JP2003056364A - Gas-fired gas turbine power generation equipment - Google Patents
Gas-fired gas turbine power generation equipmentInfo
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- JP2003056364A JP2003056364A JP2001243124A JP2001243124A JP2003056364A JP 2003056364 A JP2003056364 A JP 2003056364A JP 2001243124 A JP2001243124 A JP 2001243124A JP 2001243124 A JP2001243124 A JP 2001243124A JP 2003056364 A JP2003056364 A JP 2003056364A
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Abstract
(57)【要約】
【課題】 低カロリーガス燃料のガス圧縮に伴うエネル
ギーロスを低減し、これにより総発電効率を高めること
ができるガス焚きガスタービン発電設備を提供する。
【解決手段】 ガス燃料1を圧縮前の空気中に可燃限界
以下で噴射する低圧燃料噴射装置18と、燃焼器に追加
燃料6を高圧で噴射する高圧燃料噴射装置19と、燃焼
排ガス中の未燃成分を触媒燃焼させる触媒燃焼器20と
を備える。好ましくは、ガス燃料1は低カロリーガス燃
料であり、追加燃料は液体燃料である。
(57) [Problem] To provide a gas-fired gas turbine power generation equipment capable of reducing energy loss due to gas compression of a low calorie gas fuel and thereby increasing total power generation efficiency. A low-pressure fuel injection device for injecting gaseous fuel 1 into air before compression at a flammable limit or less, a high-pressure fuel injection device for injecting additional fuel 6 at a high pressure into a combustor, A catalytic combustor 20 for catalytically combusting the fuel component. Preferably, gas fuel 1 is a low calorie gas fuel and the additional fuel is a liquid fuel.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、低カロリーガスを
主燃料とするガス焚きガスタービン発電設備に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a gas-fired gas turbine power generation facility using low-calorie gas as a main fuel.
【0002】[0002]
【従来の技術】図2は、従来のガス焚きガスタービン発
電設備の全体構成図である。この図において、10は、
圧縮機11、燃焼器12、タービン13及び発電機14
からなるガスタービン発電機、15はガス圧縮機、16
はガス冷却制御装置、17は熱交換器である。ガス燃料
1は、ガス圧縮機15で加圧(例えば約18気圧)さ
れ、クーラ、オイルセパレータ、流量制御弁等からなる
ガス冷却制御装置16で冷却し流量制御されて高圧(例
えば約12気圧)の燃焼器12内に噴射される。圧縮機
11、タービン13及び発電機14は機械的に連結され
ており、圧縮機11で空気2を圧縮し、燃焼器12で加
圧したガス燃料1を燃焼して燃焼排ガス3を発生させ、
この燃焼排ガス3でタービン13を回転駆動し、その動
力で圧縮機11と発電機14を回転駆動して発電する。
更に、熱交換器17で高温の燃焼排ガス3を冷却して水
蒸気5を発生させ、この水蒸気5を燃焼器12内に噴射
して発電出力を高めるようになっている。なお、この図
で2aは抽気空気、4は冷却水である。2. Description of the Related Art FIG. 2 is an overall configuration diagram of a conventional gas-fired gas turbine power generation facility. In this figure, 10 is
Compressor 11, combustor 12, turbine 13 and generator 14
Gas turbine generator consisting of, 15 is a gas compressor, 16
Is a gas cooling control device, and 17 is a heat exchanger. The gas fuel 1 is pressurized (for example, about 18 atm) by the gas compressor 15, cooled by the gas cooling control device 16 including a cooler, an oil separator, a flow control valve, and the flow rate is controlled to be high pressure (for example, about 12 atm). Is injected into the combustor 12. The compressor 11, the turbine 13, and the generator 14 are mechanically connected to each other. The compressor 11 compresses the air 2 and the combustor 12 burns the pressurized gas fuel 1 to generate a combustion exhaust gas 3.
The combustion exhaust gas 3 drives the turbine 13 to rotate, and the power thereof drives the compressor 11 and the generator 14 to generate power.
Further, the heat exchanger 17 cools the high temperature combustion exhaust gas 3 to generate steam 5, and the steam 5 is injected into the combustor 12 to increase the power generation output. In this figure, 2a is extraction air, and 4 is cooling water.
