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JPH09221686A - Coal gasification power plant - Google Patents

Coal gasification power plant

Info

Publication number
JPH09221686A
JPH09221686A JP8026563A JP2656396A JPH09221686A JP H09221686 A JPH09221686 A JP H09221686A JP 8026563 A JP8026563 A JP 8026563A JP 2656396 A JP2656396 A JP 2656396A JP H09221686 A JPH09221686 A JP H09221686A
Authority
JP
Japan
Prior art keywords
gas
inert gas
combustor
combustion device
head
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
JP8026563A
Other languages
Japanese (ja)
Other versions
JP3776497B2 (en
Inventor
Shigemi Bandai
重實 萬代
Mitsuru Inada
満 稲田
Osamu Shinada
治 品田
Hiroyuki Nishida
啓之 西田
Nobuo Sato
亘男 佐藤
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 JP02656396A priority Critical patent/JP3776497B2/en
Publication of JPH09221686A publication Critical patent/JPH09221686A/en
Application granted granted Critical
Publication of JP3776497B2 publication Critical patent/JP3776497B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/16Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
    • Y02E20/18Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]

Landscapes

  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a power plant making an air compressor for starting and a gas treating furnace unnecessary and enabling reduction of building area and cost by introducing an inert gas to a gas turbine combustion device, charging from the head or the middle of the combustion device according to calorific value of the inert gas and burning the gas. SOLUTION: The first path for charging an inert gas into a combustion device is provided in the course of body part of a gas turbine combustion device 1 and the second path is provided in the head of the combustion device 1. Further, a fuel nozzle for feeding gas oil which is an auxiliary fuel is provided in the head of the combustion device 1. The charge of an inert gas from the first and second paths and feed of an auxiliary fuel from the combustion nozzle are selected by using calorific vale of the inert gas as an index. Thereby, the objective plant is operated without installing an air compressor and a gas treating facility.

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】本発明は石炭ガス化炉で発生
したガスを用いてガスタービンを作動するようにした石
炭ガス化発電プラントに関する。
TECHNICAL FIELD The present invention relates to a coal gasification power plant in which a gas turbine is operated by using gas generated in a coal gasification furnace.

【0002】[0002]

【従来の技術】図3及び図4に基づいて従来のものを説
明する。図3はこの種石炭ガス化発電プラントの系統図
であり、起動用空気圧縮機9、ガス化炉4、ガス精製設
備10、ガス処理炉11、燃焼器1、ガスタービン5、
圧縮機6、発電機20、空気昇圧機7、排ガスボイラ1
2等によって構成されている。
2. Description of the Related Art A conventional device will be described with reference to FIGS. FIG. 3 is a system diagram of this type of coal gasification power generation plant. The starting air compressor 9, the gasification furnace 4, the gas refining equipment 10, the gas processing furnace 11, the combustor 1, the gas turbine 5,
Compressor 6, generator 20, air booster 7, exhaust gas boiler 1
2 and the like.

【0003】起動時にはガス化炉4を窒素パージしたあ
と、起動用圧縮機9を起動し、ガス化炉4に空気を送
り、ガス化炉4を軽油等(図示省略)にて運転する。そ
の後、ガス化炉4に石炭を投入し、ガス化を行ってい
く。その際、ガス化炉4からは軽油等の燃焼時には窒
素、二酸化炭素水蒸気を主成分とするイナートガスが発
生し、石炭投入後は二酸化炭素に変わり一酸化炭素が増
加し、それと共にガス化ガスの発熱量も増加していく。
At the time of startup, after purging the gasification furnace 4 with nitrogen, the startup compressor 9 is started, air is sent to the gasification furnace 4, and the gasification furnace 4 is operated with light oil or the like (not shown). After that, coal is put into the gasification furnace 4 to carry out gasification. At that time, when gas oil or the like is burned, an inert gas containing nitrogen and carbon dioxide steam as main components is generated from the gasification furnace 4, and after the coal is charged, it is changed to carbon dioxide and carbon monoxide increases, and at the same time, the gasification gas The amount of heat generated also increases.

