EP1010947A2 - A gas turbine with a catalytic combustor and method of operating such a gas turbine - Google Patents
A gas turbine with a catalytic combustor and method of operating such a gas turbine Download PDFInfo
- Publication number
- EP1010947A2 EP1010947A2 EP99124944A EP99124944A EP1010947A2 EP 1010947 A2 EP1010947 A2 EP 1010947A2 EP 99124944 A EP99124944 A EP 99124944A EP 99124944 A EP99124944 A EP 99124944A EP 1010947 A2 EP1010947 A2 EP 1010947A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- catalyst
- zone
- turbine
- section
- gas turbine
- 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.)
- Withdrawn
Links
- 230000003197 catalytic effect Effects 0.000 title claims abstract description 37
- 238000000034 method Methods 0.000 title claims abstract description 13
- 239000003054 catalyst Substances 0.000 claims abstract description 54
- 238000007084 catalytic combustion reaction Methods 0.000 claims abstract description 7
- 230000000977 initiatory effect Effects 0.000 claims abstract 2
- 238000002485 combustion reaction Methods 0.000 claims description 25
- 230000005611 electricity Effects 0.000 claims description 16
- 238000010438 heat treatment Methods 0.000 claims description 16
- 239000000203 mixture Substances 0.000 claims description 8
- 239000000446 fuel Substances 0.000 claims description 6
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 2
- 229910052763 palladium Inorganic materials 0.000 claims description 2
- 229910052697 platinum Inorganic materials 0.000 claims description 2
- 229910052703 rhodium Inorganic materials 0.000 claims description 2
- 239000010948 rhodium Substances 0.000 claims description 2
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 claims description 2
- 238000011144 upstream manufacturing Methods 0.000 claims 4
- 239000007789 gas Substances 0.000 abstract description 35
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 4
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 2
- 239000000919 ceramic Substances 0.000 description 3
- 239000011159 matrix material Substances 0.000 description 3
- 239000010970 precious metal Substances 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- 230000003213 activating effect Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 230000003028 elevating effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23R—GENERATING COMBUSTION PRODUCTS OF HIGH PRESSURE OR HIGH VELOCITY, e.g. GAS-TURBINE COMBUSTION CHAMBERS
- F23R3/00—Continuous combustion chambers using liquid or gaseous fuel
- F23R3/40—Continuous combustion chambers using liquid or gaseous fuel characterised by the use of catalytic means
Definitions
- This invention relates to a gas turbine and more particularly to a method of operating a gas turbine, which includes a catalytic combustor.
- An axial flow rotary machine such as an industrial gas turbine for a co-generation system or a gas turbine engine for an aircraft, includes a compressor section, a combustion section, and a turbine section. As the working medium gases travel along the flow path, the gases are compressed in the compressor section, thereby causing the temperature and pressure of the gases to rise. The hot, pressurized gases are burned with fuel in the combustion section to add energy to the gases, which expand through the turbine section and produce useful work and/or thrust.
- a conventional catalytic combustor typically includes a precombustion zone, a premixing zone, a catalyst zone and a combustion zone.
- the catalyst zone includes a catalytic reactor, which includes a catalyst.
- a typical precombustion zone includes a preburner, which increases the temperature of the working medium gases in order to initiate and maintain the catalytic reaction between such gases and the catalyst. In this case, however, the preburner is the leading producer of NO x , especially during start-up and low load operations when the preburner is required.
- An object of the present invention includes eliminating the pre-combustion zone of a catalytic combustor in a gas turbine, thereby reducing the pollutants created by a gas turbine during operation, especially during start-up and low load operation.
- the present invention includes a method for operating a gas turbine, which contains a catalytic combustor, wherein such method comprises heating a catalyst within the catalytic combustor to a predetermined temperature thereby activating catalytic combustion of a fuel-air mixture.
