JPH07208111A - Exhaust afterburning compound cycle plant - Google Patents
Exhaust afterburning compound cycle plantInfo
- Publication number
- JPH07208111A JPH07208111A JP199794A JP199794A JPH07208111A JP H07208111 A JPH07208111 A JP H07208111A JP 199794 A JP199794 A JP 199794A JP 199794 A JP199794 A JP 199794A JP H07208111 A JPH07208111 A JP H07208111A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- oil
- fuel
- cycle plant
- exhaust
- 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
Links
- 150000001875 compounds Chemical class 0.000 title abstract 4
- 239000003921 oil Substances 0.000 claims abstract description 43
- 239000000295 fuel oil Substances 0.000 claims abstract description 34
- 239000000446 fuel Substances 0.000 claims abstract description 32
- 238000002485 combustion reaction Methods 0.000 claims abstract description 31
- 239000010779 crude oil Substances 0.000 claims description 17
- 239000006200 vaporizer Substances 0.000 claims description 14
- 238000000926 separation method Methods 0.000 claims description 2
- 238000005260 corrosion Methods 0.000 abstract description 5
- 230000007797 corrosion Effects 0.000 abstract description 5
- 239000007789 gas Substances 0.000 description 72
- 238000010586 diagram Methods 0.000 description 5
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 4
- 238000002309 gasification Methods 0.000 description 4
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- 239000011593 sulfur Substances 0.000 description 3
- 238000004821 distillation Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 1
- -1 etc. Chemical compound 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K23/00—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
- F01K23/02—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
- F01K23/06—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
- F01K23/10—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle with exhaust fluid of one cycle heating the fluid in another cycle
- F01K23/103—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle with exhaust fluid of one cycle heating the fluid in another cycle with afterburner in exhaust boiler
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
- Liquid Carbonaceous Fuels (AREA)
Abstract
Description
【０００１】[0001]
【産業上の利用分野】本発明は、ガスタービン、同ガス
タービンの排気ガスによる排気再燃ボイラ、及び同排気
再燃ボイラから蒸気の供給を受ける蒸気タービンを有す
る排気再燃複合サイクルプラントに関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas re-combustion combined cycle plant having a gas turbine, an exhaust gas re-combustion boiler using the exhaust gas of the gas turbine, and a steam turbine supplied with steam from the exhaust gas re-combustion boiler.
【０００２】[0002]
【従来の技術】従来の排気再燃複合サイクルプラント
は、図４に示すように、ガスタービン２３の排気ガス２
８を燃焼用空気として、又はその排気ガス２８を燃焼用
空気の一部とし他に空気２６を供給して、油輸送ライン
２４からの燃料を燃焼する排気再燃ボイラ２１を備え、
そのボイラ２１が発生する蒸気で蒸気タービン２２を駆
動する構成を有している。ガスタービン２３には天然ガ
スや軽質油等のガスタービン用燃料２５と空気２６が供
給される。２７はボイラ２１のスタックである。2. Description of the Related Art A conventional exhaust gas re-combustion combined cycle plant, as shown in FIG.
8 is used as combustion air, or its exhaust gas 28 is used as a part of combustion air to supply air 26 to the other, and an exhaust gas reburn boiler 21 for burning fuel from the oil transportation line 24 is provided,
The steam turbine 22 is driven by the steam generated by the boiler 21. Gas turbine fuel 25 such as natural gas or light oil and air 26 are supplied to gas turbine 23. 27 is a stack of the boiler 21.
【０００３】また、燃料油をガス化してガスタービンの
燃料とする従来の油ガス化複合サイクルは図５に示す構
成を有している。図５において、２９はガス化炉で、油
輸送ライン３０から供給される油と空気２６からガス化
燃料３１をつくり、それをガスタービン２３へ燃料とし
て供給する。ガスタービン２３の排気ガス２８は排ガス
ボイラ３２へ供給され排ガスボイラ３２の発生蒸気で蒸
気タービン２２が駆動される。A conventional oil-gasification combined cycle in which fuel oil is gasified to be used as fuel for a gas turbine has a structure shown in FIG. In FIG. 5, 29 is a gasification furnace, which produces gasification fuel 31 from oil and air 26 supplied from an oil transportation line 30, and supplies it to the gas turbine 23 as fuel. The exhaust gas 28 of the gas turbine 23 is supplied to the exhaust gas boiler 32, and the steam generated by the exhaust gas boiler 32 drives the steam turbine 22.
