JP2003090231A - Reformed fuel burning gas turbine and purge method of its fuel system - Google Patents

Reformed fuel burning gas turbine and purge method of its fuel system

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Publication number
JP2003090231A
JP2003090231A JP2001282575A JP2001282575A JP2003090231A JP 2003090231 A JP2003090231 A JP 2003090231A JP 2001282575 A JP2001282575 A JP 2001282575A JP 2001282575 A JP2001282575 A JP 2001282575A JP 2003090231 A JP2003090231 A JP 2003090231A
Authority
JP
Japan
Prior art keywords
fuel
light
reformed
supply system
reformed fuel
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.)
Granted
Application number
JP2001282575A
Other languages
Japanese (ja)
Other versions
JP3807272B2 (en
Inventor
Shinichi Inage
真一 稲毛
Hiromi Koizumi
浩美 小泉
Akinori Hayashi
林  明典
Shigeyoshi Kobayashi
成嘉 小林
Takashi Ikeguchi
隆 池口
Tomohiko Miyamoto
知彦 宮本
Nobuyuki Hokari
信幸 穂刈
Hirokazu Takahashi
宏和 高橋
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
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Filing date
Publication date
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Priority to JP2001282575A priority Critical patent/JP3807272B2/en
Publication of JP2003090231A publication Critical patent/JP2003090231A/en
Application granted granted Critical
Publication of JP3807272B2 publication Critical patent/JP3807272B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Feeding And Controlling Fuel (AREA)

Abstract

PROBLEM TO BE SOLVED: To suppress clogging in a fuel supply system in the case of switching reformed fuel and light fuel in a reformed fuel burning gas turbine of heavy oil. SOLUTION: A combustor for switching reformed fuel and light fuel to be burnt is provided, to have a means, in the case of switching from this reformed fuel to this light fuel, after stopping supply of this reformed fuel, supplying supercritical or sub-critical steam to a reformed fuel supply system to purge heavy fuel left in this reformed fuel supply system, or to have a means, in the case of switching from this light fuel to this reformed fuel, after stopping supply of this light fuel, supplying supercritical or sub-critical steam to a light fuel supply system to purge light fuel left in this light fuel supply system. Accordingly, clogging of the fuel supply system is suppressed.

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、ガスタービンに関
係し、特に重質油を超臨界水乃至超臨界蒸気により軽質
化し、前記改質燃料にて運用されるガスタービン及びそ
の燃料系統パージ方法に関わる。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a gas turbine, and more particularly, to a gas turbine that is lightened by supercritical water or supercritical steam and is operated with the reformed fuel, and a fuel system purging method thereof. Involved in.

【0002】[0002]

【従来の技術】従来の灯軽質油等の軽質燃料焚きのガス
タービンの停止時のパージ方法は、例えば、ガスタービ
ン停止時には、軽質油コントロールバルブにより軽質油
の供給量をコントロールして停止させるものがある。そ
して、燃焼器の燃料ノズル等、高温空気にさらされる部
品は、ガスタービン停止直後も400℃前後となってい
る。燃料ノズル中に軽質油が残留する場合には、余熱に
より燃料中の不飽和成分が重合し、ガム状の物質を生成
し、ノズルの目詰り等を引き起こす可能性がある。その
防止のために、従来一般的に、空気圧縮機により空気を
圧縮し、空気を軽質油燃料系統に供給し、残留する軽質
油を除去している。
2. Description of the Related Art A conventional method of purging a gas turbine for burning light fuel such as kerosene and light oil when the gas turbine is stopped is, for example, to control the supply amount of light oil by a light oil control valve when the gas turbine is stopped. There is. Then, the parts exposed to the high temperature air, such as the fuel nozzle of the combustor, are still around 400 ° C. immediately after the gas turbine is stopped. When the light oil remains in the fuel nozzle, residual heat may polymerize the unsaturated components in the fuel to form a gum-like substance, which may cause nozzle clogging. In order to prevent this, conventionally, air is generally compressed by an air compressor, air is supplied to a light oil fuel system, and residual light oil is removed.

【0003】[0003]

【発明が解決しようとする課題】重質油の改質燃料焚き
のガスタービンでは、重質油は、高温条件下で重合,ガ
ム状物質を生成しやすいオレフィン成分,芳香成分の占
める比率が高い。改質した場合でも、前記のオレフィン
成分,芳香成分を完全に軽質化することは難しく、一定
量の前記成分は燃料供給系統へ輸送される。そのため、
従来の軽質燃料に比べて、燃料供給系統に残留する改質
燃料が重合し、系統に目詰りを発生させる可能性が高
い。
SUMMARY OF THE INVENTION In a gas turbine for burning a reformed fuel of a heavy oil, the heavy oil has a high proportion of an olefin component and an aroma component which are easily polymerized under high temperature conditions to easily produce a gum-like substance. . Even when reformed, it is difficult to completely lighten the olefin component and the aroma component, and a certain amount of the component is transported to the fuel supply system. for that reason,
Compared with the conventional light fuel, the reformed fuel remaining in the fuel supply system is likely to polymerize and cause clogging in the system.

【0004】従来のように、空気乃至窒素でパージする
場合、残留する改質燃料を冷却する作用が強いために、
燃料ノズル等の余熱を持つ部分に接している個所で、重
合を引き起こす可能性がある。特に、燃料ノズルと供給
配管の接合部のように、継目,段差がある部分に改質燃
料が停留している場合には、前記の重合作用は顕著とな
る。
In the case of purging with air or nitrogen as in the conventional case, since the action of cooling the remaining reformed fuel is strong,
Polymerization may occur at a portion in contact with a portion having residual heat such as a fuel nozzle. In particular, when the reformed fuel stays at a portion having a joint or a step, such as a joint between the fuel nozzle and the supply pipe, the above-mentioned polymerization action becomes remarkable.

【0005】本発明の目的は、重質油の改質燃料焚きの
ガスタービンで、改質燃料と軽質燃料との切替え時の燃
料供給系統の詰まりを抑制することにある。
An object of the present invention is to suppress clogging of the fuel supply system at the time of switching between the reformed fuel and the light fuel in a gas turbine that burns heavy fuel reformed fuel.