- Such method includes electrically heating the catalyst when the temperature of the catalyst falls below the predetermined temperature, namely upon starting the gas turbine and/or partial load conditions during operation. Electrically heating the catalyst reduces the intake air temperature required to initiate combustion, thereby reducing and/or eliminating the requirement of preheating the intake air. Eliminating the preburner, therefore, improves the simplicity and control of operating the gas turbine.
- a method of electrically heating the catalyst includes connecting a generator to the gas turbine, thereby generating electricity which is directed to a portion of the catalyst when the catalyst falls below the predetermined temperature. Re-directing electricity to the catalyst and back into the gas turbine provides efficient operation of the gas turbine.
- An additional or alternate embodiment of a method for electrically heating the catalyst includes providing a portion of the catalyst with electricity from an auxiliary power supply.
- the present invention further includes a gas turbine as specified in claim 6.
- a gas turbine as specified in claim 6.
- gas turbine consists essentially of the elements (a), (b), (c), and (d).
- the present invention also includes a catalytic combustor consisting essentially of a premixing zone, a catalyst zone having a catalyst therein, a combustion zone, and means for electrically heating a portion of the catalyst to a predetermined temperature.
- the catalyst zone is disposed between the premixing zone and the combustion zone. Inclusion of the means for heating a portion of the catalyst eliminates the requirement of a pre-combustion zone, thereby removing such zone and the cause of a significant portion of the pollutants created when operating a gas turbine.
- the electric power generating system 10 includes an industrial gas turbine 12 that drives a generator 14 .
- the generator 14 can be used to drive local electrical needs or connected to a power grid network.
- the industrial gas turbine 12 is not limited to driving an electrical generator 14 .
- the gas turbine can also be used to drive other types of loads.
- the industrial gas turbine 12 is axially located along axis (R x ) and includes a compressor section 16 , a combustion section 18 , a turbine section 20 and a shaft 22 .
- the combustion section 18 is a catalytic combustor, which includes a premixing zone 24 , a catalyst zone 26 , and a combustion zone 28 .
- Intake air enters the compressor section 16
- fuel enters the premixing zone 24 of the combustion section 18 through fuel supply lines 30 , 32 and mixes with the intake air, thereby creating a combustible fuel-air mixture.
- the fuel-air mixture enters the catalyst zone 26 where combustion of the mixture is initiated and continues to completion in the combustion section 28 , thereby adding energy to the working medium gas.
- the turbine section 20 includes a turbine, indicated by lines 42 , which rotates as the heated gas expands through this section.
- the turbine 42 is connected to one end of the shaft 22 , which transmits power to the compressor 54 and the generator 14 .
- the shaft 22 When the turbine 42 rotates, the shaft 22 also rotates, thereby enabling the generator 14 to produce electricity, which travels along lines 44 .
- the catalyst zone 26 includes a catalytic reactor 40 and a temperature sensor 36 .
- the catalytic reactor 40 contains a ceramic or metal honeycomb catalyst matrix, which may be wash-coated with alumina, stabilized alumina or a similar catalyst substrate.
- the wash-coated catalyst substrate is impregnated with an active catalyst material, such as one or more of the precious metals or a combination of precious metals that are capable of withstanding the combustion temperature of the catalytic reactor.
- an active catalyst material such as one or more of the precious metals or a combination of precious metals that are capable of withstanding the combustion temperature of the catalytic reactor.
- Certain types of precious metals that are catalytically active and capable of withstanding elevated temperatures include platinum, palladium, and rhodium.
- the temperature sensor 36 Upon sensing that the temperature of the catalytic reactor 40 is less than a predetermined temperature, the temperature sensor 36 delivers a signal along line 52 to the controller 38 .
- the controller 38 delivers electric current via lines 50 to the catalytic reactor 40 , thereby elevating the temperature of at least a portion of the catalytic reactor 40 to the predetermined temperature. It is preferable to elevate the temperature of the portion of the catalytic reactor 40 nearest the premixing zone 24 , which is referred to as the inlet portion, in order to initiate catalytic combustion as early as possible within the catalytic reactor 40 .