【０００４】[0004]
【発明が解決しようとする課題】前記したような従来の
複合サイクルプラントにおいて、原油を燃料とした場
合、含有される硫黄分による高温腐食を防止するため、
ガスタービンでの生焚き時には燃焼温度の制限、耐食材
料開発という問題が生じ、また図５に示されたもののよ
うに原油をガス化させて燃料としても、その成分はＣ
Ｏ，Ｈ2 , ＣＯ2 , Ｎ 2 , Ｈ2 Ｓ等であり、そのＨ2 Ｓ
（硫化水素）等の腐食性ガス対策が必要となる。DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention
When using crude oil as fuel in a combined cycle plant
In order to prevent high temperature corrosion due to contained sulfur,
Limits combustion temperature and raw materials when burning with gas turbine
There is a problem of fee development,
Even if the crude oil is gasified and used as fuel, its component is C
O, H2,CO2,N 2,H2S, etc., and its H2S
Measures against corrosive gases such as (hydrogen sulfide) are required.
【０００５】本発明は、ガスタービン、同ガスタービン
の排気ガスによる排気再燃ボイラ、及び同排気再燃ボイ
ラから蒸気の供給を受ける蒸気タービンを有し原油を燃
料とした排気再燃複合サイクルプラントにおいて、高温
燃焼を可能としつつもガスタービンの腐食を防止し、ま
た効率を高めた排気再燃複合サイクルプラントを提供す
ることを課題としている。The present invention relates to an exhaust gas re-combustion combined cycle plant that uses a crude oil as a fuel and has a high temperature in a gas turbine, an exhaust gas re-combustion boiler using the exhaust gas of the gas turbine, and a steam turbine that is supplied with steam from the exhaust gas re-combustion boiler. It is an object of the present invention to provide an exhaust gas re-combustion combined cycle plant that enables combustion, prevents gas turbine corrosion, and improves efficiency.
【０００６】[0006]
【課題を解決するための手段と作用】本発明は、ガスタ
ービン、同ガスタービンの排気ガスによる排気再燃ボイ
ラ、及び同排気再燃ボイラから蒸気の供給を受ける蒸気
タービンを有し原油を燃料とした排気再燃複合サイクル
プラントにおける前記課題を解決するため、その排気再
燃複合サイクル内に原油を軽質油分と重質油に分離する
ための気化器（分溜器）を設置し、分離して得た軽質油
分は前記ガスタービンの、また分離重質油は排気再燃ボ
イラの燃料とする構成を採用する。SUMMARY OF THE INVENTION The present invention has a gas turbine, an exhaust gas reburning boiler using the exhaust gas of the gas turbine, and a steam turbine supplied with steam from the exhaust gas reburning boiler, and uses crude oil as fuel. In order to solve the above problems in an exhaust gas re-combustion combined cycle plant, a vaporizer (distiller) for separating crude oil into a light oil component and a heavy oil is installed in the exhaust gas re-combustion combined cycle plant The oil content is used as the fuel of the gas turbine, and the separated heavy oil is used as the fuel of the exhaust gas reburning boiler.
【０００７】このように構成した本発明による排気再燃
複合サイクルプラントにおいては、原油を軽質油分と重
質油に分離する気化器（分溜器）を備えていて燃料の原
油は軽質油分と重質油に分けられ、原油中の硫黄分は、
軽質油を分離後の重質油（重油）に残るため、軽質油分
はクリーンな燃料としてガスタービン燃料に使用でき
る。In the exhaust gas re-combustion combined cycle plant according to the present invention configured as described above, the vaporizer (distiller) for separating the crude oil into the light oil content and the heavy oil is provided, and the crude oil of the fuel is the light oil content and the heavy oil. Divided into oil, the sulfur content in crude oil is
Since the light oil remains in the separated heavy oil (heavy oil), the light oil can be used as a clean fuel for the gas turbine fuel.