【0006】[0006]

【課題を解決するための手段】本発明は、重質油を超臨
界蒸気により軽質化した改質燃料と軽質燃料とを負荷に
応じて切替えて燃焼させる燃焼器を備えたガスタービン
であって、該改質燃料から該軽質燃料に切替える場合
に、該改質燃料の供給停止後に改質燃料供給系統に超臨
界乃至亜臨界蒸気を供給し、該改質燃料供給系統中に残
存する重質燃料をパージする手段を有することを特徴と
する。
DISCLOSURE OF THE INVENTION The present invention is a gas turbine equipped with a combustor for switching between a reformed fuel obtained by lightening heavy oil by supercritical steam and a light fuel and burning them according to the load. , When switching from the reformed fuel to the light fuel, supplying supercritical or subcritical steam to the reformed fuel supply system after the supply of the reformed fuel is stopped, and the heavy fuel remaining in the reformed fuel supply system It is characterized by having means for purging fuel.

【0007】或いは、本発明は、重質油を超臨界蒸気に
より軽質化した改質燃料と軽質燃料とを負荷に応じて切
替えて燃焼させる燃焼器を備えたガスタービンであっ
て、該軽質燃料から該改質燃料に切替える場合に、該軽
質燃料の供給停止後に軽質燃料供給系統に超臨界乃至亜
臨界蒸気を供給し、該軽質燃料供給系統中に残存する軽
質燃料をパージする手段を有することを特徴とする。
Alternatively, the present invention is a gas turbine equipped with a combustor for switching between a reformed fuel obtained by lightening heavy oil by supercritical steam and a light fuel according to the load, and burning the light fuel. In the case of switching from the reforming fuel to the reforming fuel, a means for supplying supercritical or subcritical vapor to the light fuel supply system after stopping the supply of the light fuel and purging the light fuel remaining in the light fuel supply system is provided. Is characterized by.

【0008】[0008]

【発明の実施の形態】まず、一般的な灯軽質油等の軽質
燃料焚きのガスタービンの停止時のパージ方法を図2に
示す。図2で、1は圧縮機、2はタービン、3は燃焼
器、4は空気、12は軽質燃料、19は軽質油燃料コン
トロールバルブ、23は軽質油燃料供給系統、25は空
気圧縮機、26は空気供給系統、27は空気である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS First, FIG. 2 shows a purging method when a gas turbine for burning light fuel such as general light oil is stopped when the gas turbine is stopped. In FIG. 2, 1 is a compressor, 2 is a turbine, 3 is a combustor, 4 is air, 12 is a light fuel, 19 is a light oil fuel control valve, 23 is a light oil fuel supply system, 25 is an air compressor, 26 Is an air supply system and 27 is air.

【0009】ガスタービン停止時には、軽質油燃料コン
トロールバルブ19により軽質燃料12の供給量をコン
トロールして停止させる。燃焼器3の燃料ノズル等、高
温空気にさらされる部品は、ガスタービン停止直後も4
00℃前後となっている。燃料ノズル中に軽質燃料12
が残留する場合には、余熱により燃料中の不飽和成分が
重合し、ガム状の物質を生成し、ノズルの目詰り等を引
き起こす可能性がある。その防止のために、空気圧縮機
25により空気を圧縮し、空気27を空気供給系統26
に供給し、残留する軽質燃料を除去するのが従来の一般
的な燃料パージ方法となっている。
When the gas turbine is stopped, the light oil fuel control valve 19 controls the supply amount of the light fuel 12 to stop it. Parts exposed to high-temperature air, such as the fuel nozzle of the combustor 3, are
It is around 00 ° C. Light fuel 12 in the fuel nozzle
In the case of remaining, the unsaturated components in the fuel are polymerized by the residual heat to generate a gum-like substance, which may cause nozzle clogging. To prevent this, air is compressed by the air compressor 25 and the air 27 is supplied to the air supply system 26.
The conventional general fuel purging method is to remove the remaining light fuel by supplying it to the fuel tank.

【0010】本発明の実施の形態に係わる第一の重質油
改質燃料焚きガスタービンは、超臨界蒸気を発生させる
装置と重質油を前記超臨界蒸気により軽質化する改質器
を有し、軽質燃料及び前記改質燃料を負荷に応じて切替
えて燃焼させる燃焼器からの高温ガスにて駆動されるガ
スタービンにおいて、改質燃料から軽質燃料に切替える
場合には、改質燃料供給停止後に改質器及び改質燃料を
燃焼器に供給する系統に超臨界乃至亜臨界蒸気のみを流
し、改質器及び供給系統中に残存する重質燃料をパージ
することにより構成される。
The first heavy oil reformed fuel burning gas turbine according to the embodiment of the present invention has a device for generating supercritical steam and a reformer for lightening the heavy oil by the supercritical steam. However, in a gas turbine driven by high temperature gas from a combustor that switches and burns light fuel and the reformed fuel depending on the load, when the reformed fuel is switched to the light fuel, the reformed fuel supply is stopped. After that, only the supercritical or subcritical steam is allowed to flow into the reformer and the system for supplying the reformed fuel to the combustor, and the heavy fuel remaining in the reformer and the supply system is purged.

【0011】超臨界蒸気は、有機物の溶解作用が極めて
強く、さらに溶解した有機物を容易に分解する作用を持
つ。改質燃料は、重質油を超臨界蒸気により改質する
が、軽質燃料への切替え時には、改質反応器への燃料の
供給を遮断し、超臨界蒸気のみを供給する。改質反応器
を通過した超臨界蒸気は、改質燃料供給系統を経て、前
記軽質燃料を燃焼させている燃焼器へ流出する。超臨界
蒸気は、前記のように化学的に非常に活性が高いため、
燃料供給系統に残存する重質油分を容易に溶解,分解す
る。溶解した重質油を含んだ蒸気は、燃焼器内の軽質油
燃焼ガスにより重質油分を完全に燃焼させた後に、ガス
タービンへ流出する。これにより、燃料ノズル等の余熱
を持つ部分に接している個所でも、重合を抑制し防止で
きる。
Supercritical vapor has an extremely strong action of dissolving organic substances, and has a function of easily decomposing the dissolved organic substances. The reformed fuel reforms heavy oil with supercritical steam. When switching to light fuel, the supply of fuel to the reforming reactor is cut off and only supercritical steam is supplied. The supercritical steam that has passed through the reforming reactor flows out to the combustor burning the light fuel through the reforming fuel supply system. Since supercritical vapor is chemically very active as described above,
The heavy oil remaining in the fuel supply system is easily dissolved and decomposed. The steam containing the dissolved heavy oil flows out to the gas turbine after the heavy oil is completely burned by the light oil combustion gas in the combustor. As a result, it is possible to suppress and prevent polymerization even at a portion in contact with a portion having residual heat such as a fuel nozzle.