【0004】一方、ガスタービン5は供給系統を図示省
略した軽油等を燃焼器1で燃焼することによって起動さ
れ、低負荷状態にて運転を行い、圧縮機6、発電機20
を駆動している。ガスタービン5の排ガスは排ガスボイ
ラ12に導かれ熱回収されている。
On the other hand, the gas turbine 5 is started by burning light oil or the like, whose supply system is not shown, in the combustor 1, and is operated in a low load state to operate the compressor 6 and the generator 20.
Is driving. Exhaust gas from the gas turbine 5 is guided to the exhaust gas boiler 12 to recover heat.

【0005】その後、ガスタービン5の圧縮機6からの
空気の一部を抜き取り、その空気を空気昇圧機7によっ
て昇圧してガス化炉4に供給する。ガス化炉4はその分
起動用空気圧縮機9からの空気量を減少させ、最終的に
はガスタービン5で駆動される圧縮機6から抜き取った
空気のみによって運転される。
After that, a part of the air from the compressor 6 of the gas turbine 5 is extracted, and the air is boosted by an air booster 7 and supplied to the gasification furnace 4. The gasification furnace 4 reduces the amount of air from the starting air compressor 9 by that amount, and is finally operated only by the air extracted from the compressor 6 driven by the gas turbine 5.

【0006】また、燃焼器1は、軽油等の燃料を徐々に
減少させ、その分石炭ガス化ガスを導入していく。最終
的には、軽油等の燃料の供給を止め、石炭ガス化ガスの
みを燃焼させガスタービン5を運転する。
Further, the combustor 1 gradually reduces the fuel such as light oil and introduces the coal gasification gas correspondingly. Finally, the supply of fuel such as light oil is stopped and only the coal gasification gas is burned to operate the gas turbine 5.

【0007】停止時には、ガスタービン5で駆動される
圧縮機6から抜き取る空気流量を減少する。それによっ
て結果的に石炭ガス化ガスの供給量が減少するが、その
分軽油等の燃料を投入し、ガスタービン5の運転を維持
する。最終的にガス化炉4の運転に必要最低限の空気を
ガスタービン5で駆動される圧縮機6から抜取っている
状態に移行し、ガスタービン5自体は軽油等のみの燃焼
によって運転される。
At the time of stop, the flow rate of air drawn from the compressor 6 driven by the gas turbine 5 is reduced. As a result, the supply amount of the coal gasification gas is reduced, but fuel such as light oil is added by that amount and the operation of the gas turbine 5 is maintained. Eventually, the minimum amount of air necessary for the operation of the gasification furnace 4 is extracted from the compressor 6 driven by the gas turbine 5, and the gas turbine 5 itself is operated by burning only light oil or the like. .

【0008】このような一連の作動において、ガス化炉
起動時、石炭投入直後、またガス化炉停止時では、ガス
化炉4からでてくるガスは既燃ガスであるかあるいは発
熱量が非常に低いガス(これらのガスを含み石炭ガス化
ガスを総称して本明細書ではイナートガスという)であ
るためガスタービン5の作動用として使用することがで
きない。
In such a series of operations, at the time of starting the gasifier, immediately after the coal is charged, or when the gasifier is stopped, the gas emitted from the gasifier 4 is a burnt gas or has an extremely high calorific value. Since it is a very low gas (a coal gasification gas including these gases is generically referred to as an inert gas in this specification), it cannot be used for operating the gas turbine 5.

【0009】しかし、低発熱量ガスとはいえ、そのまま
大気解放することはできないため、ガス処理炉11で軽
油を用いて燃焼させている。ガス処理設備は図4に示す
ように、軽油などの主燃料に図に示していない点火装置
によって点火し、この主燃料を燃焼させ、イナートガス
は発熱量によって、主燃料供給部周囲あるいは主燃料に
よる火炎の下流に投入して可燃分を燃焼させている。
However, even though the gas has a low calorific value, it cannot be exposed to the atmosphere as it is. Therefore, the gas processing furnace 11 is burned with light oil. As shown in FIG. 4, the gas treatment equipment ignites a main fuel such as light oil by an ignition device (not shown) and burns this main fuel, and the inert gas is generated around the main fuel supply section or by the main fuel depending on the calorific value. It is injected downstream of the flame to burn combustible components.