【0003】[0003]
【発明が解決しようとする課題】上述したようにガス焚
きガスタービン発電設備では、ガス燃料1を燃焼器12
に噴射するために、燃焼器内の圧力(例えば12気圧)
よりも十分に高い圧力(例えは18気圧)まで圧縮する
必要があり、そのためにガス圧縮機15を用いている。
しかし、かかるガス圧縮機15の必要動力は、高カロリ
ーガス燃料(例えば天然ガス)を用いた場合でも、発電
出力(例えば約2000kW)の約5%(約100k
W)に達していた。As described above, in the gas-fired gas turbine power generation facility, the gas fuel 1 is supplied to the combustor 12
Pressure in the combustor (eg 12 atm) to inject
It is necessary to compress to a pressure sufficiently higher than that (for example, 18 atm), and therefore the gas compressor 15 is used.
However, the required power of the gas compressor 15 is about 5% (about 100 k) of the power generation output (eg, about 2000 kW) even when a high-calorie gas fuel (eg, natural gas) is used.
W) has been reached.
【0004】また、ガス圧縮機15で圧縮したガス燃料
の温度は高温(例えば約500℃)であり、かつ圧縮機
オイルを含有する。そのため、そのままでは、ガス冷却
制御装置16を構成するオイルセパレータ、流量制御弁
等が高温に耐えらず、かつそのまま燃焼させるとタービ
ン13を損傷させるおそれがある。そのため、ガス温度
が100℃前後となるまで水冷しかつ、オイルセパレー
タにより圧縮機オイルを除去している。その結果、水冷
によりエネルギーロスと、オイルセパレータでの圧損が
生じるため、ガス圧縮機動力の大半は損失となってしま
う。The temperature of the gas fuel compressed by the gas compressor 15 is high (for example, about 500 ° C.) and contains compressor oil. Therefore, if it is left as it is, the oil separator, the flow rate control valve, and the like that form the gas cooling control device 16 do not withstand high temperatures, and if they are burned as they are, the turbine 13 may be damaged. Therefore, water cooling is performed until the gas temperature reaches around 100 ° C., and the compressor oil is removed by the oil separator. As a result, energy loss and pressure loss in the oil separator occur due to water cooling, and most of the gas compressor power is lost.
【0005】更に、ガス燃料1として、低カロリーガス
燃料を用いる場合には、一般に低カロリーガス燃料はC
O2、蒸気、窒素などの非可燃成分を大量に含んでいる
ため、カロリーが低いほど大量のガスを圧縮し噴射する
ことになるため、圧縮動力が増加し損失が増大する。Further, when a low-calorie gas fuel is used as the gas fuel 1, generally, the low-calorie gas fuel is C
Since it contains a large amount of non-combustible components such as O 2 , steam, and nitrogen, the lower the calorie, the larger the amount of gas that is compressed and injected, so the compression power increases and the loss increases.
【0006】図3は、この関係を示す図であり、横軸は
ガス燃料の発熱量、縦軸はガス圧縮動力と総発電効率で
ある。ガス圧縮動力(右縦軸)はLNGを1とし、総発
電効率は液焚きを1としている。この図からわかるよう
に、ガス焚きガスタービン発電設備では燃焼器にガス噴
射するために、ガス圧縮機を用いており、その動力が大
きいため正味の発電効率は低下し、特にバイオマスガ
ス、汚泥消化ガス等の低カロリーガスを用いる場合に
は、ガス圧縮動力が大幅に増大するため、その損失は発
電出力の数割に達する問題点があった。FIG. 3 is a diagram showing this relationship, in which the horizontal axis represents the calorific value of gas fuel, and the vertical axis represents gas compression power and total power generation efficiency. The gas compression power (right vertical axis) has LNG of 1, and the total power generation efficiency has liquid burning of 1. As can be seen from this figure, the gas-fired gas turbine power generation equipment uses a gas compressor to inject gas into the combustor, and its large power reduces the net power generation efficiency, especially biomass gas and sludge digestion. When a low-calorie gas such as gas is used, the gas compression power is significantly increased, so that there is a problem that the loss reaches several percent of the power generation output.