【0012】本発明の実施の形態に係わる第二の重質油
改質燃料焚きガスタービンは、第一の発明において、灯
軽質油等の軽質燃料を改質燃料に切替える際に、軽質燃
料供給停止後に軽質燃料供給系統にも超臨界乃至亜臨界
蒸気を供給し、供給系統に残存する軽質燃料をパージす
ることにより構成される。
A second heavy oil reformed fuel-fired gas turbine according to an embodiment of the present invention provides a light fuel supply when switching from a light fuel such as light oil to a reformed fuel in the first invention. It is configured by supplying supercritical or subcritical steam also to the light fuel supply system after the stop, and purging the light fuel remaining in the supply system.

【0013】軽質油の中にも、上記課題の部分に記載し
たオレフィン成分,芳香成分を含むものがある。例え
ば、従来の灯軽油に比べて安価なライトサイクルオイル
と呼ばれる軽質油がガスタービン燃料として利用されつ
つある。ライトサイクルオイル中には、約70%の芳香
成分が含まれる。このような軽質油が供給系統及び燃料
ノズルに座温存し、加熱された場合には、改質燃料同様
に、重合による詰まりが懸念される。超臨界蒸気を軽質
油供給系統に供給することにより、軽質燃料の重合を抑
制し防止できる。
Some light oils contain the olefin component and the aroma component described in the above-mentioned problems. For example, light oil called light cycle oil, which is cheaper than conventional kerosene, is being used as a gas turbine fuel. Light cycle oil contains about 70% aroma components. When such a light oil is seat-saved in the supply system and the fuel nozzle and is heated, there is a risk of clogging due to polymerization, like the reformed fuel. By supplying supercritical steam to the light oil supply system, polymerization of light fuel can be suppressed and prevented.

【0014】本発明の実施の形態に係わる第三の重質油
改質燃料焚きガスタービンは、第一,第二の発明におい
て、改質燃料及び軽質燃料の供給系統を超超臨界乃至亜
臨界蒸気にてパージした後に、さらに空気或いは窒素に
てパージすることにより構成される。
A third heavy oil reformed fuel burning gas turbine according to the embodiment of the present invention is the supercritical or subcritical supply system for the reformed fuel and the light fuel in the first and second inventions. It is constituted by purging with steam and then with air or nitrogen.

【0015】超臨界蒸気乃至亜臨界蒸気でパージした場
合、燃料供給系統内に前記蒸気が残存したまま、ガスタ
ービンが冷却されると、蒸気が水に相変化し、燃料供給
系統や燃料ノズル内に錆を発生させる場合が想定され
る。前記錆はやはり、供給系統及び燃料ノズルを詰まら
せる要因となる。蒸気パージ後、窒素乃至空気でさらに
供給系統に残存するドレインをパージすることにより、
錆等の発生を抑制し防止できる。
When purging with supercritical steam or subcritical steam, when the gas turbine is cooled while the steam remains in the fuel supply system, the phase of the steam is changed to water, and the steam in the fuel supply system and the fuel nozzle is changed. It is expected that rust will occur on the. The rust also causes the clogging of the supply system and the fuel nozzle. After the steam purge, by purging the drain remaining in the supply system with nitrogen or air,
The generation of rust can be suppressed and prevented.

【0016】(第一実施例)以下図1及び図3に基づい
て本発明の第一実施例を説明する。図1で、1は圧縮
機、2はタービン、3は燃焼器、4は空気、5は高温排
ガス、6は排熱回収ボイラー、7は水、8は超臨界蒸
気、9は重質油、10は改質器、11は改質燃料、12
は軽質燃料、16は燃焼ガス、17は改質燃料供給系
統、18は重質油コントロールバルブ、19は軽質油燃
料コントロールバルブ、20は改質燃料パージライン、
21及び22は改質燃料用コントロールバルブである。
また、図3で、4は空気、13は軽質油用燃料ノズル、
14は改質燃料用燃料ノズル、15はスワーラー、16
は燃焼ガスである。
(First Embodiment) A first embodiment of the present invention will be described below with reference to FIGS. 1 and 3. In FIG. 1, 1 is a compressor, 2 is a turbine, 3 is a combustor, 4 is air, 5 is high temperature exhaust gas, 6 is an exhaust heat recovery boiler, 7 is water, 8 is supercritical steam, 9 is heavy oil, 10 is a reformer, 11 is a reformed fuel, 12
Is a light fuel, 16 is a combustion gas, 17 is a reformed fuel supply system, 18 is a heavy oil control valve, 19 is a light oil fuel control valve, 20 is a reformed fuel purge line,
21 and 22 are control valves for reforming fuel.
In FIG. 3, 4 is air, 13 is a fuel nozzle for light oil,
14 is a fuel nozzle for reforming fuel, 15 is a swirler, 16
Is combustion gas.

【0017】図3は、図1中に示す燃焼器3の詳細構造
を示したものである。本実施例では、圧縮機1で圧縮さ
れた空気4と、軽質燃料12により起動される。空気4
と軽質燃料の燃焼ガス16にてタービン2を駆動する。
タービン2を駆動した後の排ガス5は排熱回収ボイラー
6にて、水7と熱交換し、超臨界蒸気8を発生させる。
改質に適した超臨界蒸気になった時点で、超臨界蒸気及
び重質燃料9を改質器へ供給し、改質燃料11を製造す
る。
FIG. 3 shows a detailed structure of the combustor 3 shown in FIG. In this embodiment, the air 4 compressed by the compressor 1 and the light fuel 12 are activated. Air 4
The turbine 2 is driven by the combustion gas 16 of light fuel.
Exhaust gas 5 after driving the turbine 2 exchanges heat with water 7 in an exhaust heat recovery boiler 6 to generate supercritical steam 8.
When the supercritical steam suitable for reforming is obtained, the supercritical steam and the heavy fuel 9 are supplied to the reformer to produce the reformed fuel 11.