【0010】[0010]

【発明が解決しようとする課題】従来稼働中の石炭ガス
化発電プラントでは前記のような構成となっているが、
起動用空気圧縮機9およびガス処理設備11は、石炭ガ
ス化発電プラントの建設面積、建設コストのかなりの部
分を占める結果となっている。ほかの方式による発電設
備と比較して建設面積、建設費が莫大である石炭ガス化
発電プラントにおいては、設備の簡略化による施設面積
の縮小、建設費の低下を図ることが課題となっている。
Although the conventional coal gasification power plant which is in operation has the above-mentioned structure,
The start-up air compressor 9 and the gas treatment facility 11 occupy a considerable part of the construction area and construction cost of the coal gasification power generation plant. In the coal gasification power plant, where the construction area and construction cost are enormous compared to other types of power generation equipment, it is an issue to reduce the facility area and construction cost by simplifying the equipment. .

【0011】[0011]

【課題を解決するための手段】本発明は、前記課題を解
決するべくなされたもので、ガスタービン燃焼器内へイ
ナートガスを投入する第1の経路と第2の経路のうち前
者を同燃焼器の胴部途中に後者を同燃焼器の頭部に設け
ると共に、軽油等の助燃燃料を供給する燃料ノズルを前
記燃焼器の頭部に設けてなり、前記イナートガスの発熱
量を指針として前記第1、第2の経路及び燃料ノズルを
選択的に作動させるようにした石炭ガス化発電プラント
を提供し、ガスタービン燃焼器にイナートガスを導き、
同イナートガスの発熱量に応じて燃焼器の胴部途中の第
1経路と燃焼器頭部の第2経路を選択してイナートガス
を投入し、更に燃焼器頭部からの軽油等の助燃燃料を選
択的に供給して燃焼させることにより、起動用空気圧縮
機及びガス処理設備の省略を図るようにしたものであ
る。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and the former of the first path and the second path for injecting inert gas into the gas turbine combustor is the same combustor. The latter is provided in the head of the combustor in the middle of the body, and a fuel nozzle for supplying auxiliary combustion fuel such as light oil is provided in the head of the combustor, and the first calorific value of the inert gas is used as a guide. Providing a coal gasification power plant adapted to selectively actuate a second path and a fuel nozzle, directing inert gas to a gas turbine combustor,
According to the calorific value of the inert gas, select the 1st path in the middle of the combustor and the 2nd path of the combustor head to inject the inert gas, and then select the auxiliary fuel such as light oil from the combustor head. The starting air compressor and the gas treatment facility are omitted by supplying and combusting the gas.

【0012】[0012]

【発明の実施の形態】本発明の実施の一形態を図1、図
2に基づいて説明する。なお、先に従来の技術として説
明したものと同一の部位については図面中に同一の符号
を付して示し、重複する説明は省略する。
BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of the present invention will be described with reference to FIGS. It should be noted that the same parts as those described as the related art previously are designated by the same reference numerals in the drawings, and overlapping description will be omitted.

【0013】プラント起動前にガス化炉4を窒素パージ
したあと、軽油等8を燃焼器1に供給し燃焼させること
によってガスタービン5を起動し、圧縮機6からの空気
を一部抜取り、これを空気昇圧機7にて更に昇圧し、ガ
ス化炉4に空気を送る。その空気を使い図示省略の系路
から供給した軽油等の燃料を燃焼させガス化炉4を運転
する。
After the gasification furnace 4 is purged with nitrogen before the plant is started, the gas turbine 5 is started by supplying light oil 8 to the combustor 1 and burning it, and a part of the air from the compressor 6 is extracted. Is further boosted by the air booster 7, and air is sent to the gasification furnace 4. The air is used to burn a fuel such as light oil supplied from a system (not shown) to operate the gasification furnace 4.

