US3914091A - Combustion method for hydrocarbonic fuels with low emission of nitrogen oxides - Google Patents

Combustion method for hydrocarbonic fuels with low emission of nitrogen oxides Download PDF

Info

Publication number
US3914091A
US3914091A US447035A US44703574A US3914091A US 3914091 A US3914091 A US 3914091A US 447035 A US447035 A US 447035A US 44703574 A US44703574 A US 44703574A US 3914091 A US3914091 A US 3914091A
Authority
US
United States
Prior art keywords
combustion
fuel
hydrocarbonic
air
inorganic gases
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.)
Expired - Lifetime
Application number
US447035A
Inventor
Kazuo Yamagishi
Masaaki Nozawa
Tsunenori Tokumoto
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.)
Tokyo Gas Co Ltd
Original Assignee
Tokyo Gas Co 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 Tokyo Gas Co Ltd filed Critical Tokyo Gas Co Ltd
Application granted granted Critical
Publication of US3914091A publication Critical patent/US3914091A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C13/00Apparatus in which combustion takes place in the presence of catalytic material
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C6/00Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion
    • F23C6/04Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23RGENERATING COMBUSTION PRODUCTS OF HIGH PRESSURE OR HIGH VELOCITY, e.g. GAS-TURBINE COMBUSTION CHAMBERS
    • F23R3/00Continuous combustion chambers using liquid or gaseous fuel
    • F23R3/40Continuous combustion chambers using liquid or gaseous fuel characterised by the use of catalytic means

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion Of Fluid Fuel (AREA)

Abstract

A combustion method for hydrocarbonic fuels with low emission of nitrogen oxides comprising a step of primary combustion where a hydrocarbonic fuel mixed with air in an amount less than 70 percent of the theoretically required amount for completion of combustion of the fuel is subjected to a primary combustion and then allowed to pass through a process of accelerating the partial combustion to decompose into simple inorganic gases consisting mainly of H2 and CO as combustible components, and a step of secondary combustion where the simple inorganic gases are led to a secondary combustion chamber independent from the foregoing steps to have the combustion completed with feed of air for combustion. A combustion method for hydrocarbonic fuels with low emission of nitrogen oxides comprising a step of primary combustion where a hydrocarbonic fuel mixed with air in an amount less than 70 percent of the theoretically required amount for completion of combustion of the fuel is subjected to a primary combustion and then allowed to pass through a process of accelerating the partial combustion to decompose into simple inorganic gases consisting mainly of H2 and CO as combustible components, and a step of final combustion where the simple inorganic gases are led across heat absorbing processes to a combustion chamber independent from the foregoing steps for completion of the combustion with feed of air for combustion.