【0018】一定の部分負荷運転までは、改質燃料11
の組成が燃焼に適しないために、コントロールバルブ2
2を閉止し、コントロールバルブ21を開いてパージラ
イン20へ捨てる。負荷が上昇し、改質燃料11の組成
が安定した時点で、コントロールバルブ21を閉止、バ
ルブ22を開いて改質燃料11を燃焼器3へ供給、同時
に軽質燃料12をバルブ19によりコントロールし、改
質燃料11のみでガスタービンを運用する。
Up to a certain partial load operation, the reformed fuel 11
Control valve 2 because the composition of is not suitable for combustion
2 is closed, the control valve 21 is opened, and it is discarded into the purge line 20. When the load increases and the composition of the reformed fuel 11 becomes stable, the control valve 21 is closed, the valve 22 is opened to supply the reformed fuel 11 to the combustor 3, and at the same time the light fuel 12 is controlled by the valve 19. The gas turbine is operated only with the reformed fuel 11.

【0019】逆に負荷が低下する場合は、軽質油燃料の
コントロールバルブ19を開いて軽質燃料12を供給す
ると同時に、改質燃料用コントロールバルブ22を閉止
することにより改質燃料11の燃焼器への供給を停止
し、バルブ21を開いて20の改質燃料パージラインへ
と排出される。軽質燃料12による排熱を利用し、排熱
回収ボイラー6内で、超臨界蒸気8を継続的に発生させ
る。
On the contrary, when the load decreases, the control valve 19 for the light oil fuel is opened to supply the light fuel 12, and at the same time, the control valve 22 for the reformed fuel is closed to the combustor of the reformed fuel 11. Is stopped and the valve 21 is opened to discharge the reformed fuel to the reformed fuel purge line 20. The exhaust heat from the light fuel 12 is used to continuously generate the supercritical steam 8 in the exhaust heat recovery boiler 6.

【0020】改質燃料11供給停止時には、重質燃料9
の供給を止め、超臨界蒸気8のみを改質器10に供給す
る。超臨界蒸気8は、改質器10を素通りし、まず改質
燃料パージライン20の流路を十分にパージする。つい
で、コントロールバルブ21を閉止し、コントロールバ
ルブ22を開くことにより、超臨界蒸気8は燃料供給系
統17を経て、燃焼器3へ流入する。燃焼器3内の軽質
燃料12と空気4による燃焼ガス16中に、改質燃料供
給系統17中に残存した重質油9を溶解した超臨界蒸気
8が噴射されることにより、重質燃料11は完全に燃焼
された後、タービン2へ流出する。
When the supply of the reformed fuel 11 is stopped, the heavy fuel 9
Is stopped and only the supercritical steam 8 is supplied to the reformer 10. The supercritical steam 8 passes straight through the reformer 10 and first sufficiently purges the flow path of the reformed fuel purge line 20. Then, by closing the control valve 21 and opening the control valve 22, the supercritical steam 8 flows into the combustor 3 via the fuel supply system 17. By injecting the supercritical steam 8 in which the heavy oil 9 remaining in the reformed fuel supply system 17 is dissolved into the combustion gas 16 of the light fuel 12 and the air 4 in the combustor 3, the heavy fuel 11 Is completely burned and then flows out to the turbine 2.

【0021】本実施例によれば、改質燃料から軽質燃料
への切替え時は、改質燃料供給系統に残存する重質燃料
分を改質燃料供給系統へ超臨界蒸気を注入することによ
り容易に溶解,分解することでき、燃料供給系統の余熱
による前記残存重質油の重合を抑制して防止し、引いて
は前記重合による改質燃料供給系統の詰まりを抑制して
防止できる。
According to the present embodiment, when switching from the reformed fuel to the light fuel, the heavy fuel remaining in the reformed fuel supply system can be easily injected by injecting the supercritical steam into the reformed fuel supply system. Can be dissolved and decomposed in the fuel supply system, and the residual heavy oil due to residual heat in the fuel supply system can be suppressed and prevented from being polymerized, and the reformed fuel supply system can be prevented from being clogged due to the polymerization.

【0022】逆に、軽質燃料から改質燃料への切替える
時は、前記軽質燃料供給系統にも超臨界蒸気を注入する
ことにより、供給系統中の残存軽質燃料を溶解,分解す
ることにより、余熱による前記残存軽質燃料の重合を抑
制して防止し、引いては前記重合による軽質燃料供給系
統の詰まりを抑制して防止できる。
On the contrary, when switching from the light fuel to the reformed fuel, by injecting the supercritical steam also into the light fuel supply system, the residual light fuel in the supply system is melted and decomposed, and the residual heat is removed. It is possible to suppress and prevent the polymerization of the remaining light fuel due to the above, and eventually to suppress and prevent the clogging of the light fuel supply system due to the polymerization.

【0023】(第二実施例)以下、図4に基づいて本発
明の第二実施例を説明する。図4で1は圧縮機、2はタ
ービン、3は燃焼器、4は空気、5は高温排ガス、6は
排熱回収ボイラー、7は水、8は超臨界蒸気、9は重質
油、10は改質器、11は改質燃料、12は軽質燃料、
16は燃焼ガス、17は改質燃料供給系統、18は重質
油コントロールバルブ、19は軽質油燃料コントロール
バルブ、20は改質燃料パージライン、21及び22は
改質燃料用コントロールバルブ、23は軽質油燃料供給
系統、24は軽質油供給系統への超臨界蒸気コントロー
ルバルブである。
(Second Embodiment) A second embodiment of the present invention will be described below with reference to FIG. In FIG. 4, 1 is a compressor, 2 is a turbine, 3 is a combustor, 4 is air, 5 is high temperature exhaust gas, 6 is an exhaust heat recovery boiler, 7 is water, 8 is supercritical steam, 9 is heavy oil, 10 Is a reformer, 11 is a reformed fuel, 12 is a light fuel,
Reference numeral 16 is a combustion gas, 17 is a reformed fuel supply system, 18 is a heavy oil control valve, 19 is a light oil fuel control valve, 20 is a reformed fuel purge line, 21 and 22 are reformed fuel control valves, and 23 is A light oil fuel supply system, and 24 is a supercritical steam control valve for the light oil supply system.