【0014】その後、ガス化炉4に石炭を投入し、ガス
化を行っていく。その際、ガス化炉4からは軽油燃焼時
には窒素、二酸化炭素、水蒸気を主成分とするイナート
ガスが発生し、石炭投入後は二酸化炭素に変わり一酸化
炭素が増加し、それと共に同イナートガスの発熱量も増
加していく。
After that, coal is put into the gasification furnace 4 to carry out gasification. At that time, an inert gas containing nitrogen, carbon dioxide, and steam as main components is generated from the gasification furnace 4 during combustion of light oil, and after coal is added, carbon monoxide increases and carbon monoxide increases, and at the same time, the calorific value of the inert gas. Will also increase.

【0015】これらイナートガスをガス精製設備10を
経てガスタービン5の燃焼器1に導き、イナートガスの
発熱量に応じて燃焼器頭部あるいは途中より投入し燃焼
させる。即ち、イナートガスの発熱量が低く、燃焼しが
たい時には、燃焼器1の途中にあるバイパス弁3のすぐ
上流に設けた第1の経路1Aからイナートガスを燃焼器
内1に投入して燃焼させる。
These inert gases are introduced into the combustor 1 of the gas turbine 5 through the gas refining equipment 10, and are injected from the head of the combustor or in the middle thereof in accordance with the amount of heat generated by the inert gas and burned. That is, when the calorific value of the inert gas is low and it is difficult to burn the inert gas, the inert gas is injected into the combustor 1 through the first path 1A provided immediately upstream of the bypass valve 3 in the middle of the combustor 1 and burned.

【0016】このバイパス弁3は、通常燃焼器1の上流
側に流入する空気流量を調整することを目的に設けられ
ているもので、弁3を開けることにより燃焼器1の頭部
をバイパスし、燃焼器1の途中から空気を合流させる目
的で設けられているものである。
The bypass valve 3 is provided for the purpose of adjusting the flow rate of the air that normally flows into the upstream side of the combustor 1. By opening the valve 3, the head of the combustor 1 is bypassed. It is provided for the purpose of merging air from the middle of the combustor 1.

【0017】一方、イナートガスの発熱量が上昇してく
ると、図示省略したイナートガス成分分析をする装置に
よって計算される発熱量を指針に、軽油等の燃料8を供
給したまま、ガスタービン燃焼器1の頭部にある燃料ス
ワラ2等よりなる第2の経路1Bからイナートガスを投
入して燃焼させる。このとき、燃焼器1の出口(タービ
ン5の第1段静翼13の入口)の温度が一定になるよう
に図示省略した適宜の制御装置で軽油等の燃料流量を調
整する。
On the other hand, when the calorific value of the inert gas rises, the gas turbine combustor 1 is supplied with the fuel 8 such as light oil being supplied, with the calorific value calculated by a device (not shown) for analyzing the inert gas component as a guide. The inert gas is injected from the second path 1B including the fuel swirler 2 and the like at the head of the engine and burned. At this time, the flow rate of fuel such as light oil is adjusted by an appropriate control device (not shown) so that the temperature of the outlet of the combustor 1 (the inlet of the first stage vane 13 of the turbine 5) becomes constant.

【0018】イナートガスの発熱量が更に上昇し、単独
で燃焼するようになると、軽油等燃料の供給を止め、石
炭ガス化ガスであるイナートガスのみを燃焼させてガス
タービン5を運転する通常の運転方式となる。
When the calorific value of the inert gas further rises and starts to burn independently, the supply of fuel such as light oil is stopped and only the inert gas which is a coal gasification gas is burned to operate the gas turbine 5. Becomes

【0019】なお、停止する時には、ガス化炉4への石
炭投入を停止する。それによって結果的に石炭ガス化ガ
スの発熱量が減少するが、その分軽油等の助燃燃料を燃
焼器1に投入燃焼しガスタービン5の運転を維持する。
At the time of stopping, the coal charging to the gasification furnace 4 is stopped. As a result, the calorific value of the coal gasification gas is reduced, but the auxiliary combustion fuel such as light oil is injected into the combustor 1 and burned to maintain the operation of the gas turbine 5.