Description

United States Patent 1 Yamagishi et a1.
[ COMBUSTION METHOD FOR HYDROCARBONIC FUELS WITH LOW EMISSION OF NITROGEN OXIDES [75] Inventors: Kazuo Yamagishi, Urawa; Masaaki Nozawa, Yokohama; Tsunenori Tokumoto, Yokosuka, all of Japan [73] Assignee: Tokyo Gas Company Limited,
Tokyo, Japan 221 Filed: Feb. 23, 1974 [21] Appl. No.: 447,035
Primary Examiner-Edward G. Favors Attorney, Agent, or FirmWenderoth, Lind 8!. Ponack [57] ABSTRACT A combustion method for hydrocarbonic fuels with 1 Oct. 21, 1975 low emission of nitrogen oxides comprising a step of primary combustion where a hydrocarbonic fuel mixed with air in an amount less than 70 percent of the theoretically required amount for completion of combustion of the fuel is subjected to a primary combustion and then allowed to pass through a process of accelerating the partial combustion to decompose into simple inorganic gases consisting mainly of H, and CO as combustible components, and a step of secondary combustion where the simple inorganic gases are led to a secondary combustion chamber independent from the foregoing steps to have the combustion completed with feed of air for combustion.
A combustion method for hydrocarbonic fuels with low emission of nitrogen oxides comprising a step of primary combustion where a hydrocarbonic fuel mixed with air in an amount less than 70 percent of the theoretically required amount for completion of combustion of the fuel is subjected to a primary combustion and then allowed to pass through a process of accelerating the partial combustion to decompose into simple inorganic gases consisting mainly of 1-1 and CO as combustible components, and a step of final combustion where the simple inorganic gases are led across heat absorbing processes to a combustion chamber independent from the foregoing steps for completion of the combustion with feed of air for combustion.
2 Claims, 1 Drawing Figure Heat. absorbing process COMBUSTION METHOD FOR I-IYDROCARBONIC FUELS WI'I'I'I LOW EMISSION OF NITROGEN OXIDES DESCRIPTION OF THE INVENTION This invention is concerned with a method of combustion of hydrocarbonic fuels with low emission of nitrogen oxides. It is known theoretically as well as experimentally that nitrogen oxides (N are less produced in combustion at an air ratio less than the theoretical requirement. Further, in the secondary combustion and thereafter, the combustion temperature generally tends to decline so that the amount of nitrogen oxides to be produced tends to decrease. But, when the conventional staged combustion method is used in which diffusion flames are preferred, the following difficulties are involved, viz. (1) although the primary combustion may be of combustion under the air ratio below the theoretical requirement as a whole, there may be locally created an oxygen rich region where NO are likely to be produced; (2) the partial combustion may not be completed in the primary combustion resulting to the production of the hydrocarbonic gas components which tend to produce soot, leading to troubles of soot formation in the heat absorbing processes after the primary combustion or in the stage of secondary combustion; and (3) the stage of secondary combustion has a large amount of hydrocarbon left so that there is much formation of the so-called prompt NO probably due to the C-l-I radicals. With such difficulties, there is a limit in the final reduction of N0 and the reduction rate is 50 to 60 percent at best.
The combustion method of the present invention eliminates the difficulties of the conventional staged combustion method entirely. According to the combustion method of the invention, a hydrocarbonic fuel is mixed with air in an amount less than 70 percent of the theoretically required amount, and is subjected to a primary combustion and then allowed to pass through a process of accelerating the partial combustion to decompose into simple inorganic gases consisting mainly of H, and CO as combustible components, then the simple inorganic gases are led to an independent secondary combustion chamber from the foregoing stages for completion of the combustion with feed of air for combustion. Any hydrocarbonic fuels are applicable, and as a partial combustion accelerating process, a combustion chamber having a sufficient geometric volume or some catalytic layer kept at an appropriate temperature may be used. As a catalyst, any of the nickel catalysts usually used as a catalyst for partial combustion of hydrocarbons can be used.
Now the low NO, emission characteristics of a staged combustion method having such a partial combustion accelerating process incorporated will be described. In the primary combustion, a fuel is burned at a ratio of air sufficiently lower than 70 percent of the theoretical requirement. For such combustion, a premix flame is preferable in that it produces only a small amount of NO in the primary combustion, but from the aspect of stability of combustion, the diffusion flame is advantageous. However, when the diffusion flame is used, the amount of NO, produced in the primary combustion tends to increase, as mentioned in the foregoing. In this stage, the partial combustion is not complete, and a large amount of undecomposed hydrocarbon or Cl-l compounds are present. The gas is then led to a promising partial combustion accelerating process which consists of some catalytic layer or a combustion chamber having sufficient geometric volume and the following reactions proceed:
and the gas is decomposed into simple inorganic gases comprising mainly CO and H, as combustible components. It must be noted here that the NO produced in the primary combustion are reduced in the partial combustion accelerating process by H, and CO produced by the partial combustion. Thus, there is obtained a high temperature partial combustion gas containing mainly C0 and H as combustible components with little NO This gas is then subjected to a secondary combustion together with air for secondary combustion. But, in order to reduce the generation of NO, in the secondary combustion to a low level, it is preferable to pass the gas through a heat absorbing process as is generally practiced in the conventional stage combustion. In this case, the gas contains no unstable intermediate products of combustion as a substance producing soot but consists mainly of relatively stable CO and H, so that formation of soot can be suppressed to a minimum. Since the combustible gases in the secondary combustion are for the most part H and CO, a low temperature combustion enabling to suppress the generation of NO to a sufficiently low level is practicable, and if required, an oxidation catalyst for low temperature combustion can be used. Where the cooling process after the partial combustion has to be omitted from the restriction in the configuration of combustion equipment and thus the partial combustion gas of high temperature is immediately brought to the secondary combustion, the unburned portion according to the present method consists of H and CO so that the final emission of NO can be reduced to a far lower level than that in the conventional combustion of hydrocarbons.
As an example, experimental data are shown in the following. With the primary and secondary air ratios taken as percent and 50 percent of the theoretical amount respectively (viz. percent in total) and a Ni catalyst is used as the partial combustion accelerating process, the combustion is carried out at a temperature of about l,l00C. The values of measurement of NO, are l to 2 ppm at the exit of the catalytic layer and less than 10 ppm at the point of termination of the secondary combustion, indicating that the NO, content is suppressed to a low level not attainable by the conventional staged combustion method. In the foregoing example, a Ni catalyst is used for the process of accelerating the partial combustion, but the method of the invention is not limited thereto. In the combustion method of the present invention, anything can be used for such purpose if it will decompose the unburned hydrocarbon component in the primary combustion gas burned in air less than 70 percent of that theoretically required to simple inorganic gases comprising CO and H, and preferably to accelerate the reduction of NO by hydrogen or CO. For example, the acceleration of partial combustion may be accomplished not by a catalyst but by a combustion chamber having a sufficiently large geometric volume as described in the foregoing. As an example, there are obtained, under the conditions of combustion of the primary and secondary air ratios at 55 percent and 65 percent respectively (viz. I20 percent in total), SV at 1,000 hrs and temperature at l,050C., the values of measurement are l to 2 ppm at the exit of the primary combustion chamber and ppm at the point of termination of the secondary combustion chamber. Now referring to the secondary combustion chamber, the combustion method of the present invention has the secondary combustion and subsequent processes isolated from the processes of the prior stages. Thus, the method of the invention has an advantage in that for various configurations of the secondary combustion chamber, any advantageous pattern of secondary combustion for NO, combustion can be determined freely without any adverse effect upon the processes of the prior stages. Further, in the combustion method of the invention having the partial combustion accelerating process incorporated, the secondary combustion is mainly of H and CO which are readily combustible gases so that the combustion is completed with ease and that it is possible to reduce the emission of CO to a minimum even under a low excess air ratio. As described in the foregoing, the combustion method of the present invention is a unique method which reduces the emission of hazardous substances such as NO, and CO and that of unburned gases to a minimum.
DRAWING The drawing represents a block diagram of the method of the present invention wherein numeral 1 indicates a fuel system and numeral 2 indicates an air systern.
1. A combustion method for hydrocarbonic fuel which results in low emission of nitrogen oxides comprising a primary combustion step of mixing a hydrocarbonic fuel with air in the amount of less than per cent of the theoretically required amount for complete combustion of the fuel and then accelerating the partial combustion in the presence of a nickel catalyst to decompose the fuel into simple inorganic gases consisting mainly of H and CO as combustible components, and a secondary combustion step of transferring the simply inorganic gases to a secondary combustion chamber for completing combustion, further air being provided in said secondary combustion chamber.
2. A combustion method for hydrocarbonic fuel which results in low emission of nitrogen oxides comprising a primary combustion step of mixing a hydrocarbonic fuel with air in the amount of less than 70 per cent of the theoretically required amount for complete combustion of the fuel and then accelerating the partial combustion in the presence of a nickel catalyst to decompose the fuel into simple inorganic gases consisting mainly of H, and CO as combustible components, and a secondary combustion step of transferring the simple inorganic gases through a heat absorbing means and thence to a combustion chamber for completing combustion, further air being provided in said combustion chamber.
I! it