- the predetermined temperature is dependent upon the type of catalyst, the type of fuel and the fuel-air composition.
- the predetermined temperature is a temperature at or above the catalyst light-off temperature, wherein the catalyst light-off temperature is a temperature sufficient to initiate and maintain catalytic combustion. Maintaining at least a portion of the catalytic reactor 40 at the predetermined temperature ensures that the fuel-air mixture will combust within the combustion zone 18 . The heat generated by the combustion, in turn, increases the temperature of the catalytic reactor 40 , thereby sustaining catalytic combustion.
- the temperature sensor 36 senses the temperature of the catalytic reactor 40 and sends a signal to controller 38 along line 52 . Upon sensing that the catalytic reactor 40 has attained the predetermined temperature, the controller discontinues or reduces (i.e., modulates) the amount of electricity delivered to the catalytic reactor 40 as necessary to maintain the catalyst temperature at or above the predetermined temperature. If the catalyst matrix of the catalytic reactor 40 is constructed of ceramic, then the electric current will have to be applied to an electrically conducting material within or on the ceramic. If the catalyst matrix is constructed of metal, then the electric current will be applied directly to the support structure.
- the controller 38 is capable of receiving electricity from both the generator 14 , along lines 44 and 46 , and an auxiliary power supply 34 (e.g., auxiliary generator) along lines 48 .
- auxiliary power supply 34 e.g., auxiliary generator
- the controller 38 furnishes the catalytic reactor 40 with the necessary power to maintain the catalytic reactor 40 at the predetermined temperature until the generator 14 independently produces a sufficient amount of electricity to maintain the temperature of the catalytic reactor 40 above the predetermined temperature. Re-directing the electricity generated by the generator 14 to the catalytic reactor 40 provides for an efficient co-generation system 10 .
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
Abstract
Description
- This invention relates to a gas turbine and more particularly to a method of operating a gas turbine, which includes a catalytic combustor.
- An axial flow rotary machine, such as an industrial gas turbine for a co-generation system or a gas turbine engine for an aircraft, includes a compressor section, a combustion section, and a turbine section. As the working medium gases travel along the flow path, the gases are compressed in the compressor section, thereby causing the temperature and pressure of the gases to rise. The hot, pressurized gases are burned with fuel in the combustion section to add energy to the gases, which expand through the turbine section and produce useful work and/or thrust.
- The burning of fuel, however, causes the gas turbine to emit undesirable oxides of nitrogen (NOx). Regulations limiting the amount of NOx emissions produced by gas turbines has motivated the development of certain technologies such as diluent injection in the combustion section, lean premixed Dry Low NOx (DLN) combustion and catalytic combustion. A conventional catalytic combustor typically includes a precombustion zone, a premixing zone, a catalyst zone and a combustion zone. The catalyst zone includes a catalytic reactor, which includes a catalyst. A typical precombustion zone includes a preburner, which increases the temperature of the working medium gases in order to initiate and maintain the catalytic reaction between such gases and the catalyst. In this case, however, the preburner is the leading producer of NOx, especially during start-up and low load operations when the preburner is required.
- An object of the present invention includes eliminating the pre-combustion zone of a catalytic combustor in a gas turbine, thereby reducing the pollutants created by a gas turbine during operation, especially during start-up and low load operation.
- Accordingly the present invention includes a method for operating a gas turbine, which contains a catalytic combustor, wherein such method comprises heating a catalyst within the catalytic combustor to a predetermined temperature thereby activating catalytic combustion of a fuel-air mixture. Such method includes electrically heating the catalyst when the temperature of the catalyst falls below the predetermined temperature, namely upon starting the gas turbine and/or partial load conditions during operation. Electrically heating the catalyst reduces the intake air temperature required to initiate combustion, thereby reducing and/or eliminating the requirement of preheating the intake air. Eliminating the preburner, therefore, improves the simplicity and control of operating the gas turbine. A method of electrically heating the catalyst includes connecting a generator to the gas turbine, thereby generating electricity which is directed to a portion of the catalyst when the catalyst falls below the predetermined temperature. Re-directing electricity to the catalyst and back into the gas turbine provides efficient operation of the gas turbine.