【0007】本発明はかかる問題点を解決するために創
案されたものである。すなわち、本発明の目的は、低カ
ロリーガス燃料のガス圧縮に伴うエネルギーロスを低減
し、これにより総発電効率を高めることができるガス焚
きガスタービン発電設備を提供することにある。The present invention was created to solve such problems. That is, an object of the present invention is to provide a gas-fired gas turbine power generation facility that can reduce energy loss associated with gas compression of low-calorie gas fuel and thereby increase total power generation efficiency.
【0008】[0008]
【課題を解決するための手段】本発明によれば、圧縮機
(11)で空気(2)を圧縮し、燃焼器(12)でガス
燃料(1)を燃焼して燃焼排ガス(3)を発生させ、燃
焼排ガスでタービン(13)を回転駆動して圧縮機と発
電機(14)を回転駆動し、熱交換器(17)で燃焼排
ガスを冷却して水蒸気(5)を発生させ、水蒸気を燃焼
器内に噴射して発電出力を高めるガス焚きガスタービン
発電設備において、ガス燃料(1)を圧縮前の空気中に
可燃限界以下で噴射する低圧燃料噴射装置(18)と、
燃焼器に追加燃料(6)を高圧で噴射する高圧燃料噴射
装置(19)と、燃焼排ガス中の未燃成分を触媒燃焼さ
せる触媒燃焼器(20)とを備えた、ことを特徴とする
ガス焚きガスタービン発電設備が提供される。According to the present invention, a compressor (11) compresses air (2) and a combustor (12) burns a gas fuel (1) to produce a combustion exhaust gas (3). The combustion exhaust gas is driven to rotate to drive the turbine (13) to rotate the compressor and the generator (14) to rotate, and the heat exchanger (17) cools the combustion exhaust gas to generate steam (5). A low pressure fuel injection device (18) for injecting gas fuel (1) into the air before compression below a flammable limit in a gas-fired gas turbine power generation facility for injecting into the combustor to increase power generation output,
A gas characterized by comprising a high-pressure fuel injector (19) for injecting additional fuel (6) at high pressure into the combustor, and a catalytic combustor (20) for catalytically burning unburned components in the combustion exhaust gas. A gas turbine power generation facility is provided.
【0009】本発明の好ましい実施形態によれば、前記
ガス燃料(1)は、低カロリーガス燃料であり、前記追
加燃料は液体燃料である。According to a preferred embodiment of the present invention, the gas fuel (1) is a low-calorie gas fuel and the additional fuel is a liquid fuel.
【0010】上記本発明の構成によれば、ガス燃料
(1)(低カロリーガス燃料)を圧縮前の空気中に噴射
するので、従来のガス圧縮機とガス冷却制御装置を省略
することができ、装置が簡略化できると共に、圧縮動力
を低減し、かつ冷却や圧損によるエネルギーロスをなく
すことができる。なお、噴射量は可燃限界以下であるの
で、圧縮機(11)におけるガス燃料の着火を本質的に
防止できる。According to the above-mentioned configuration of the present invention, the gas fuel (1) (low-calorie gas fuel) is injected into the air before compression, so that the conventional gas compressor and gas cooling control device can be omitted. The device can be simplified, the compression power can be reduced, and the energy loss due to cooling and pressure loss can be eliminated. Since the injection amount is less than the flammability limit, ignition of gas fuel in the compressor (11) can be essentially prevented.
【0011】また、燃焼器に追加燃料(6)を高圧で噴
射するので、希薄可燃限界以下の予混合気と追加燃料
(6)との混合により可燃範囲の燃料ガスを形成し、こ
れを安定燃焼させ、かつ保炎することができる。なお、
燃焼器での追加燃料はガス圧縮機が不要な灯油等液体燃
料が望ましいが、ガス燃料を用いる場合でも、ガス圧縮
機容量を大幅に減らせる効果がある。Further, since the additional fuel (6) is injected into the combustor at a high pressure, the premixture below the lean flammability limit and the additional fuel (6) are mixed to form a fuel gas in the flammable range, which is stabilized. It can be burned and flame-retained. In addition,
Liquid fuel such as kerosene, which does not require a gas compressor, is desirable as the additional fuel in the combustor, but even when gas fuel is used, it has the effect of significantly reducing the capacity of the gas compressor.