【0020】イナートガス成分分析によって計算される
発熱量を指針に、途中からガス供給をバイパス弁3の上
流の第1の経路1Aからの供給に切り替え、最終的にガ
ス化炉4の運転に必要最低限の空気をガスタービン5か
ら抜きとる形態に移行し、ガスタービン5自体は軽油の
みの燃焼によって運転される。
Using the calorific value calculated by the inert gas component analysis as a guide, the gas supply is switched from the middle to the supply from the first path 1A upstream of the bypass valve 3 and finally the minimum required for the operation of the gasification furnace 4. A transition is made to a mode in which a limited amount of air is extracted from the gas turbine 5, and the gas turbine 5 itself is operated by burning only light oil.

【0021】このように本実施の形態によれば、従来の
もののように起動用空気圧縮機もガス処理炉も不要とし
てプラントの運転を行うことができるものである。そし
て、このガスタービン5が運転される結果、発電機20
が駆動されて所定の電力が得られ、これにより、発電プ
ラントということになる。
As described above, according to this embodiment, the plant can be operated without the need for the starting air compressor and the gas treatment furnace, unlike the conventional one. Then, as a result of operating the gas turbine 5, the generator 20
Is driven to obtain a predetermined amount of electric power, which is a power plant.

【0022】なお、ガスタービン5の排気は排ガスボイ
ラ12に導入されており、それ以降については図面では
省略しているが、この排ガスボイラ12で発生した蒸気
で蒸気タービンを作動して別途発電を行えば、前記発電
機20と併せて、ここに複合発電プラントを完成できる
ことは、改めて言うまでもないことである。
The exhaust gas of the gas turbine 5 is introduced into the exhaust gas boiler 12, and the subsequent steps are omitted in the drawing, but the steam generated by the exhaust gas boiler 12 operates the steam turbine to generate electricity separately. It goes without saying that, if done, the combined power generation plant can be completed here together with the generator 20.

【0023】従って、その場合には本明細書において石
炭ガス化発電プラントと言うのは、石炭ガス化複合発電
プラントと適宜読み替えてもよいものである。
Therefore, in this case, the term "coal gasification power generation plant" in this specification may be appropriately read as "coal gasification combined cycle power generation plant".

【0024】以上、本発明を図示の実施の形態について
説明したが、本発明はかかる実施の形態に限定されず、
本発明の範囲内でその具体的構造に種々の変更を加えて
よいことはいうまでもない。
Although the present invention has been described with reference to the illustrated embodiment, the present invention is not limited to such an embodiment.
It goes without saying that various modifications may be made to the specific structure within the scope of the present invention.

【0025】[0025]

【発明の効果】以上、本発明によれば、ガスタービン燃
焼器にイナートガスを導き、イナートガスの発熱量に応
じて燃焼器頭部あるいは途中より投入し燃焼させること
により、起動用空気圧縮機及びガス処理炉を不要とし、
建設面積、コストの縮小を可能とした発電プラントを得
ることができたものである。
As described above, according to the present invention, the inert gas is introduced into the gas turbine combustor, and the starting air compressor and the gas are injected by burning the inert gas from the head of the combustor or in the middle of the combustor according to the calorific value of the inert gas. No processing furnace required,
We were able to obtain a power generation plant that made it possible to reduce the construction area and cost.

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

【図1】本発明の実施の一形態に係る石炭ガス化発電プ
ラントに用いる燃焼器の概略図。
FIG. 1 is a schematic diagram of a combustor used in a coal gasification power plant according to an embodiment of the present invention.

【図2】図1の燃焼器を組入れた石炭ガス化発電プラン
トの系統図。
FIG. 2 is a system diagram of a coal gasification power plant incorporating the combustor of FIG.

【図3】従来の石炭ガス化発電プラントの系統図。FIG. 3 is a system diagram of a conventional coal gasification power generation plant.

【図4】図3のものに組入れられるガス処理炉の概略
図。
FIG. 4 is a schematic diagram of a gas treatment furnace incorporated into that of FIG.

