濃度(15%)に換算する
ことが必要である。このように補正すると、
NOx濃度は第2図のN線の如くなる。N線に示
されるように、とくに低負荷時では希釈効果によ
る補正でNOx濃度は約4倍に増加する。一方、
低負荷時では排ガス温度低下により脱硝効率も低
下するため、排気されるNOx濃度はL線に示す
ように定格負荷時よりも上昇し、さらに規制値以
上になるという問題がある。すなわち50%以下の
負荷範囲において第3図に示すように排ガス温度
(C線)が負荷の低下と共に低くなることに起因
し、脱硝効率(D線)が低下してしまうのであ
る。これは第4図に示すように低負荷から定格負
荷までは燃焼器に供給される空気量(A実線)が
一定であり、かつ負荷変化により燃焼流量(B点
線)が変わるので、とくに燃料流量が少ない低負
荷時において排ガス温度が低くなり、このため脱
硝効率が低下するものである。結居従来技術では
NOx濃度を規制値以下に抑えることが困難にな
つている。又、負荷によらず、空気流量が一定で
しかも燃焼器において生成するNOxを抑えるた
めNOx排出の多い定格負荷時を基準にして空気
過剰の燃焼を行なうということは、低負荷時にお
いては約定格負荷時の4倍の空気過剰となる(こ
れは空気流量一定で燃料流量のみが変化するため
に生ずる)。よつてこの場合過度の低温度燃焼と
なり、燃焼が阻害され、この結果、COやHCなど
の末燃焼成分の発生が多くなり、燃焼効率低下も
生ずるものである。
Figure 1 shows the main configuration of the gas turbine. The gas turbine consists of an air compressor 1, a combustor 2, and a turbine 3, and the exhaust gas 4 that has passed through the turbine 3 passes through a catalyst layer 5, or in some cases, a boiler for exhaust heat recovery is installed after this. , released into the atmosphere. NOx, which causes pollution, is generated in the combustor 2, and its generation is greatly affected by the gas temperature during combustion. combustion, so-called low-temperature combustion method
Efforts are being made to reduce NOx. further emitted into the atmosphere
A catalyst layer 5 is installed to further suppress the amount of NOx. Ultimately, it is required to keep the amount of NOx below 10 to 15 ppm over the entire operating load range of the gas turbine. However, the prior art is particularly problematic at low loads. In other words, the NOx concentration relative to the gas turbine load increases as the load increases at the gas turbine outlet, as shown by the M line in Figure 2, but this is because the data includes the effect that the exhaust gas is diluted with air at the gas turbine outlet. In order to eliminate this effect, it is necessary to convert the exhaust gas to a constant oxygen concentration (15%). When corrected like this,
The NOx concentration is as shown by the N line in Figure 2. As shown in the N line, especially at low loads, the NOx concentration increases approximately four times due to the correction due to the dilution effect. on the other hand,
When the load is low, the denitrification efficiency also decreases due to the decrease in exhaust gas temperature, so the concentration of NOx exhausted increases from the rated load, as shown by the L line, and even exceeds the regulation value. That is, in a load range of 50% or less, as shown in FIG. 3, the exhaust gas temperature (C line) decreases as the load decreases, and the denitrification efficiency (D line) decreases. This is because, as shown in Figure 4, the amount of air supplied to the combustor (solid line A) is constant from low load to rated load, and the combustion flow rate (dotted line B) changes as the load changes. The exhaust gas temperature becomes low at low load when the amount of gas is low, and therefore the denitrification efficiency decreases. YuiWith conventional technology
It is becoming difficult to keep NOx concentrations below regulatory limits. In addition, regardless of the load, the air flow rate is constant and in order to suppress NOx generated in the combustor, combustion with excess air is performed based on the rated load when NOx emissions are high. The air excess is four times that under load (this occurs because the air flow rate is constant and only the fuel flow rate changes). Therefore, in this case, combustion occurs at an excessively low temperature and combustion is inhibited, resulting in increased generation of end-combustion components such as CO and HC, and a decrease in combustion efficiency.

〔発明の目的〕[Purpose of the invention]

本発明の目的は、ガスタービン低負荷運転範囲
においても触媒による脱硝効率を低下させず低
NOx化を図り、しかも低負荷時における燃焼効
率向上を行ない未燃焼成分の発生を抑えることが
できるガスタービン装置を提供することである。
The purpose of the present invention is to reduce the denitrification efficiency of the catalyst without reducing the denitrification efficiency even in the gas turbine low load operating range.
It is an object of the present invention to provide a gas turbine device capable of reducing NOx, improving combustion efficiency at low loads, and suppressing the generation of unburned components.