【0012】更に、抽気空気中にガス燃料が混入する
が、触媒燃焼器(20)でこれを触媒燃焼させ、熱交換
器(17)で水蒸気としてエネルギー回収できる。すな
わち、タービン冷却等による未燃分は、タービン下流の
触媒燃焼器で燃焼させ、その排ガス温度は触媒反応によ
りやや高めとなるので、熱交換器で水蒸気を発生させ、
燃焼器への蒸気噴射を行うことにより高効率化が図れ
る。Further, although gas fuel is mixed in the extracted air, it can be catalytically burned in the catalytic combustor (20) and energy can be recovered as steam in the heat exchanger (17). That is, unburned components due to turbine cooling and the like are burned in the catalytic combustor downstream of the turbine, and the exhaust gas temperature thereof is slightly raised by the catalytic reaction, so steam is generated in the heat exchanger,
High efficiency can be achieved by injecting steam to the combustor.
【0013】[0013]
【発明の実施の形態】以下、本発明の好ましい実施形態
を図面を参照して説明する。なお、各図において共通す
る部分には同一の符号を使用する。BEST MODE FOR CARRYING OUT THE INVENTION Preferred embodiments of the present invention will be described below with reference to the drawings. The same reference numerals are used for the common parts in each drawing.
【0014】図1は、本発明のガス焚きガスタービン発
電設備の全体構成図である。この図に示すように、本発
明のガス焚きガスタービン発電設備は、圧縮機11、燃
焼器12、タービン13及び発電機14からなるガスタ
ービン発電機10と熱交換器17を備え、圧縮機11で
空気2を圧縮し、燃焼器12でガス燃料1を燃焼して燃
焼排ガス3を発生させ、燃焼排ガス3でタービン13を
回転駆動して圧縮機11と発電機14を回転駆動して発
電機14で発電し、熱交換器17で燃焼排ガス3を冷却
して水蒸気5を発生させ、水蒸気5を燃焼器12内に噴
射して発電出力を高めるようになっている。なお、この
例で圧縮機11、タービン13及び発電機14は機械的
に同軸に連結されているが、歯車等を介して連結しても
よい。FIG. 1 is an overall configuration diagram of the gas-fired gas turbine power generation equipment of the present invention. As shown in this figure, the gas-fired gas turbine power generation facility of the present invention includes a gas turbine generator 10 including a compressor 11, a combustor 12, a turbine 13, and a generator 14, and a heat exchanger 17, and the compressor 11 To compress the air 2 and to combust the gas fuel 1 in the combustor 12 to generate the combustion exhaust gas 3. The combustion exhaust gas 3 rotationally drives the turbine 13 to rotationally drive the compressor 11 and the generator 14 to generate a generator. Power is generated in 14, the combustion exhaust gas 3 is cooled in the heat exchanger 17, steam 5 is generated, and the steam 5 is injected into the combustor 12 to increase the power generation output. Although the compressor 11, the turbine 13, and the generator 14 are mechanically connected coaxially in this example, they may be connected via a gear or the like.
【0015】図1において本発明のガス焚きガスタービ
ン発電設備は、更に、低圧燃料噴射装置18、高圧燃料
噴射装置19及び触媒燃焼器20を備える。ガス燃料1
は、本発明において、バイオマスガス、汚泥消化ガス、
石炭ガス化ガス等の低カロリーガス燃料が適している
が、LPG、LNG等の高カロリーガス燃料にも本発明
は適用できる。In FIG. 1, the gas-fired gas turbine power generation equipment of the present invention further comprises a low pressure fuel injection device 18, a high pressure fuel injection device 19 and a catalytic combustor 20. Gas fuel 1
Is, in the present invention, biomass gas, sludge digestion gas,
Low calorie gas fuels such as coal gasification gas are suitable, but the present invention can also be applied to high calorie gas fuels such as LPG and LNG.