- An additional or alternate embodiment of a method for electrically heating the catalyst includes providing a portion of the catalyst with electricity from an auxiliary power supply.
- The present invention further includes a gas turbine as specified in claim 6. Preferably, such gas turbine consists essentially of the elements (a), (b), (c), and (d).
- The present invention also includes a catalytic combustor consisting essentially of a premixing zone, a catalyst zone having a catalyst therein, a combustion zone, and means for electrically heating a portion of the catalyst to a predetermined temperature. The catalyst zone is disposed between the premixing zone and the combustion zone. Inclusion of the means for heating a portion of the catalyst eliminates the requirement of a pre-combustion zone, thereby removing such zone and the cause of a significant portion of the pollutants created when operating a gas turbine.
- The foregoing and other objects, features and advantages of the present invention will become more apparent in light of the following detailed description of exemplary embodiments thereof as illustrated in the accompanying drawings.
-
- Fig. 1 is an illustration of an electric power generating system which includes an industrial gas turbine engine and generator.
- Fig. 2 is a schematic diagram of a gas turbine of the present invention equipped with an electrically heated catalytic combustor.
-
- Although the present invention is described in relation to an industrial gas turbine, the present invention can also apply to any gas turbine engine application.
- Referring to Fig. 1, the electric
power generating system 10 includes anindustrial gas turbine 12 that drives agenerator 14. Thegenerator 14 can be used to drive local electrical needs or connected to a power grid network. Theindustrial gas turbine 12, however, is not limited to driving anelectrical generator 14. The gas turbine can also be used to drive other types of loads. - Referring to Fig. 2, the
industrial gas turbine 12 is axially located along axis (Rx) and includes acompressor section 16, acombustion section 18, aturbine section 20 and ashaft 22. Thecombustion section 18 is a catalytic combustor, which includes apremixing zone 24, acatalyst zone 26, and acombustion zone 28. Intake air enters thecompressor section 16, and fuel enters thepremixing zone 24 of thecombustion section 18 through 30, 32 and mixes with the intake air, thereby creating a combustible fuel-air mixture. The fuel-air mixture enters thefuel supply lines catalyst zone 26 where combustion of the mixture is initiated and continues to completion in thecombustion section 28, thereby adding energy to the working medium gas. Theturbine section 20 includes a turbine, indicated bylines 42, which rotates as the heated gas expands through this section. Theturbine 42 is connected to one end of theshaft 22, which transmits power to thecompressor 54 and thegenerator 14. When theturbine 42 rotates, theshaft 22 also rotates, thereby enabling thegenerator 14 to produce electricity, which travels alonglines 44. - The
catalyst zone 26 includes acatalytic reactor 40 and atemperature sensor 36. Thecatalytic reactor 40 contains a ceramic or metal honeycomb catalyst matrix, which may be wash-coated with alumina, stabilized alumina or a similar catalyst substrate. The wash-coated catalyst substrate is impregnated with an active catalyst material, such as one or more of the precious metals or a combination of precious metals that are capable of withstanding the combustion temperature of the catalytic reactor. Certain types of precious metals that are catalytically active and capable of withstanding elevated temperatures include platinum, palladium, and rhodium. - Upon sensing that the temperature of the
catalytic reactor 40 is less than a predetermined temperature, thetemperature sensor 36 delivers a signal alongline 52 to thecontroller 38. Thecontroller 38, in turn, delivers electric current vialines 50 to thecatalytic reactor 40, thereby elevating the temperature of at least a portion of thecatalytic reactor 40 to the predetermined temperature. It is preferable to elevate the temperature of the portion of thecatalytic reactor 40 nearest thepremixing zone 24, which is referred to as the inlet portion, in order to initiate catalytic combustion as early as possible within thecatalytic reactor 40. The predetermined temperature is dependent upon the type of catalyst, the type of fuel and the fuel-air composition. The predetermined temperature, however, is a temperature at or above the catalyst light-off temperature, wherein the catalyst light-off temperature is a temperature sufficient to initiate and maintain catalytic combustion. Maintaining at least a portion of thecatalytic reactor 40 at the predetermined temperature ensures that the fuel-air mixture will combust within thecombustion zone 18. The heat generated by the combustion, in turn, increases the temperature of thecatalytic reactor 40, thereby sustaining catalytic combustion. - The