【符号の説明】[Explanation of symbols]

1 燃焼器 3 バイパス弁 4 ガス化炉 5 ガスタービン 6 圧縮機 12 排ガスボイラ 20 発電機 1A 第1の経路 1B 第2の経路 1 Combustor 3 Bypass Valve 4 Gasification Furnace 5 Gas Turbine 6 Compressor 12 Exhaust Gas Boiler 20 Generator 1A 1st Route 1B 2nd Route

───────────────────────────────────────────────────── フロントページの続き (72)発明者 西田 啓之 兵庫県高砂市荒井町新浜二丁目1番1号 三菱重工業株式会社高砂研究所内 (72)発明者 佐藤 亘男 兵庫県高砂市荒井町新浜2丁目8番19号 高菱エンジニアリング株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Hiroyuki Nishida, Inventor Hiroyuki Nishihama 1-1-1, Arai-cho, Takasago-shi, Hyogo Mitsubishi Heavy Industries, Ltd. Takasago Research Center (72) Inventor Watao Sato 2-chome, Niihama, Arai-cho, Takasago-shi, Hyogo No. 19 Takahishi Engineering Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 ガスタービン燃焼器内へイナートガスを
投入する第1の経路と第2の経路のうち前者を同燃焼器
の胴部途中に後者を同燃焼器の頭部に設けると共に、軽
油等の助燃燃料を供給する燃料ノズルを前記燃焼器の頭
部に設けてなり、前記イナートガスの発熱量を指針とし
て前記第1、第2の経路及び燃料ノズルを選択的に作動
させるようにしたことを特徴とする石炭ガス化発電プラ
ント。
1. A first path and a second path for injecting inert gas into a gas turbine combustor, the former is provided in the middle of the body of the combustor and the latter is installed at the head of the combustor, and light oil, etc. A fuel nozzle for supplying auxiliary combustion fuel is provided at the head of the combustor, and the first and second paths and the fuel nozzle are selectively operated by using the calorific value of the inert gas as a guide. Characteristic coal gasification power plant.
JP02656396A 1996-02-14 1996-02-14 Coal gasification power plant Expired - Lifetime JP3776497B2 (en)

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Application Number Priority Date Filing Date Title
JP02656396A JP3776497B2 (en) 1996-02-14 1996-02-14 Coal gasification power plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP02656396A JP3776497B2 (en) 1996-02-14 1996-02-14 Coal gasification power plant

Publications (2)

Publication Number Publication Date
JPH09221686A true JPH09221686A (en) 1997-08-26
JP3776497B2 JP3776497B2 (en) 2006-05-17

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Application Number Title Priority Date Filing Date
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008163873A (en) * 2006-12-28 2008-07-17 Mitsubishi Heavy Ind Ltd Solid fuel gasified gas using plant
WO2008149731A1 (en) * 2007-05-30 2008-12-11 Mitsubishi Heavy Industries, Ltd. Integrated gasification combined cycle plant
JP2010168951A (en) * 2009-01-21 2010-08-05 Kawasaki Plant Systems Ltd Stable operating method for gasification power generation plant and gasification power generation plant
CN104832231A (en) * 2015-04-27 2015-08-12 南京瑞柯徕姆环保科技有限公司 Fuel heat treatment furnace flue gas residual heat power generation method and device

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008163873A (en) * 2006-12-28 2008-07-17 Mitsubishi Heavy Ind Ltd Solid fuel gasified gas using plant
WO2008149731A1 (en) * 2007-05-30 2008-12-11 Mitsubishi Heavy Industries, Ltd. Integrated gasification combined cycle plant
JPWO2008149731A1 (en) * 2007-05-30 2010-08-26 三菱重工業株式会社 Gasification combined power plant
US8028511B2 (en) 2007-05-30 2011-10-04 Mitsubishi Heavy Industries, Ltd. Integrated gasification combined cycle power generation plant
JP4981901B2 (en) * 2007-05-30 2012-07-25 三菱重工業株式会社 Gasification combined power plant
KR101175577B1 (en) * 2007-05-30 2012-08-21 미츠비시 쥬고교 가부시키가이샤 Integrated gasification combined cycle plant
JP2010168951A (en) * 2009-01-21 2010-08-05 Kawasaki Plant Systems Ltd Stable operating method for gasification power generation plant and gasification power generation plant
CN104832231A (en) * 2015-04-27 2015-08-12 南京瑞柯徕姆环保科技有限公司 Fuel heat treatment furnace flue gas residual heat power generation method and device

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