Claims (2)

1. A COMBUSTION METHOD FOR HYDROCARBONIC FUEL WHICH RESULTS IN LOW EMISSION OF NITROGEN OXIDE COMPRISING A PRIMARY COMBUSTION STEP OF MIXING A HYDROCARBONIC FUEL WITH AIR IN THE AMOUNT OF LESS THAN 70 PER CENT OF THE THEORETICALLY REQUIRED AMOUNT FOR COMPLETE COMBUSTION OF THE FUEL AND THEN ACCELERATING THE PARTIAL COMBUSTION IN THE PRESENCE OF A NICKEL CATALYST TO DECOMPOSE THE FUEL INTO SIMPLE INORGANIC GASES CONSISTING MAINLY OF H2 AND CO AS COMBUSTIBLE COMPONENTS. AND A SECONDARY COMBUSTION STEP OF TRANSFERRING THE SIMPLY INORGANIC GASES TO A SECONDARY COMBUSTION CHAMBER FOR COMPLETING COMBUSTION FURTHER AIR BEING PROVIDED IN SAID SECONDARY COMBUSTION CHAMBER.
2. A combustion method for hydrocarbonic fuel which results in low emission of nitrogen oxides comprising a primary combustion step of mixing a hydrocarbonic fuel with air in the amount of less than 70 per cent of the theoretically required amount for complete combustion of the fuel and then accelerating the partial combustion in the presence of a nickel catalyst to decompose the fuel into simple inorganic gases consisting mainly of H2 and CO as combustible components, and a secondary combustion step of transferring thE simple inorganic gases through a heat absorbing means and thence to a combustion chamber for completing combustion, further air being provided in said combustion chamber.
US447035A 1973-03-01 1974-02-28 Combustion method for hydrocarbonic fuels with low emission of nitrogen oxides Expired - Lifetime US3914091A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP48024697A JPS5237611B2 (en) 1973-03-01 1973-03-01