【0016】低圧燃料噴射装置18は、ガス燃料1を圧
縮前の空気中に可燃限界以下で噴射する。すなわち、低
圧燃料噴射装置18は、ガス燃料1と空気2との混合ガ
スが自己燃焼できない希薄可燃限界以下の予混合気とな
るように制御する。また同時に、発電機14の回転速度
を維持するように、発電出力指令等に応じてガス燃料1
の流量を制御する。The low-pressure fuel injection device 18 injects the gas fuel 1 into the air before compression below the flammability limit. That is, the low-pressure fuel injection device 18 controls so that the mixed gas of the gas fuel 1 and the air 2 becomes a premixed gas that is less than the lean combustible limit that cannot self-combust. At the same time, in order to maintain the rotation speed of the generator 14, the gas fuel 1
Control the flow rate of.
【0017】高圧燃料噴射装置19は、燃焼器に追加燃
料6を高圧で噴射する。この追加燃料6は、加圧動力を
最小限度に抑えるために、灯油等の液体燃料であるのが
好ましいが、ガス燃料を用いてもよい。灯油等の液体燃
料を用いる場合、高圧燃料噴射装置19は、液圧ポンプ
とその流量制御弁からなる。また、ガス燃料を用いる場
合には、高圧燃料噴射装置19は、小型のガス圧縮機と
その流量制御弁からなる。The high-pressure fuel injection device 19 injects the additional fuel 6 into the combustor at high pressure. The additional fuel 6 is preferably a liquid fuel such as kerosene in order to minimize the pressurizing power, but a gas fuel may be used. When a liquid fuel such as kerosene is used, the high-pressure fuel injection device 19 is composed of a hydraulic pump and its flow control valve. When using gas fuel, the high-pressure fuel injection device 19 comprises a small gas compressor and its flow control valve.
【0018】触媒燃焼器20は、タービン13と熱交換
器17の間のガス流路に設けられる。この触媒燃焼器2
0は、内部に燃焼触媒層を有し、比較的低温(例えば2
00℃以上)で燃焼排ガス中の未燃成分を触媒燃焼させ
るようになっている。本発明の構成において、タービン
13に導入させる抽気空気2aには、ガス燃料1が混入
している。従って、このガス燃料1は燃焼器12を通過
せずにそのまま、タービン13の排ガス中に未燃成分と
して残り、これが触媒燃焼器20で燃焼して排ガス温度
を上昇させ、熱交換器17で水蒸気として熱回収される
ようになっている。The catalytic combustor 20 is provided in the gas flow path between the turbine 13 and the heat exchanger 17. This catalytic combustor 2
0 has a combustion catalyst layer inside and has a relatively low temperature (for example, 2
It is designed to catalytically burn unburned components in flue gas at temperatures above 00 ° C. In the configuration of the present invention, the gas fuel 1 is mixed in the extracted air 2a introduced into the turbine 13. Therefore, the gas fuel 1 does not pass through the combustor 12 and remains as it is in the exhaust gas of the turbine 13 as an unburned component, which burns in the catalytic combustor 20 to raise the temperature of the exhaust gas and the steam in the heat exchanger 17. It is designed to recover heat.
【0019】上述した本発明の構成によれば、ガス燃料
1(低カロリーガス燃料)を低圧燃料噴射装置18によ
り圧縮前の空気中に噴射するので、従来のガス圧縮機と
ガス冷却制御装置を省略することができ、装置が簡略化
できると共に、圧縮動力を低減し、かつ冷却や圧損によ
るエネルギーロスをなくすことができる。なお、噴射量
は可燃限界以下であるので、圧縮機11におけるガス燃
料1の着火を本質的に防止できる。According to the above-described configuration of the present invention, the gas fuel 1 (low-calorie gas fuel) is injected into the air before compression by the low-pressure fuel injection device 18, so that the conventional gas compressor and gas cooling control device can be used. It can be omitted, the device can be simplified, the compression power can be reduced, and the energy loss due to cooling and pressure loss can be eliminated. Since the injection amount is below the flammability limit, ignition of the gas fuel 1 in the compressor 11 can be essentially prevented.
【0020】また、高圧燃料噴射装置19により燃焼器
12に追加燃料6を高圧で噴射するので、希薄可燃限界
以下の予混合気と追加燃料6との混合により可燃範囲の
燃料ガスを形成し、これを安定燃焼させ、かつ保炎する
ことができる。なお、燃焼器での追加燃料はガス圧縮機
が不要な灯油等液体燃料が望ましいが、ガス燃料を用い
る場合でも、ガス圧縮機容量を大幅に減らせる効果があ
る。Since the high pressure fuel injection device 19 injects the additional fuel 6 into the combustor 12 at a high pressure, the premixture below the lean flammability limit and the additional fuel 6 are mixed to form a fuel gas in the combustible range. This can be stably burned and flame-retained. Liquid fuel such as kerosene that does not require a gas compressor is desirable as the additional fuel in the combustor, but even when gas fuel is used, it has the effect of significantly reducing the gas compressor capacity.