【0024】図4中の燃焼器3は、図3と同様の構造に
より構成される。本実施例では、圧縮機1で圧縮された
空気4と、軽質燃料12により起動される。空気4と軽
質燃料の燃焼ガス16にてタービン2を駆動する。ター
ビン2を駆動した後の排ガス5は排熱回収ボイラー6に
て、水7と熱交換し、超臨界蒸気8を発生させる。改質
に適した超臨界蒸気になった時点で、超臨界蒸気及び重
質燃料9を改質器へ供給し、改質燃料11を製造する。
The combustor 3 shown in FIG. 4 has the same structure as that shown in FIG. In this embodiment, the air 4 compressed by the compressor 1 and the light fuel 12 are activated. The turbine 2 is driven by the air 4 and the combustion gas 16 of the light fuel. Exhaust gas 5 after driving the turbine 2 exchanges heat with water 7 in an exhaust heat recovery boiler 6 to generate supercritical steam 8. When the supercritical steam suitable for reforming is obtained, the supercritical steam and the heavy fuel 9 are supplied to the reformer to produce the reformed fuel 11.

【0025】一定の部分負荷運転までは、改質燃料11
の組成が燃焼に適しないために、コントロールバルブ2
2を閉止し、コントロールバルブ21を開いてパージラ
イン20へ捨てる。負荷が上昇し、改質燃料11の組成
が安定した時点で、コントロールバルブ21を閉止、バ
ルブ21を開いて改質燃料11を燃焼器3へ供給、同時
に軽質燃料12をバルブ19によりコントロールし、改
質燃料11のみでガスタービンを運用する。その後、バ
ルブ24を開き、超臨界蒸気8を、軽質油燃料供給系統
23へ供給する。超臨界蒸気8は、軽質油燃料供給系統
23中を経て、燃焼器3へ流入する。燃焼器3内の軽質
燃料12と空気4による燃焼ガス16中に、軽質油燃料
供給系統23中に残存した軽質燃料12を溶解した超臨
界蒸気8が噴射されることにより、軽質燃料12は完全
に燃焼された後、タービン2へ流出する。そして、軽質
油燃料供給系統23の目詰まりを抑制する。
Up to a certain partial load operation, the reformed fuel 11
Control valve 2 because the composition of is not suitable for combustion
2 is closed, the control valve 21 is opened, and it is discarded into the purge line 20. When the load increases and the composition of the reformed fuel 11 becomes stable, the control valve 21 is closed, the valve 21 is opened to supply the reformed fuel 11 to the combustor 3, and at the same time the light fuel 12 is controlled by the valve 19. The gas turbine is operated only with the reformed fuel 11. Then, the valve 24 is opened to supply the supercritical steam 8 to the light oil fuel supply system 23. The supercritical steam 8 flows into the combustor 3 through the light oil fuel supply system 23. By injecting the supercritical steam 8 in which the light fuel 12 remaining in the light oil fuel supply system 23 is dissolved into the combustion gas 16 of the light fuel 12 and the air 4 in the combustor 3, the light fuel 12 is completely discharged. After being burned to the turbine 2, it flows out to the turbine 2. Then, clogging of the light oil fuel supply system 23 is suppressed.

【0026】(第三実施例)以下、図5に基づいて本発
明の第三実施例を説明する。図5で1は圧縮機、2はタ
ービン、3は燃焼器、4は空気、5は高温排ガス、6は
排熱回収ボイラー、7は水、8は超臨界蒸気、9は重質
油、10は改質器、11は改質燃料、12は軽質燃料、
16は燃焼ガス、17は改質燃料供給系統、18は重質
油コントロールバルブ、19は軽質油燃料コントロール
バルブ、20は改質燃料パージライン、21及び22は
改質燃料用コントロールバルブ、23は軽質油燃料供給
系統、24は軽質油供給系統への超臨界蒸気コントロー
ルバルブ25は空気圧縮機、26は空気供給系統、27
は空気、28は改質器への超臨界蒸気コントロールバル
ブ、29は軽質燃料供給系統への空気コントロールバル
ブ、30は改質燃料供給系統への空気コントロールバル
ブである。
(Third Embodiment) The third embodiment of the present invention will be described below with reference to FIG. In FIG. 5, 1 is a compressor, 2 is a turbine, 3 is a combustor, 4 is air, 5 is high temperature exhaust gas, 6 is an exhaust heat recovery boiler, 7 is water, 8 is supercritical steam, 9 is heavy oil, 10 Is a reformer, 11 is a reformed fuel, 12 is a light fuel,
Reference numeral 16 is a combustion gas, 17 is a reformed fuel supply system, 18 is a heavy oil control valve, 19 is a light oil fuel control valve, 20 is a reformed fuel purge line, 21 and 22 are reformed fuel control valves, and 23 is Light oil fuel supply system, 24 is a supercritical steam control valve for the light oil supply system 25 is an air compressor, 26 is an air supply system, 27
Is air, 28 is a supercritical steam control valve for the reformer, 29 is an air control valve for the light fuel supply system, and 30 is an air control valve for the reformed fuel supply system.

【0027】図5中の燃焼器3は、図3と同様の構造に
より構成される。本実施例では、圧縮機1で圧縮された
空気4と、軽質燃料12により起動される。空気4と軽
質燃料の燃焼ガス16にてタービン2を駆動する。ター
ビン2を駆動した後の排ガス5は排熱回収ボイラー6に
て、水7と熱交換し、超臨界蒸気8を発生させる。改質
に適した超臨界蒸気になった時点で、超臨界蒸気及び重
質燃料9を改質器へ供給し、改質燃料11を製造する。
The combustor 3 shown in FIG. 5 has the same structure as that shown in FIG. In this embodiment, the air 4 compressed by the compressor 1 and the light fuel 12 are activated. The turbine 2 is driven by the air 4 and the combustion gas 16 of the light fuel. Exhaust gas 5 after driving the turbine 2 exchanges heat with water 7 in an exhaust heat recovery boiler 6 to generate supercritical steam 8. When the supercritical steam suitable for reforming is obtained, the supercritical steam and the heavy fuel 9 are supplied to the reformer to produce the reformed fuel 11.