Publications (1)

Publication Number Publication Date
US3914091A true US3914091A (en) 1975-10-21

Family

ID=12145352

Family Applications (1)

Application Number Title Priority Date Filing Date
US447035A Expired - Lifetime US3914091A (en) 1973-03-01 1974-02-28 Combustion method for hydrocarbonic fuels with low emission of nitrogen oxides

Country Status (4)

Country Link
US (1) US3914091A (en)
JP (1) JPS5237611B2 (en)
DE (1) DE2409950B2 (en)
FR (1) FR2220043B1 (en)

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2337305A1 (en) * 1975-12-29 1977-07-29 Engelhard Min & Chem PROCESS FOR BURNING FUELS CONTAINING NITROGEN
US4047877A (en) * 1976-07-26 1977-09-13 Engelhard Minerals & Chemicals Corporation Combustion method and apparatus
US4054028A (en) * 1974-09-06 1977-10-18 Mitsubishi Jukogyo Kabushiki Kaisha Fuel combustion apparatus
US4067299A (en) * 1975-09-25 1978-01-10 Daimler-Benz Aktiengesellschaft Split-gas production for internal combustion engine
US4090362A (en) * 1976-08-23 1978-05-23 Bourque Robert F External combustion power cycle and engine with combustion air preheating
US4095928A (en) * 1977-02-14 1978-06-20 Southern California Edison Company Method of reducing nitrogen oxide emissions in flue gas
US4113417A (en) * 1974-11-06 1978-09-12 Stein Industrie Combustion of hot gases of low calorific power
US4231302A (en) * 1979-05-14 1980-11-04 Albert Neuhaus-Schwermann Apparatus and process for burning of fuels of relatively young geological age and of any resulting gases
US4422391A (en) * 1981-03-12 1983-12-27 Kawasaki Jukogyo Kabushiki Kaisha Method of combustion of pulverized coal by pulverized coal burner
US4562795A (en) * 1983-07-20 1986-01-07 Firma Ferdinand Lentjes Dampfkessel- Und Maschinenbau Process and equipment for reducing the emission of pollutants in flue gases from furnace installations
US4761132A (en) * 1987-03-04 1988-08-02 Combustion Tec, Inc. Oxygen enriched combustion
US4842509A (en) * 1983-03-30 1989-06-27 Shell Oil Company Process for fuel combustion with low NOx soot and particulates emission
WO1989006334A1 (en) * 1988-01-04 1989-07-13 Oy Tampella Ab A method of comubustion for the reduction of the formation of nitrogen oxides in a combustion process, and an apparatus for applying the method
US4878830A (en) * 1988-06-20 1989-11-07 Exxon Research And Engineering Company Substoichiometric fuel firing for minimum NOx emissions
US4909727A (en) * 1987-03-04 1990-03-20 Combustion Tec, Inc. Oxygen enriched continuous combustion in a regenerative furance
US5316750A (en) * 1990-07-05 1994-05-31 Eduardo Szegu Hydrocarbon combustion process in which the carbon dioxide produced is prevented from dispersing onto the atmosphere, and a plant for its implementation
US5683238A (en) * 1994-05-18 1997-11-04 Praxair Technology, Inc. Method for operating a furnace
US5895211A (en) * 1994-12-27 1999-04-20 Asea Brown Boveri Ag Method and device for supplying a gaseous fuel to a premixing burner
WO2004020901A1 (en) * 2002-08-30 2004-03-11 Alstom Technology Ltd Hybrid burner and corresponding operating method
US20060080967A1 (en) * 2004-10-20 2006-04-20 Colket Meredith B Iii Method and system for rich-lean catalytic combustion

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5225479A (en) * 1975-08-21 1977-02-25 Asahi Chem Ind Co Ltd Exhaust gas purifying method
US4144017A (en) * 1976-11-15 1979-03-13 The Babcock & Wilcox Company Pulverized coal combustor
DE2850551A1 (en) * 1977-11-29 1979-06-07 Exxon Research Engineering Co MULTISTAGE PROCESS FOR COMBUSTION OF COMBINED NITROGEN CONTAINING FUELS
JPS5596811A (en) * 1979-01-19 1980-07-23 Masaki Sadakata Method for low nox combustion utilizing reduction by soot
AT391195B (en) * 1987-09-21 1990-08-27 Vaillant Gmbh METHOD FOR BURNING LIQUID OR GASEOUS FUELS AND DEVICE FOR CARRYING OUT THE METHOD
AT391185B (en) * 1988-02-08 1990-08-27 Vaillant Gmbh DEVICE FOR STAGE COMBUSTION OF A FUEL-AIR MIXTURE