〔発明の概要〕[Summary of the invention]

本発明は、低負荷時において燃焼器に導入され
る空気流量を調節することにより、触媒の性能低
下を防止することによつて、上記目的を達成する
ものである。この構成を用いて、低負荷時に燃焼
器に導入される空気流量を抑えるようにすれば、
これにより低負荷時においても排ガス温度を低下
させず脱硝効率低下を抑えることができ、よつて
排ガス中のNOx濃度の大幅低減を図ることがで
きる。かつ空気流量を抑えることにより、過度の
空気過剰による低温度燃焼を解消することができ
るため、低負荷時の燃焼効率向上を図ることがで
きるものである。
The present invention achieves the above object by regulating the flow rate of air introduced into the combustor during low load to prevent deterioration in catalyst performance. If this configuration is used to suppress the air flow rate introduced into the combustor at low loads,
This makes it possible to suppress a decrease in denitrification efficiency without lowering the exhaust gas temperature even under low load conditions, thereby making it possible to significantly reduce the NOx concentration in the exhaust gas. In addition, by suppressing the air flow rate, it is possible to eliminate low-temperature combustion caused by an excessive excess of air, and therefore it is possible to improve combustion efficiency at low loads.

〔発明の実施例〕[Embodiments of the invention]

本発明の一実施例を第5図に示す。このガスタ
ービン装置は、圧縮機1とタービン3と燃焼器2
とを備えるとともに、排ガス通路部に窒素酸化物
の除去のための脱硝触媒層5を設置して成る。本
発明においては、圧縮機のインレツトガイドベー
ンにより、もしくは圧縮機への空気流入路に設け
た流量制御弁により、もしくはその双方を併用す
ることによりガスタービン低負荷時に燃焼器へ流
入する空気量を調節するものであるが、本実施例
では、圧縮機1のインレツト部7に空気8の流量
コントロールが可能な空気流量制御装置9を設置
し、これに制御器10を介し空気流量の制御を行
う構成としている。勿論、場合によつては、圧縮
機1前段に装着されているインレツトガイドベー
ン11によるか、あるいはガイドベーン11と流
量制御装置9とを併合して動作させることもあり
得る。又、圧縮機1の途中段から空気12を抽気
し、これをコントロールするバルブ13を設置
し、空気は触媒層5を通過するガス温度の低下を
防ぐため触媒層5の後流へ導入する構成とするこ
ともできる。
An embodiment of the present invention is shown in FIG. This gas turbine device includes a compressor 1, a turbine 3, and a combustor 2.
In addition, a denitrification catalyst layer 5 for removing nitrogen oxides is installed in the exhaust gas passage. In the present invention, the amount of air flowing into the combustor during low load of the gas turbine is controlled by an inlet guide vane of the compressor, a flow control valve provided in the air inflow path to the compressor, or a combination of both. In this embodiment, an air flow rate control device 9 capable of controlling the flow rate of air 8 is installed in the inlet section 7 of the compressor 1, and the air flow rate is controlled via a controller 10. It is configured to do so. Of course, depending on the case, the operation may be performed by the inlet guide vane 11 installed at the front stage of the compressor 1, or by combining the guide vane 11 and the flow rate control device 9. In addition, air 12 is extracted from an intermediate stage of the compressor 1, a valve 13 is installed to control this, and the air is introduced downstream of the catalyst layer 5 in order to prevent the temperature of the gas passing through the catalyst layer 5 from decreasing. It is also possible to do this.

空気流量の調整は次のように行なう。すなわち
空気流量調整は第4図に示すように無負荷近傍か
ら50%負荷近傍まで行い、図中のI線に示すよう
に負荷上昇とともに可変コントロールする。この
時燃料流量はJ線に示すように従来の制御と大差
ないが、このように空気流量を可変にすることに
より、燃焼器の燃焼状態は、空気流量がA線から
I線に減少する条件となる。このため低負荷時に
過度の空気過剰燃焼が防がれることになる。それ
ばかりでなく、タービン排気温度は第3図に示す
C線からK点線に示すように、無負荷から50%負
荷時の間は50%負荷相当時の排ガス温度を約400
℃に保つことができる。このため脱硝効率は、第
6図の従来技術(E線)に示す如き低負荷時にお
いて低下するという傾向はなくなり、排気温度が
上るためむしろG点線に示すように脱硝効率は向
上する。この結果NOx濃度は、低負荷時に高濃
度を呈する従来技術F線に比べ、低負荷時におい
てとくに増加するという傾向はなくなり、却つて
脱硝効率が向上する。したがつて第6図のH線に
示すように、全負荷範囲において15ppm以下の
NOx濃度に抑えることが出来る。
Adjust the air flow rate as follows. That is, the air flow rate is adjusted from near no load to near 50% load as shown in FIG. 4, and is variably controlled as the load increases as shown by line I in the figure. At this time, the fuel flow rate is not much different from conventional control as shown in the J line, but by making the air flow rate variable in this way, the combustion state of the combustor is changed to the condition where the air flow rate decreases from the A line to the I line. becomes. This prevents excessive air combustion during low loads. In addition, as shown in the dotted line C to K in Figure 3, the turbine exhaust temperature is approximately 400% lower than the exhaust gas temperature equivalent to 50% load from no load to 50% load.
Can be kept at ℃. Therefore, the denitrification efficiency does not tend to decrease at low loads as shown in the prior art (line E) in FIG. 6, but rather increases as the exhaust temperature increases as shown in the dotted line G. As a result, the NOx concentration does not tend to increase particularly at low loads, compared to the conventional F-line which exhibits a high concentration at low loads, and on the contrary, the denitrification efficiency improves. Therefore, as shown by the H line in Figure 6, the
NOx concentration can be suppressed.