【0021】更に、抽気空気2a中にガス燃料1が混入
するが、触媒燃焼器20でこれを触媒燃焼させ、熱交換
器17で水蒸気としてエネルギー回収するので、燃焼器
12への蒸気噴射を行うことにより高効率化が図れる。Further, although the gas fuel 1 is mixed in the extracted air 2a, it is catalytically burned in the catalytic combustor 20 and the energy is recovered as steam in the heat exchanger 17, so that the steam is injected into the combustor 12. As a result, high efficiency can be achieved.
【0022】なお、本発明は上述した実施形態に限定さ
れず、本発明の要旨を逸脱しない範囲で種々変更できる
ことは勿論である。The present invention is not limited to the above-mentioned embodiments, and it goes without saying that various modifications can be made without departing from the gist of the present invention.
【0023】[0023]
【発明の効果】上述したように、本発明ではガス圧縮機
による損失をなくすために、圧縮機入口からガス燃料噴
射を行う。また、圧縮機の作動流体は予混合気となる
が、これを可燃限界以下としてその着火を防ぎ、燃焼器
における追加燃料の噴射により燃焼と保炎を行う。更に
タービン冷却等による未燃分は、タービン下流の触媒燃
焼器により除去し、その回収エネルギーを燃焼器への蒸
気噴射を行うことにより高効率化を図るようになってい
る。As described above, in the present invention, in order to eliminate the loss due to the gas compressor, gas fuel injection is performed from the compressor inlet. Further, the working fluid of the compressor becomes a premixed gas, which is kept below the flammability limit to prevent its ignition, and the combustion and flame holding are performed by the injection of the additional fuel in the combustor. Further, unburned components due to turbine cooling and the like are removed by a catalytic combustor downstream of the turbine, and the recovered energy is injected into the combustor to improve efficiency.
【0024】従って、本発明のガス焚きガスタービン発
電設備は、低カロリーガス燃料のガス圧縮に伴うエネル
ギーロスを低減し、これにより総発電効率を高めること
ができる等の優れた効果を有する。Therefore, the gas-fired gas turbine power generation equipment of the present invention has an excellent effect that energy loss due to gas compression of low-calorie gas fuel is reduced, and thereby total power generation efficiency can be increased.
【図1】本発明のガス焚きガスタービン発電設備の全体
構成図である。FIG. 1 is an overall configuration diagram of a gas-fired gas turbine power generation facility of the present invention.
【図2】従来のガス焚きガスタービン発電設備の構成図
である。FIG. 2 is a configuration diagram of a conventional gas-fired gas turbine power generation facility.
【図3】ガス燃料の発熱量とガス圧縮動力及び総発電効
率との関係図である。FIG. 3 is a relationship diagram of the calorific value of gas fuel, gas compression power, and total power generation efficiency.