【0028】一定の部分負荷運転までは、改質燃料11
の組成が燃焼に適しないために、コントロールバルブ2
2を閉止し、コントロールバルブ21を開いてパージラ
イン20へ捨てる。負荷が上昇し、改質燃料11の組成
が安定した時点で、コントロールバルブ21を閉止、バ
ルブ21を開いて改質燃料11を燃焼器3へ供給、同時
に軽質燃料12をバルブ19によりコントロールし、改
質燃料11のみでガスタービンを運用する。以上が、起
動から定格までの運転方法である。この場合は、第二実
施例で示したように、バルブ24を開き、超臨界蒸気8
を、軽質油燃料供給系統23へ供給する。超臨界蒸気8
は、供給系統23中の残存軽質燃料12を溶解した後、
燃焼器3へ流入する。十分に、軽質油燃料供給系統23
及び軽質油用燃料ノズル13を超臨界蒸気8でパージし
た後に、蒸気コントロールバルブ24を閉止する。次い
で、空気圧縮機25を起動し、圧縮空気27を軽質燃料
供給系統23へ供給し、供給系統23に残存する蒸気又
はドレインをパージする。その際、改質燃料系統への空
気コントロールバルブ30は閉止される。パージ後、空
気圧縮機25は停止し、パージ操作を終了する。
Up to a certain partial load operation, the reformed fuel 11
Control valve 2 because the composition of is not suitable for combustion
2 is closed, the control valve 21 is opened, and it is discarded into the purge line 20. When the load increases and the composition of the reformed fuel 11 becomes stable, the control valve 21 is closed, the valve 21 is opened to supply the reformed fuel 11 to the combustor 3, and at the same time the light fuel 12 is controlled by the valve 19. The gas turbine is operated only with the reformed fuel 11. The above is the operation method from start to rating. In this case, as shown in the second embodiment, the valve 24 is opened and the supercritical steam 8
Is supplied to the light oil fuel supply system 23. Supercritical steam 8
After dissolving the remaining light fuel 12 in the supply system 23,
It flows into the combustor 3. Light oil fuel supply system 23
After purging the fuel nozzle 13 for light oil with the supercritical steam 8, the steam control valve 24 is closed. Next, the air compressor 25 is started, the compressed air 27 is supplied to the light fuel supply system 23, and the vapor or drain remaining in the supply system 23 is purged. At that time, the air control valve 30 to the reformed fuel system is closed. After purging, the air compressor 25 is stopped, and the purging operation ends.

【0029】逆に負荷が低下する場合は、軽質油燃料の
コントロールバルブ19を開いて軽質燃料12を供給す
ると同時に、改質燃料用コントロールバルブ22を閉止
することにより改質燃料11の燃焼器への供給を停止
し、バルブ21を開いて20の改質燃料パージラインへ
と排出される。軽質燃料12による排熱を利用し、排熱
回収ボイラー6内で、超臨界蒸気8を継続的に発生させ
る。改質燃料11供給停止時には、重質燃料9の供給を
止め、超臨界蒸気8のみを改質器10に供給する。超臨
界蒸気8は、改質器10を素通りし、まず改質燃料パー
ジライン20の流路を十分にパージする。
On the contrary, when the load decreases, the control valve 19 for the light oil fuel is opened to supply the light fuel 12, and at the same time the control valve 22 for the reformed fuel is closed to the combustor of the reformed fuel 11. Is stopped and the valve 21 is opened to discharge the reformed fuel to the reformed fuel purge line 20. The exhaust heat from the light fuel 12 is used to continuously generate the supercritical steam 8 in the exhaust heat recovery boiler 6. When the supply of the reformed fuel 11 is stopped, the supply of the heavy fuel 9 is stopped and only the supercritical steam 8 is supplied to the reformer 10. The supercritical steam 8 passes straight through the reformer 10 and first sufficiently purges the flow path of the reformed fuel purge line 20.

【0030】ついで、コントロールバルブ21を閉止
し、コントロールバルブ22を開くことにより、超臨界
蒸気8は燃料供給系統17を経て、燃焼器3へ流入す
る。十分に、改質燃料供給系統17及び改質燃料ノズル
14を超臨界蒸気8でパージした後に、蒸気コントロー
ルバルブ28を閉止する。次いで、空気圧縮機25を起
動し、圧縮空気27を改質燃料供給系統17へ供給し、
供給系統17に残存する蒸気又はドレインをパージす
る。その際、軽質燃料系統への空気コントロールバルブ
29は閉止される。パージ後、空気圧縮機25は停止
し、パージ操作を終了する。これにより、前記各流路中
に残存する蒸気分をパージすることができる。
Then, by closing the control valve 21 and opening the control valve 22, the supercritical steam 8 flows into the combustor 3 via the fuel supply system 17. After the reforming fuel supply system 17 and the reforming fuel nozzle 14 are sufficiently purged with the supercritical steam 8, the steam control valve 28 is closed. Next, the air compressor 25 is started, compressed air 27 is supplied to the reformed fuel supply system 17,
The steam or drain remaining in the supply system 17 is purged. At that time, the air control valve 29 to the light fuel system is closed. After purging, the air compressor 25 is stopped, and the purging operation ends. As a result, the vapor content remaining in each of the flow paths can be purged.

【0031】[0031]

【発明の効果】本発明によると、重質油の改質燃料焚き
のガスタービンで、改質燃料と軽質燃料との切替え時の
燃料供給系統の詰まりを抑制することができる。
According to the present invention, it is possible to suppress clogging of the fuel supply system at the time of switching between reforming fuel and light fuel in a gas turbine that burns heavy fuel reforming fuel.

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

【図1】本実施例によるガスタービンの燃料系統図。FIG. 1 is a fuel system diagram of a gas turbine according to the present embodiment.

【図2】ガスタービンの燃料系統図。FIG. 2 is a fuel system diagram of a gas turbine.

【図3】本実施例による燃焼器構造図。FIG. 3 is a structural diagram of a combustor according to the present embodiment.

【図4】本実施例によるガスタービンの燃料系統図。FIG. 4 is a fuel system diagram of the gas turbine according to the present embodiment.

【図5】本実施例によるガスタービンの燃料系統図。FIG. 5 is a fuel system diagram of the gas turbine according to the present embodiment.