このように低負荷時に燃焼器へ供給される空気
流量を減少することによつて脱硝性の低下を抑え
ることができるものであるが、この場合の空気流
量の減少量は、無負荷時において定格負荷時の約
50%程度にしておき、負荷上昇と共に燃料流量と
空気流量を増加し、50%負荷時にほぼ定格負荷時
の空気流量となるように流量制御することが望ま
しい。このようにすると、無負荷時から50%負荷
時までの燃焼状態をほぼ等しい状態にすることが
できる。これは、インレツトのガイドベーン11
による制御にすると、ベーン角度30°以上の制御
となる。
In this way, by reducing the air flow rate supplied to the combustor at low loads, it is possible to suppress the deterioration of denitrification performance, but the amount of decrease in air flow rate in this case is less than the rated value at no load. Approximately at load
It is desirable to keep it at about 50%, increase the fuel flow rate and air flow rate as the load increases, and control the flow rate so that at 50% load, the air flow rate is approximately the same as at the rated load. In this way, the combustion state can be made almost equal from no load to 50% load. This is the guide vane 11 of the inlet.
If the control is controlled by , the vane angle will be controlled at 30° or more.

したがつて、無負荷時の燃焼状態は50%負荷時
の燃焼状態にほほ等しくなるため、従来技術のよ
うな過度の空気過剰による低温度燃焼とはなら
ず、よつてCOやHC等の未燃焼生成分の生成が少
なくなり、燃焼性能が向上し、燃焼効率の向上も
なし得るという効果を得られる。
Therefore, the combustion state at no load is almost the same as the combustion state at 50% load, so low-temperature combustion due to excessive air excess does not occur as in the conventional technology, and the combustion state does not result in the combustion of CO, HC, etc. It is possible to obtain the effects that the generation of combustion products is reduced, combustion performance is improved, and combustion efficiency can also be improved.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、低負荷時から高負荷時にわた
り、脱硝効率を向上させ、かつ燃焼性能を向上す
ることができる効果がある。
According to the present invention, it is possible to improve denitrification efficiency and combustion performance from low load to high load.

なお当然のことではあるが、本発明は図示の実
施例にのみ限定されるものではない。
It should be noted that, as a matter of course, the present invention is not limited to the illustrated embodiment.

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

第1図は従来形ガスタービン装置を示す構成図
である。第2図は、タービン負荷とNOx濃度の
関係を示す特性図である。第3図はタービン負荷
とガス温度および脱硝効率の関係を示す特性図で
ある。第4図はガスタービン負荷と空気、燃料流
量の関係を示すもので、従来技術および本発明の
一実施例によるデータとを比較して示す図であ
る。第5図は本発明の一実施例に係るガスタービ
ン装置を示す構成図である。第6図は本実施例と
従来技術との脱硝効率およびNOx濃度特性の比
較図である。 1……圧縮機、2……燃焼器、3……タービ
ン、5……脱硝触媒層、7……インレツト部、9
……空気流量制御装置、11……インレツトガイ
ドベーン、12……抽気配管、13……抽気バル
ブ。
FIG. 1 is a block diagram showing a conventional gas turbine device. FIG. 2 is a characteristic diagram showing the relationship between turbine load and NOx concentration. FIG. 3 is a characteristic diagram showing the relationship between turbine load, gas temperature, and denitrification efficiency. FIG. 4 shows the relationship between the gas turbine load and the air and fuel flow rates, and is a diagram comparing data from the prior art and an embodiment of the present invention. FIG. 5 is a configuration diagram showing a gas turbine device according to an embodiment of the present invention. FIG. 6 is a comparison diagram of the denitrification efficiency and NOx concentration characteristics between this example and the conventional technology. DESCRIPTION OF SYMBOLS 1... Compressor, 2... Combustor, 3... Turbine, 5... Denitration catalyst layer, 7... Inlet part, 9
... Air flow control device, 11 ... Inlet guide vane, 12 ... Air bleed piping, 13 ... Air bleed valve.