1 ガス燃料、2 空気、2a 抽気空気、3 燃焼排
ガス、4 冷却水、5 水蒸気、6 追加燃料、10
ガスタービン発電機、11 圧縮機、12 燃焼器、1
3 タービン、14 発電機、15 ガス圧縮機、16
ガス冷却制御装置、17 熱交換器、18 低圧燃料
噴射装置、19 高圧燃料噴射装置、20 触媒燃焼器1 gas fuel, 2 air, 2a extraction air, 3 combustion exhaust gas, 4 cooling water, 5 steam, 6 additional fuel, 10
Gas turbine generator, 11 compressor, 12 combustor, 1
3 turbines, 14 generators, 15 gas compressors, 16
Gas cooling control device, 17 heat exchanger, 18 low pressure fuel injection device, 19 high pressure fuel injection device, 20 catalyst combustor
Claims (2)
燃焼器(12)でガス燃料(1)を燃焼して燃焼排ガス
(3)を発生させ、燃焼排ガスでタービン(13)を回
転駆動して圧縮機と発電機(14)を回転駆動し、熱交
換器(17)で燃焼排ガスを冷却して水蒸気(5)を発
生させ、水蒸気を燃焼器内に噴射して発電出力を高める
ガス焚きガスタービン発電設備において、 ガス燃料(1)を圧縮前の空気中に可燃限界以下で噴射
する低圧燃料噴射装置(18)と、燃焼器に追加燃料
(6)を高圧で噴射する高圧燃料噴射装置(19)と、
燃焼排ガス中の未燃成分を触媒燃焼させる触媒燃焼器
(20)とを備えた、ことを特徴とするガス焚きガスタ
ービン発電設備。1. A compressor (11) compresses air (2),
The combustor (12) burns the gas fuel (1) to generate combustion exhaust gas (3), and the combustion exhaust gas rotationally drives the turbine (13) to rotationally drive the compressor and the generator (14) to generate heat. In a gas-fired gas turbine power generation facility in which a combustion exhaust gas is cooled by an exchanger (17) to generate steam (5) and the steam is injected into the combustor to increase power generation output, the gas fuel (1) is compressed before compression. A low pressure fuel injector (18) for injecting into the air below the flammability limit, a high pressure fuel injector (19) for injecting additional fuel (6) into the combustor at high pressure,
A gas-fired gas turbine power generation facility comprising a catalytic combustor (20) for catalytically burning unburned components in combustion exhaust gas.
燃料であり、前記追加燃料は液体燃料である、ことを特
徴とする請求項1に記載のガス焚きガスタービン発電設
備。2. The gas-fired gas turbine power generation facility according to claim 1, wherein the gas fuel (1) is a low-calorie gas fuel, and the additional fuel is a liquid fuel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001243124A JP2003056364A (en) | 2001-08-10 | 2001-08-10 | Gas-fired gas turbine power generation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001243124A JP2003056364A (en) | 2001-08-10 | 2001-08-10 | Gas-fired gas turbine power generation equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2003056364A true JP2003056364A (en) | 2003-02-26 |
Family
ID=19073268
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2001243124A Pending JP2003056364A (en) | 2001-08-10 | 2001-08-10 | Gas-fired gas turbine power generation equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2003056364A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006000812A (en) * | 2004-06-21 | 2006-01-05 | Ishikawajima Harima Heavy Ind Co Ltd | Sewage treatment system |
| JP2007283182A (en) * | 2006-04-14 | 2007-11-01 | Fujimori Kogyo Co Ltd | Apparatus and method for treating volatile organic compounds |
| JP2008133751A (en) * | 2006-11-27 | 2008-06-12 | Toyota Motor Corp | Purification device and purification method |
| JP2009167909A (en) * | 2008-01-16 | 2009-07-30 | Takuma Co Ltd | Biomass gasification gas power generating system and its power generating method |
| JP2012511121A (en) * | 2008-12-08 | 2012-05-17 | フレックスエナジー,インコーポレーテッド | Fuel oxidation in multiple modes of operation |
| US8980192B2 (en) | 2012-03-09 | 2015-03-17 | Ener-Core Power, Inc. | Gradual oxidation below flameout temperature |
-
2001
- 2001-08-10 JP JP2001243124A patent/JP2003056364A/en active Pending
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006000812A (en) * | 2004-06-21 | 2006-01-05 | Ishikawajima Harima Heavy Ind Co Ltd | Sewage treatment system |
| JP2007283182A (en) * | 2006-04-14 | 2007-11-01 | Fujimori Kogyo Co Ltd | Apparatus and method for treating volatile organic compounds |
| JP2008133751A (en) * | 2006-11-27 | 2008-06-12 | Toyota Motor Corp | Purification device and purification method |
| JP2009167909A (en) * | 2008-01-16 | 2009-07-30 | Takuma Co Ltd | Biomass gasification gas power generating system and its power generating method |
| JP2012511121A (en) * | 2008-12-08 | 2012-05-17 | フレックスエナジー,インコーポレーテッド | Fuel oxidation in multiple modes of operation |
| US8980192B2 (en) | 2012-03-09 | 2015-03-17 | Ener-Core Power, Inc. | Gradual oxidation below flameout temperature |
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