【０００８】一方、分離された重質油は、既に高Ｓ分油
燃焼ボイラとして実績のある従来技術を用いて排気再燃
ボイラの燃料に利用できる。このように、本発明の排気
再燃複合サイクルプラントによれば原油を燃料としつゝ
も腐食の恐れなくガスタービンでの高温燃焼を可能とす
る。なお、気化器（分溜器）で得られた軽質油分はその
まゝガスタービンの燃料としてもよいし或いは凝縮器で
液体化してからガスタービンに供給してもよい。On the other hand, the separated heavy oil can be used as a fuel for an exhaust gas reburning boiler by using the conventional technique which has already been proven as a high S component oil combustion boiler. As described above, according to the exhaust gas re-combustion combined cycle plant of the present invention, it is possible to use high temperature combustion in a gas turbine without fear of using crude oil as fuel. The light oil obtained in the vaporizer (distiller) may be used as fuel for the gas turbine as it is, or may be liquefied by the condenser and then supplied to the gas turbine.
【０００９】また、他の本発明においては、前記した構
成に加え、前記気化器（分溜器）に連通され前記重質油
を貯蔵する重質油貯蔵タンク、及び前記気化器で分離し
て得られた軽質油を貯蔵する軽質油貯蔵タンクを具えた
構成を採用する。このように構成することによって、分
離後の軽質油と重質油はそれぞれのタンクに貯蔵できる
ので、分離生成される軽質油と重質油の量と、ガスター
ビン及び排気再燃ボイラで燃焼される燃料量との差がこ
のタンクで吸収される。これによって燃料の安定供給が
可能となる。In addition, in another aspect of the present invention, in addition to the above-described structure, a heavy oil storage tank which communicates with the vaporizer (distiller) and stores the heavy oil, and a heavy oil storage tank which separates the heavy oil are separated. A configuration including a light oil storage tank for storing the obtained light oil is adopted. With this configuration, the separated light oil and heavy oil can be stored in their respective tanks, so the amount of light oil and heavy oil that are separated and produced, and the amount of light oil and heavy oil that are separated and produced, are burned in the gas turbine and the exhaust gas reburn boiler. The difference from the fuel quantity is absorbed in this tank. This enables a stable supply of fuel.
【００１０】[0010]
【実施例】以下本発明を図示した実施例に基づいて具体
的に説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be specifically described below based on the illustrated embodiments.
【００１１】（第１実施例）まず、図１に示した第１実
施例について説明する。図１において、１は排気再燃ボ
イラである。２は蒸気タービンで、排気再燃ボイラ１か
ら蒸気供給ライン１０を介して蒸気が供給される。３は
ガスタービンで、その排気ガスは、ガスタービン排気ガ
ス供給ライン８を経て排気再燃ボイラ１の風箱・バーナ
１１に供給される。４は気化器（分溜器）で原油輸送ラ
イン５から供給される原油を重質油と軽質油分に分離
し、軽質油分は軽質油供給ライン７、重質油は重質油供
給ライン６へ送られる。原油中には軽質油としてのガソ
リン、灯油及び軽油が合計で約５０％含まれている。(First Embodiment) First, the first embodiment shown in FIG. 1 will be described. In FIG. 1, reference numeral 1 is an exhaust gas reburning boiler. A steam turbine 2 is supplied with steam from the exhaust gas reburning boiler 1 through a steam supply line 10. Reference numeral 3 is a gas turbine, and its exhaust gas is supplied to a wind box / burner 11 of the exhaust gas reburning boiler 1 via a gas turbine exhaust gas supply line 8. A vaporizer (distiller) 4 separates crude oil supplied from a crude oil transport line 5 into heavy oil and light oil, and light oil to a light oil supply line 7 and heavy oil to a heavy oil supply line 6. Sent. Crude oil contains about 50% of gasoline, kerosene and light oil as light oil in total.