Claims (1)

【特許請求の範囲】 1 ガスタービンと、該ガスタービンに駆動され
空気を圧縮する圧縮機と、該圧縮機からの圧縮空
気のもとで燃料を燃焼し燃焼ガスを前記ガスター
ビンに供給する燃焼器と、前記ガスタービンの排
気ガス通路に設けた窒素酸化物除去用の脱硝触媒
装置とを備えるガスタービン装置において、前記
圧縮機に流入する空気量を調整するインレツトガ
イドベーンと、前記圧縮機の途中段から吐出する
空気を前記脱硝装置の後流に逃がす抽気配管と、
該抽気配管の途中に設けられ抽気量を調整する抽
気弁とを備えることを特徴とする低公害ガスター
ビン装置。 2 ガスタービンと、該ガスタービンに駆動され
空気を圧縮する圧縮機と、該圧縮機からの圧縮空
気のもとで燃料を燃焼し燃焼ガスを前記ガスター
ビンに供給する燃焼器と、前記ガスタービンの排
気ガス通路に設けた窒素酸化物除去用の脱硝触媒
装置とを備えるガスタービン装置において、前記
圧縮機に流入する空気量を調整するインレツトガ
イドベーンと、前記圧縮機の最終段から吐出する
空気を前記脱硝装置の後流に逃がす抽気配管と、
該抽気配管の途中に設けられ抽気量を調整する抽
気弁とを備えることを特徴とする低公害ガスター
ビン装置。
[Claims] 1. A gas turbine, a compressor that is driven by the gas turbine and compresses air, and a combustion system that combusts fuel under the compressed air from the compressor and supplies combustion gas to the gas turbine. and a denitrification catalyst device for removing nitrogen oxides provided in an exhaust gas passage of the gas turbine, the gas turbine device comprising: an inlet guide vane that adjusts the amount of air flowing into the compressor; bleed air piping that releases air discharged from an intermediate stage of the denitrification device to the downstream side of the denitrification device;
A low-pollution gas turbine device comprising: a bleed valve provided in the middle of the bleed pipe to adjust an amount of bleed air. 2. A gas turbine, a compressor that is driven by the gas turbine and compresses air, a combustor that combusts fuel under compressed air from the compressor and supplies combustion gas to the gas turbine, and the gas turbine. A gas turbine device comprising: a denitrification catalyst device for removing nitrogen oxides provided in an exhaust gas passage; an inlet guide vane for adjusting the amount of air flowing into the compressor; a bleed pipe that releases air to the downstream side of the denitrification device;
A low-pollution gas turbine device comprising: a bleed valve provided in the middle of the bleed pipe to adjust an amount of bleed air.
JP15519784A 1984-07-27 1984-07-27 Low environmental-pollution type gas turbine Granted JPS6134322A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15519784A JPS6134322A (en) 1984-07-27 1984-07-27 Low environmental-pollution type gas turbine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15519784A JPS6134322A (en) 1984-07-27 1984-07-27 Low environmental-pollution type gas turbine

Publications (2)

Publication Number Publication Date
JPS6134322A JPS6134322A (en) 1986-02-18
JPH0331899B2 true JPH0331899B2 (en) 1991-05-09

Family

ID=15600617

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15519784A Granted JPS6134322A (en) 1984-07-27 1984-07-27 Low environmental-pollution type gas turbine

Country Status (1)

Country Link
JP (1) JPS6134322A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2680033B2 (en) * 1988-05-11 1997-11-19 株式会社日立製作所 Method and apparatus for operating combined plant
KR101981647B1 (en) * 2014-11-27 2019-05-24 한화파워시스템 주식회사 Control system for compressor

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5545739A (en) * 1978-09-29 1980-03-31 Japan Crown Cork Co Ltd Bonding of polyolefin liner to metallic crown cap
JPS56101025A (en) * 1980-01-18 1981-08-13 Hitachi Ltd System for controlling guide vane at air inlet of gas turbine
US4353207A (en) * 1980-08-20 1982-10-12 Westinghouse Electric Corp. Apparatus for removing NOx and for providing better plant efficiency in simple cycle combustion turbine plants

Also Published As

Publication number Publication date
JPS6134322A (en) 1986-02-18

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