temperature sensor 36 senses the temperature of thecatalytic reactor 40 and sends a signal to controller 38 alongline 52. Upon sensing that thecatalytic reactor 40 has attained the predetermined temperature, the controller discontinues or reduces (i.e., modulates) the amount of electricity delivered to thecatalytic reactor 40 as necessary to maintain the catalyst temperature at or above the predetermined temperature. If the catalyst matrix of thecatalytic reactor 40 is constructed of ceramic, then the electric current will have to be applied to an electrically conducting material within or on the ceramic. If the catalyst matrix is constructed of metal, then the electric current will be applied directly to the support structure. - The
controller 38 is capable of receiving electricity from both thegenerator 14, along 44 and 46, and an auxiliary power supply 34 (e.g., auxiliary generator) alonglines lines 48. At start-up and at low load conditions, thegenerator 14 may not produce a sufficient amount of electricity to heat thecatalytic reactor 40 to the predetermined temperature due to the lack of rotational shaft speed. Theauxiliary power supply 34, therefore, provides thecontroller 38, alonglines 48 with additional electricity during such operating conditions. Thecontroller 38, in turn, furnishes thecatalytic reactor 40 with the necessary power to maintain thecatalytic reactor 40 at the predetermined temperature until thegenerator 14 independently produces a sufficient amount of electricity to maintain the temperature of thecatalytic reactor 40 above the predetermined temperature. Re-directing the electricity generated by thegenerator 14 to thecatalytic reactor 40 provides for anefficient co-generation system 10.
Claims (9)
- A method for operating a gas turbine, the gas turbine extending axially and having an upstream end and a downstream end, a compressor section, a catalytic combustor section and a turbine section, the compressor section being relatively toward the upstream end, the turbine section being relatively toward the downstream end, the catalytic combustor section disposed between the compressor section and the turbine section, the catalytic combustor section having a premixing zone, a catalyst zone and a combustion zone, the premixing zone being relatively toward the compressor section, the combustion zone being relatively toward the turbine section, the catalyst zone disposed between the premixing zone and the combustion zone and having a catalyst therein, comprising the steps of:(a) introducing intake air into the compressor section;(b) allowing the intake air to enter the mixing zone of the catalytic combustor section;(c) introducing fuel into the mixing zone and creating a fuel-air mixture which enters the catalyst zone; and(d) heating at least a portion of the catalyst to a predetermined temperature, thereby initiating catalytic combustion of the fuel-air mixture.
- The method of claim 1 further comprising the step of heating the portion of the catalyst to said predetermined temperature when the temperature of the catalyst falls below the predetermined temperature.
- The method of claim 1 or 2, wherein the step of heating the portion of the catalyst comprises electrically heating the portion.
- The method of claim 3 wherein the step of electrically heating a portion of the catalyst comprises the steps of connecting a turbine, within the turbine section, to a shaft; rotating the turbine and the shaft; generating electricity from the rotating shaft; and directing at least a portion of the generated electricity to the portion of the catalyst.
- The method of claim 3 or 4 wherein the step of electrically heating a portion of the catalyst comprises applying electricity to the portion from an auxiliary power supply.