【００１２】１２は凝縮器で、気化器４から送られて来
る蒸留分離後の軽質油分を液体化する。液体化された軽
質油は軽質油加圧ポンプ１３によってガスタービンへ送
られ燃焼用空気９によって燃焼される。重質油は重質油
加圧ポンプ１５によって排気再燃ボイラ１へ送られ、ガ
スタービン排ガス供給ライン８からの排気ガスを燃焼用
空気の一部として燃焼用空気９によって燃焼される。な
お、凝縮器１２を用いずに気化器（分溜器）４からの軽
質油分をガスタービン３に直接導いてもよい。Numeral 12 is a condenser, which liquefies the light oil component after distillation separation sent from the vaporizer 4. The liquefied light oil is sent to the gas turbine by the light oil pressure pump 13 and burned by the combustion air 9. The heavy oil is sent to the exhaust gas reburning boiler 1 by the heavy oil pressure pump 15, and the exhaust gas from the gas turbine exhaust gas supply line 8 is burned by the combustion air 9 as a part of the combustion air. The light oil content from the vaporizer (distiller) 4 may be directly introduced to the gas turbine 3 without using the condenser 12.
【００１３】このように、図１に示した排気再燃複合サ
イクルプラントにおいてはガスタービン３で腐食の恐れ
なくクリーンな軽質油が高温燃焼され、原油中の硫黄分
は排気再燃ボイラ１において問題なく燃焼できる。ま
た、図２に示すように気化器４の熱源としてタービンか
らの抽気１６を用いることによってシステムの効率増加
をはかることができる。As described above, in the exhaust gas re-combustion combined cycle plant shown in FIG. 1, clean light oil is burned at high temperature in the gas turbine 3 without fear of corrosion, and the sulfur content in the crude oil is burned in the exhaust gas re-burning boiler 1 without any problem. it can. Further, as shown in FIG. 2, by using the extraction air 16 from the turbine as the heat source of the carburetor 4, the efficiency of the system can be increased.
【００１４】（第２実施例）本発明による排気再燃複合
サイクルプラントの第２実施例を図３に示してある。図
３において図１に示した複合サイクルプラントと同じ機
器には同じ符号を付してあり、それらについての重複す
る説明は省略する。図３に示す複合サイクルにおいて
は、凝縮器１２の後流の軽質油供給ライン７に軽質油貯
蔵タンクＡが配設されている。また、重質油供給ライン
６には重質油貯蔵タンクＢが配設されている。(Second Embodiment) FIG. 3 shows a second embodiment of the exhaust gas reburn combined cycle plant according to the present invention. In FIG. 3, the same components as those of the combined cycle plant shown in FIG. 1 are designated by the same reference numerals, and duplicate description thereof will be omitted. In the combined cycle shown in FIG. 3, the light oil storage tank A is arranged in the light oil supply line 7 downstream of the condenser 12. A heavy oil storage tank B is arranged in the heavy oil supply line 6.
【００１５】この第２実施例による複合サイクルプラン
トでは、気化器（分溜器）４で分離した軽質油分と重質
油分をそれぞれ貯蔵タンクＡ，Ｂに貯蔵し、気化器（分
溜器）４で分離生成される軽質油、重質油の量（発生燃
料）とガスタービン３、ボイラ１で燃焼させる燃料（消
費燃料）の時定数の違いをこの貯蔵タンクＡ，Ｂに一時
的に貯蔵することにより吸収する。In the combined cycle plant according to the second embodiment, the light oil component and the heavy oil component separated by the vaporizer (distiller) 4 are stored in storage tanks A and B, respectively, and the vaporizer (distiller) 4 is stored. The difference between the time constants of the amounts of light oil and heavy oil (generated fuel) that are separated and produced in step S1 and the fuel (consumed fuel) burned in the gas turbine 3 and the boiler 1 is temporarily stored in the storage tanks A and B. Absorb by
【００１６】また、軽質油貯蔵タンクＡからの払出しを
ボイラ１側へも可能とすればガスタービン３、ボイラ１
の受持つ負荷のバランスが違ってもタンクがオーバフロ
ーする事なく発生燃料をすべて消費できる。以上、本発
明を図示した実施例に基づいて具体的に説明したが、本
発明がこれらの実施例に限定されず特許請求の範囲に示
す本発明の範囲内で、その形状、構造に種々の変更を加
えてよいことはいうまでもない。If the light oil storage tank A can also be discharged to the boiler 1 side, the gas turbine 3 and the boiler 1
Even if the load balance of the vehicle is different, all the generated fuel can be consumed without the tank overflowing. The present invention has been specifically described above based on the illustrated embodiments, but the present invention is not limited to these embodiments, and within the scope of the present invention set forth in the claims, various shapes and structures can be used. It goes without saying that changes may be made.