【符号の説明】[Explanation of symbols]

1…圧縮機、2…タービン、3…燃焼器、4,27…空
気、5…高温排ガス、6…排熱回収ボイラー、7…水、
8…超臨界蒸気、9…重質油、10…改質器、11…改
質燃料、12…軽質燃料、13…軽質油用燃料ノズル、
14…改質燃料用燃料ノズル、15…スワーラー、16
…燃焼ガス、17…改質燃料供給系統、18…重質油コ
ントロールバルブ、19…軽質油燃料コントロールバル
ブ、20…改質燃料パージライン、21,22…改質燃
料用コントロールバルブ、23…軽質油燃料供給系統、
24…軽質油供給系統への超臨界蒸気コントロールバル
ブ、25…空気圧縮機、26…空気供給系統、28…改
質器への超臨界蒸気コントロールバルブ、29…軽質燃
料供給系統への空気コントロールバルブ、30…改質燃
料供給系統への空気コントロールバルブ。
1 ... Compressor, 2 ... Turbine, 3 ... Combustor, 4, 27 ... Air, 5 ... High temperature exhaust gas, 6 ... Exhaust heat recovery boiler, 7 ... Water,
8 ... Supercritical steam, 9 ... Heavy oil, 10 ... Reformer, 11 ... Reformed fuel, 12 ... Light fuel, 13 ... Light oil fuel nozzle,
14 ... Fuel nozzle for reforming fuel, 15 ... Swirler, 16
... combustion gas, 17 ... reformed fuel supply system, 18 ... heavy oil control valve, 19 ... light oil fuel control valve, 20 ... reformed fuel purge line 21,22 ... reformed fuel control valve, 23 ... light Oil fuel supply system,
24 ... Supercritical steam control valve for light oil supply system, 25 ... Air compressor, 26 ... Air supply system, 28 ... Supercritical steam control valve for reformer, 29 ... Air control valve for light fuel supply system , 30 ... Air control valve to the reformed fuel supply system.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 林 明典 茨城県日立市大みか町七丁目2番1号 株 式会社日立製作所電力・電機開発研究所内 (72)発明者 小林 成嘉 茨城県日立市大みか町七丁目2番1号 株 式会社日立製作所電力・電機開発研究所内 (72)発明者 池口 隆 茨城県日立市大みか町七丁目2番1号 株 式会社日立製作所電力・電機開発研究所内 (72)発明者 宮本 知彦 茨城県日立市大みか町七丁目2番1号 株 式会社日立製作所電力・電機開発研究所内 (72)発明者 穂刈 信幸 茨城県日立市大みか町七丁目2番1号 株 式会社日立製作所電力・電機開発研究所内 (72)発明者 高橋 宏和 茨城県日立市大みか町七丁目2番1号 株 式会社日立製作所電力・電機開発研究所内   ─────────────────────────────────────────────────── ─── Continued front page    (72) Inventor Akinori Hayashi             2-12-1 Omika-cho, Hitachi-shi, Ibaraki Prefecture             Ceremony Company Hitachi, Ltd. (72) Inventor Shigeyoshi Kobayashi             2-12-1 Omika-cho, Hitachi-shi, Ibaraki Prefecture             Ceremony Company Hitachi, Ltd. (72) Inventor Takashi Ikeguchi             2-12-1 Omika-cho, Hitachi-shi, Ibaraki Prefecture             Ceremony Company Hitachi, Ltd. (72) Inventor Tomohiko Miyamoto             2-12-1 Omika-cho, Hitachi-shi, Ibaraki Prefecture             Ceremony Company Hitachi, Ltd. (72) Inventor Nobuyuki Hokari             2-12-1 Omika-cho, Hitachi-shi, Ibaraki Prefecture             Ceremony Company Hitachi, Ltd. (72) Inventor Hirokazu Takahashi             2-12-1 Omika-cho, Hitachi-shi, Ibaraki Prefecture             Ceremony Company Hitachi, Ltd.