- A gas turbine extending axially and having an upstream end and a downstream end, comprising:(a) a compressor section being relatively toward the upstream end;(b) a turbine section being relatively toward the downstream end;(c) a catalytic combustor section disposed between said compressor section and said turbine section, said catalytic combustor section consisting essentially of a premixing zone, a catalyst zone and a combustion zone, said premixing zone being relatively toward said compressor section, said combustion zone being relatively toward said turbine section, said catalyst zone disposed between said premixing zone and said combustion zone, said catalyst zone comprising a catalyst therein; and(d) means for heating at least a portion of said catalyst to a predetermined temperature.
- The gas turbine of claim 6 wherein said means for heating comprises:(a) a turbine within said turbine section;(b) a shaft connected to said turbine;(c) a generator connected to said shaft, said generator generating electricity when said turbine rotates; and(d) a controller which directs electricity from said generator to said portion of said catalyst when the temperature of said catalyst is less than said predetermined temperature.
- The gas turbine of claim 6 or 7 wherein said means for heating comprises an auxiliary electrical power supply and a controller which directs electricity from said auxiliary electrical power supply to said portion of said catalyst when the temperature of said catalyst is less than said predetermined temperature.
- The gas turbine of any of claims 6 to 8 wherein said catalyst is a material from the group consisting essentially of platinum, palladium and rhodium.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US21114798A | 1998-12-14 | 1998-12-14 | |
| US211147 | 1998-12-14 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP1010947A2 true EP1010947A2 (en) | 2000-06-21 |
| EP1010947A3 EP1010947A3 (en) | 2002-03-20 |
Family
ID=22785751
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP99124944A Withdrawn EP1010947A3 (en) | 1998-12-14 | 1999-12-14 | A gas turbine with a catalytic combustor and method of operating such a gas turbine |
Country Status (1)
| Country | Link |
|---|---|
| EP (1) | EP1010947A3 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE10062253A1 (en) * | 2000-12-14 | 2002-06-20 | Rolls Royce Deutschland | Gas turbine for aircraft has mesh of heat-resistant material, e.g. ceramic, in its combustion chamber |
| WO2004029433A1 (en) * | 2002-09-27 | 2004-04-08 | Commonwealth Scientific And Industrial Research Organisation | A system for catalytic combustion |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4081958A (en) * | 1973-11-01 | 1978-04-04 | The Garrett Corporation | Low nitric oxide emission combustion system for gas turbines |
| MX3874E (en) * | 1975-12-29 | 1981-08-26 | Engelhard Min & Chem | IMPROVEMENTS IN METHOD TO INITIATE A COMBUSTION SYSTEM USING A CATALYST |
| JPS59180220A (en) * | 1983-03-31 | 1984-10-13 | Toshiba Corp | Gas turbine combustor |
| US5440872A (en) * | 1988-11-18 | 1995-08-15 | Pfefferle; William C. | Catalytic method |
| GB2268694A (en) * | 1992-07-14 | 1994-01-19 | Rolls Royce Plc | A catalytic combustion chamber |
| EP0702135B1 (en) * | 1994-04-14 | 1999-12-01 | Precision Combustion, Inc. | A fuel injector and igniter assembly |
| US6109018A (en) * | 1996-07-26 | 2000-08-29 | Catalytica, Inc. | Electrically-heated combustion catalyst structure and method for start-up of a gas turbine using same |
| DE19654022A1 (en) * | 1996-12-21 | 1998-06-25 | Abb Research Ltd | Process for operating a gas turbine group |
-
1999
- 1999-12-14 EP EP99124944A patent/EP1010947A3/en not_active Withdrawn
Non-Patent Citations (1)
| Title |
|---|