【００１７】[0017]
【発明の効果】以上詳細に説明したように本発明による
排気再燃複合サイクルプラントにおいては燃料の原油を
重質油分と軽質油に蒸留分離し、軽質油分のみガスター
ビン燃料として供するため、ガスタービンの腐食を防
止、抑制しつつ、高温度燃焼が可能となり高効率運転が
可能となる。また、原油をガス化して燃料とする場合の
ように金属に対し腐食性の高い硫化水素が発生すること
もない。また、気化器（分溜器）の高温熱源に、タービ
ンの抽気を利用することにより、システムの効率面でも
有利となる。As described above in detail, in the exhaust gas re-combustion combined cycle plant according to the present invention, the crude oil of the fuel is separated into the heavy oil and the light oil by distillation, and only the light oil is used as the gas turbine fuel. High-temperature combustion becomes possible and high-efficiency operation becomes possible while preventing and suppressing corrosion. In addition, hydrogen sulfide, which is highly corrosive to metals, unlike the case where crude oil is gasified and used as fuel, is not generated. Further, by utilizing the extraction air of the turbine as the high temperature heat source of the vaporizer (distiller), it is advantageous in terms of system efficiency.
【図１】本発明の第１実施例による排気再燃複合サイク
ルプラントを示す機器系統図。FIG. 1 is an equipment system diagram showing an exhaust gas recombustion combined cycle plant according to a first embodiment of the present invention.
【図２】第１実施例の変形を示す機器系統図。FIG. 2 is a device system diagram showing a modification of the first embodiment.
【図３】本発明の第２実施例による排気再燃複合サイク
ルプラントを示す機器系統図。FIG. 3 is an equipment system diagram showing an exhaust gas recombustion combined cycle plant according to a second embodiment of the present invention.
【図４】従来の排気再燃複合サイクルプラントを示す機
器系統図。FIG. 4 is an equipment system diagram showing a conventional exhaust gas reburn combined cycle plant.
【図５】従来の油ガス化複合サイクルプラントを示す機
器系統図。FIG. 5 is an equipment system diagram showing a conventional oil gasification combined cycle plant.
１ 排気再燃ボイラ ２ 蒸気タービン ３ ガスタービン ４ 気化器（分溜器） ５ 原油輸送ライン ６ 重質油供給ライン ７ 軽質油供給ライン ８ ガスタービン排気ガス供給ライン ９ 燃焼用空気 １０ 蒸気供給ライン １１ 風箱・バーナ １２ 凝縮器 １３ 軽質油加圧ポンプ １４ スタック １５ 重質油加圧ポンプ １６ タービン抽気 1 Exhaust Reburning Boiler 2 Steam Turbine 3 Gas Turbine 4 Vaporizer (Distiller) 5 Crude Oil Transport Line 6 Heavy Oil Supply Line 7 Light Oil Supply Line 8 Gas Turbine Exhaust Gas Supply Line 9 Combustion Air 10 Steam Supply Line 11 Wind Box / burner 12 Condenser 13 Light oil pressurizing pump 14 Stack 15 Heavy oil pressurizing pump 16 Turbine extraction
Claims (2)
スによる排気再燃ボイラ、及び同排気再燃ボイラから蒸
気の供給を受ける蒸気タービンを有し原油を燃料とした
排気再燃複合サイクルプラントにおいて、前記原油を軽
質油分と重質油に分離するための気化器を有し前記軽質
油分は前記ガスタービンの、前記重質油は前記排気再燃
ボイラの燃料とすることを特徴とする排気再燃複合サイ
クルプラント。1. An exhaust gas re-combustion combined cycle plant having a gas turbine, an exhaust gas re-combustion boiler using the exhaust gas of the gas turbine, and a steam turbine supplied with steam from the exhaust gas re-combustion boiler, wherein the crude oil is used as a fuel. An exhaust gas re-combustion combined cycle plant, comprising a vaporizer for separating a light oil component and a heavy oil, wherein the light oil component is used as a fuel for the gas turbine, and the heavy oil is used as a fuel for the exhaust gas reburning boiler.