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】重質油を超臨界蒸気により軽質化した改質
燃料と軽質燃料とを負荷に応じて切替えて燃焼させる燃
焼器を備えたガスタービンであって、 該改質燃料から該軽質燃料に切替える場合に、該改質燃
料の供給停止後に改質燃料供給系統に超臨界乃至亜臨界
蒸気を供給し、該改質燃料供給系統中に残存する重質燃
料をパージする手段を有することを特徴とする改質燃料
焚きガスタービン。
1. A gas turbine comprising a combustor for switching between a reformed fuel obtained by lightening heavy oil by supercritical steam and a light fuel according to a load, and burning the reformed fuel from the reformed fuel to the light fuel. In the case of switching to the fuel, it has means for supplying supercritical or subcritical steam to the reformed fuel supply system after the supply of the reformed fuel is stopped, and purging heavy fuel remaining in the reformed fuel supply system. A reformed fuel-fired gas turbine characterized by:
【請求項2】重質油を超臨界蒸気により軽質化した改質
燃料と軽質燃料とを負荷に応じて切替えて燃焼させる燃
焼器を備えたガスタービンであって、 該軽質燃料から該改質燃料に切替える場合に、該軽質燃
料の供給停止後に軽質燃料供給系統に超臨界乃至亜臨界
蒸気を供給し、該軽質燃料供給系統中に残存する軽質燃
料をパージする手段を有することを特徴とする改質燃料
焚きガスタービン。
2. A gas turbine having a combustor for switching between a reformed fuel obtained by lightening heavy oil by supercritical steam and a light fuel according to a load, and burning the reformed fuel from the light fuel. In the case of switching to fuel, it is characterized by having means for supplying supercritical or subcritical steam to the light fuel supply system after stopping the supply of the light fuel and purging the light fuel remaining in the light fuel supply system. Reformed fuel-fired gas turbine.
【請求項3】超臨界蒸気を発生させる装置と重質油を前
記超臨界蒸気により軽質化する改質器を有し、軽質燃料
及び前記改質燃料を負荷に応じて切替えて燃焼させる燃
焼器からの高温ガスにて駆動されるガスタービンにおい
て、改質燃料から軽質燃料に切替える場合には、改質燃
料供給停止後に改質器及び改質燃料を燃焼器に供給する
系統に超臨界乃至亜臨界蒸気のみを流し、改質器及び供
給系統中に残存する重質燃料をパージすることを特徴と
する改質燃料焚きガスタービン。
3. A combustor having a device for generating supercritical steam and a reformer for lightening heavy oil by the supercritical steam, and combusting the light fuel and the reformed fuel by switching according to load. When switching from reformed fuel to light fuel in a gas turbine that is driven by high-temperature gas from, the supercritical or subcritical fuel is supplied to the reformer and the system that supplies reformed fuel to the combustor after the reformed fuel supply is stopped. A reformed fuel-fired gas turbine, wherein only the critical steam is flowed and the heavy fuel remaining in the reformer and the supply system is purged.
【請求項4】請求項3に記載の改質燃料焚きガスタービ
ンにおいて、灯軽質油等の軽質燃料を改質燃料に切替え
る際にも、軽質燃料供給停止後に軽質燃料供給系統にも
超臨界乃至亜臨界蒸気を供給し、供給系統に残存する軽
質燃料をパージすることを特徴とする改質燃料焚きガス
タービン。
4. The reformed fuel-fired gas turbine according to claim 3, wherein when the light fuel such as light oil is switched to the reformed fuel, the light fuel supply system is supercritical or supercritical after the light fuel supply is stopped. A reformed fuel-fired gas turbine characterized by supplying subcritical steam and purging light fuel remaining in the supply system.
【請求項5】請求項3又は請求項4に記載の改質燃料焚
きガスタービンにおいて、改質燃料供給系及び軽質燃料
供給系統を上記超臨界乃至亜臨界蒸気にてパージした後
に、さらに空気或いは窒素にて供給系統中に存損するド
レインをパージすることを特徴とする改質燃料焚きガス
タービン。
5. The reformed fuel-fired gas turbine according to claim 3 or 4, wherein the reformed fuel supply system and the light fuel supply system are purged with the supercritical or subcritical steam, and then further air or A reformed fuel-fired gas turbine, characterized in that nitrogen is used to purge the drain that is damaged in the supply system.
【請求項6】重質油を超臨界蒸気により軽質化した改質
燃料と軽質燃料とを負荷に応じて切替えて燃焼させる燃
焼器を備えたガスタービンの燃料パージ系統方法であっ
て、 該改質燃料から該軽質燃料に切替える場合に、該改質燃
料の供給停止後に改質燃料供給系統に超臨界乃至亜臨界
蒸気を供給し、該改質燃料供給系統中に残存する重質燃
料をパージすることを特徴とする改質燃料焚きガスター
ビンの燃料系統パージ方法。
6. A fuel purge system method for a gas turbine having a combustor for switching between a reformed fuel obtained by lightening heavy oil by supercritical steam and a light fuel according to a load, the method comprising: When switching from a high-quality fuel to the light fuel, supercritical or subcritical steam is supplied to the reformed fuel supply system after the supply of the reformed fuel is stopped, and the heavy fuel remaining in the reformed fuel supply system is purged. A method of purging a fuel system of a reformed fuel-fired gas turbine, the method comprising:
【請求項7】重質油を超臨界蒸気により改質器で軽質化
した改質燃料と軽質燃料とを負荷に応じて切替えて燃焼
させる燃焼器を備えたガスタービンの燃料系統パージ方
法であって、 該改質燃料から該軽質燃料に切替える場合に、該改質燃
料の供給停止後に該改質器及び改質燃料供給系統に超臨
界乃至亜臨界蒸気を供給し、該改質器及び該改質燃料供
給系統中に残存する重質燃料をパージすることを特徴と
する改質燃料焚きガスタービンの燃料系統パージ方法。
7. A fuel system purging method for a gas turbine equipped with a combustor for switching between a reformed fuel obtained by lightening heavy oil by a supercritical steam in a reformer and a light fuel according to a load. When switching from the reformed fuel to the light fuel, the supercritical or subcritical vapor is supplied to the reformer and the reformed fuel supply system after the supply of the reformed fuel is stopped. A method of purging a fuel system of a reformed fuel-fired gas turbine, characterized in that the heavy fuel remaining in the reformed fuel supply system is purged.
【請求項8】重質油を超臨界蒸気により軽質化した改質
燃料と軽質燃料とを負荷に応じて切替えて燃焼させる燃
焼器を備えたガスタービンの燃料パージ系統方法であっ
て、 該軽質燃料から該改質燃料に切替える場合に、該軽質燃
料の供給停止後に軽質燃料供給系統に超臨界乃至亜臨界
蒸気を供給し、該軽質燃料供給系統中に残存する軽質燃
料をパージすることを特徴とする改質燃料焚きガスター
ビンの燃料系統パージ方法。
8. A fuel purge system method for a gas turbine having a combustor for switching between a reformed fuel obtained by lightening heavy oil by supercritical steam and a light fuel according to a load, the method comprising: When switching from the fuel to the reformed fuel, supercritical or subcritical vapor is supplied to the light fuel supply system after the supply of the light fuel is stopped, and the light fuel remaining in the light fuel supply system is purged. Method of purging fuel system of reformed fuel-fired gas turbine.
JP2001282575A 2001-09-18 2001-09-18 Reformed fuel-fired gas turbine and its fuel system purge method Expired - Fee Related JP3807272B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001282575A JP3807272B2 (en) 2001-09-18 2001-09-18 Reformed fuel-fired gas turbine and its fuel system purge method

Publications (2)

Publication Number Publication Date
JP2003090231A true JP2003090231A (en) 2003-03-28
JP3807272B2 JP3807272B2 (en) 2006-08-09

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Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013104427A (en) * 2011-11-10 2013-05-30 General Electric Co <Ge> System for purging gas fuel circuit for gas turbine engine
JP2013174239A (en) * 2012-02-27 2013-09-05 General Electric Co <Ge> Fuel purging system for turbine assembly

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013104427A (en) * 2011-11-10 2013-05-30 General Electric Co <Ge> System for purging gas fuel circuit for gas turbine engine
JP2013174239A (en) * 2012-02-27 2013-09-05 General Electric Co <Ge> Fuel purging system for turbine assembly
EP2631453A3 (en) * 2012-02-27 2018-03-14 General Electric Company Fuel purging system for a turbine assembly

Also Published As

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