| None |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE10062253A1 (en) * | 2000-12-14 | 2002-06-20 | Rolls Royce Deutschland | Gas turbine for aircraft has mesh of heat-resistant material, e.g. ceramic, in its combustion chamber |
| WO2004029433A1 (en) * | 2002-09-27 | 2004-04-08 | Commonwealth Scientific And Industrial Research Organisation | A system for catalytic combustion |
| US7430869B2 (en) | 2002-09-27 | 2008-10-07 | Commonwealth Scientific And Industrial Research Organisation | System for catalytic combustion |
| EP1549842A4 (en) * | 2002-09-27 | 2009-05-13 | Commw Scient Ind Res Org | SYSTEM FOR CATALYTIC COMBUSTION |
| CN101798960B (en) * | 2002-09-27 | 2011-11-30 | 联邦科学和工业研究组织 | A system for catalytic combustion |
Also Published As
| Publication number | Publication date |
|---|---|
| EP1010947A3 (en) | 2002-03-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4825658A (en) | Fuel nozzle with catalytic glow plug | |
| JP2591866B2 (en) | Gas turbine catalytic combustor with preburner with reduced NOx generation | |
| KR100483774B1 (en) | PREMIXING DRY LOW NOx EMISSIONS COMBUSTOR WITH LEAN DIRECT INJECTION OF GAS FUEL | |
| US4112675A (en) | Apparatus and method for starting a large gas turbine having a catalytic combustor | |
| EP0809076A2 (en) | Gas turbine with catalytic combustion system | |
| CN1864032A (en) | Heat exchange gas turbine engine system and method employing catalytic combustion | |
| EP1040254A1 (en) | A LOW NOx CONDITIONER SYSTEM AND PROCESS FOR A MICROTURBINE POWER GENERATING SYSTEM | |
| JP2000514911A (en) | Catalytic combustion chamber and method for ignition and control of the catalytic combustion chamber | |
| JPH09287740A (en) | Combustor for gas turbine and usage | |
| US6588213B2 (en) | Cross flow cooled catalytic reactor for a gas turbine | |
| RU2142566C1 (en) | Gas turbine for burning combustible gas | |
| JPS63254304A (en) | How to burn fuel | |
| US6148617A (en) | Natural gas fired combustion system for gas turbine engines | |
| AU2012354936A1 (en) | Gas turbine engine provided with heat exchanger, and method for starting same | |
| EP1010947A2 (en) | A gas turbine with a catalytic combustor and method of operating such a gas turbine | |
| JPH11507433A (en) | Burners especially for gas turbines | |
| JP3706455B2 (en) | Hydrogen / oxygen combustor for hydrogen combustion turbine | |
| EP0062149B1 (en) | Catalytic combustor having secondary fuel injection for a stationary gas turbine | |
| JP2808404B2 (en) | Starting method of catalytic combustor for gas turbine engine | |
| Dalla Betta et al. | Application of catalytic combustion technology to industrial gas turbines for ultra-low NOx emissions | |
| JP2745352B2 (en) | Gas turbine engine | |
| JP3583736B2 (en) | Gas turbine combustor | |
| JP3521013B2 (en) | Catalytic combustion boiler | |
| JPH05346207A (en) | Catalytic combustor | |
| JPH06257465A (en) | Gas turbine power generator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
| AK | Designated contracting states |
Kind code of ref document: A2 Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE Kind code of ref document: A2 Designated state(s): CH DE FR GB IT LI |
|
| AX | Request for extension of the european patent |
Free format text: AL;LT;LV;MK;RO;SI |
|
| 17P | Request for examination filed |
Effective date: 20001222 |
|
| PUAL | Search report despatched |
Free format text: ORIGINAL CODE: 0009013 |
|
| AK | Designated contracting states |
Kind code of ref document: A3 Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE |
|
| AX | Request for extension of the european patent |
Free format text: AL;LT;LV;MK;RO;SI |
|
| RIC1 | Information provided on ipc code assigned before grant |
Free format text: 7F 23R 3/40 A, 7F 02C 3/04 B, 7F 02C 3/00 B |
|
| AKX | Designation fees paid |
Free format text: CH DE FR GB IT LI |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN |
|
| 18D | Application deemed to be withdrawn |
Effective date: 20030701 |