する重質油貯蔵タンク、及び前記気化器で分離して得ら
れた軽質油を貯蔵する軽質油貯蔵タンクを有することを
特徴とする請求項１記載の排気再燃複合サイクルプラン
ト。2. A heavy oil storage tank communicating with the vaporizer for storing the heavy oil, and a light oil storage tank for storing the light oil obtained by separation in the vaporizer. The exhaust gas re-combustion combined cycle plant according to claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6001997A JP2966713B2 (en) | 1994-01-13 | 1994-01-13 | Exhaust reburn combined cycle plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6001997A JP2966713B2 (en) | 1994-01-13 | 1994-01-13 | Exhaust reburn combined cycle plant |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH07208111A true JPH07208111A (en) | 1995-08-08 |
| JP2966713B2 JP2966713B2 (en) | 1999-10-25 |
Family
ID=11517095
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6001997A Expired - Fee Related JP2966713B2 (en) | 1994-01-13 | 1994-01-13 | Exhaust reburn combined cycle plant |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2966713B2 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6223522B1 (en) * | 1999-03-25 | 2001-05-01 | Mitsubishi Heavy Industries, Ltd. | Combined cycle power plant and method using both light and heavy oils |
| US6298651B1 (en) | 1996-12-26 | 2001-10-09 | Mitsubishi Heavy Industries, Ltd. | Power generation method and power generating apparatus |
| JP2012092852A (en) * | 2012-02-16 | 2012-05-17 | Mitsubishi Heavy Ind Ltd | Gas turbine power generation system |
| CN116624268A (en) * | 2023-05-04 | 2023-08-22 | 北京航空航天大学 | A turbo-piston hybrid power system suitable for multi-fuel and its application method |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06272515A (en) * | 1993-03-17 | 1994-09-27 | Mitsubishi Heavy Ind Ltd | Power generating method |
-
1994
- 1994-01-13 JP JP6001997A patent/JP2966713B2/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06272515A (en) * | 1993-03-17 | 1994-09-27 | Mitsubishi Heavy Ind Ltd | Power generating method |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6298651B1 (en) | 1996-12-26 | 2001-10-09 | Mitsubishi Heavy Industries, Ltd. | Power generation method and power generating apparatus |
| EP0955455A4 (en) * | 1996-12-26 | 2002-07-17 | Mitsubishi Heavy Ind Ltd | ELECTRICITY PRODUCTION AND ASSOCIATED FACILITIES |
| US6223522B1 (en) * | 1999-03-25 | 2001-05-01 | Mitsubishi Heavy Industries, Ltd. | Combined cycle power plant and method using both light and heavy oils |
| EP1039097A3 (en) * | 1999-03-25 | 2002-08-21 | Mitsubishi Heavy Industries, Ltd. | Transport of high viscosity fuel to a power generation plant |
| JP2012092852A (en) * | 2012-02-16 | 2012-05-17 | Mitsubishi Heavy Ind Ltd | Gas turbine power generation system |
| CN116624268A (en) * | 2023-05-04 | 2023-08-22 | 北京航空航天大学 | A turbo-piston hybrid power system suitable for multi-fuel and its application method |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2966713B2 (en) | 1999-10-25 |
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