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3228451A (en) * 1957-06-25 1966-01-11 Urquhart S 1926 Ltd Method of burning fuels
US3730668A (en) * 1971-03-03 1973-05-01 Tokyo Gas Co Ltd Combustion method of gas burners for suppressing the formation of nitrogen oxides and burner apparatus for practicing said method
US3746498A (en) * 1972-01-24 1973-07-17 Combustion Eng Reducing no{11 {11 emissions by additive injection
US3770369A (en) * 1971-03-31 1973-11-06 Mitsui Shipbuilding Eng Method of burning liquid fuel in fluid bed apparatus
US3832122A (en) * 1971-11-15 1974-08-27 Aqua Chem Inc Reduction of nitrogen oxides from products of hydrocarbon combustion with air

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BE361276A (en) *
FR648844A (en) * 1926-06-24 1928-12-14 Process for the preparation of mixtures of hydrogen and nitrogen
DE1135430B (en) * 1969-06-16 1962-08-30 Engelhard Ind Inc Process for the selective reduction of oxides of nitrogen in exhaust gas mixtures that arise during the production of nitric acid from ammonia

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3228451A (en) * 1957-06-25 1966-01-11 Urquhart S 1926 Ltd Method of burning fuels
US3730668A (en) * 1971-03-03 1973-05-01 Tokyo Gas Co Ltd Combustion method of gas burners for suppressing the formation of nitrogen oxides and burner apparatus for practicing said method
US3770369A (en) * 1971-03-31 1973-11-06 Mitsui Shipbuilding Eng Method of burning liquid fuel in fluid bed apparatus
US3832122A (en) * 1971-11-15 1974-08-27 Aqua Chem Inc Reduction of nitrogen oxides from products of hydrocarbon combustion with air
US3746498A (en) * 1972-01-24 1973-07-17 Combustion Eng Reducing no{11 {11 emissions by additive injection

Cited By (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4054028A (en) * 1974-09-06 1977-10-18 Mitsubishi Jukogyo Kabushiki Kaisha Fuel combustion apparatus
US4113417A (en) * 1974-11-06 1978-09-12 Stein Industrie Combustion of hot gases of low calorific power
US4067299A (en) * 1975-09-25 1978-01-10 Daimler-Benz Aktiengesellschaft Split-gas production for internal combustion engine
FR2337305A1 (en) * 1975-12-29 1977-07-29 Engelhard Min & Chem PROCESS FOR BURNING FUELS CONTAINING NITROGEN
US4054407A (en) * 1975-12-29 1977-10-18 Engelhard Minerals & Chemicals Corporation Method of combusting nitrogen-containing fuels
US4047877A (en) * 1976-07-26 1977-09-13 Engelhard Minerals & Chemicals Corporation Combustion method and apparatus
US4090362A (en) * 1976-08-23 1978-05-23 Bourque Robert F External combustion power cycle and engine with combustion air preheating
US4095928A (en) * 1977-02-14 1978-06-20 Southern California Edison Company Method of reducing nitrogen oxide emissions in flue gas
US4231302A (en) * 1979-05-14 1980-11-04 Albert Neuhaus-Schwermann Apparatus and process for burning of fuels of relatively young geological age and of any resulting gases
US4422391A (en) * 1981-03-12 1983-12-27 Kawasaki Jukogyo Kabushiki Kaisha Method of combustion of pulverized coal by pulverized coal burner
US4842509A (en) * 1983-03-30 1989-06-27 Shell Oil Company Process for fuel combustion with low NOx soot and particulates emission
US4562795A (en) * 1983-07-20 1986-01-07 Firma Ferdinand Lentjes Dampfkessel- Und Maschinenbau Process and equipment for reducing the emission of pollutants in flue gases from furnace installations
EP0281144A2 (en) * 1987-03-04 1988-09-07 Combustion Tec. Inc. Oxygen enriched combustion
US4761132A (en) * 1987-03-04 1988-08-02 Combustion Tec, Inc. Oxygen enriched combustion
US4909727A (en) * 1987-03-04 1990-03-20 Combustion Tec, Inc. Oxygen enriched continuous combustion in a regenerative furance
EP0281144A3 (en) * 1987-03-04 1990-04-04 Combustion Tec. Inc. Oxygen enriched combustion
WO1989006334A1 (en) * 1988-01-04 1989-07-13 Oy Tampella Ab A method of comubustion for the reduction of the formation of nitrogen oxides in a combustion process, and an apparatus for applying the method
US4878830A (en) * 1988-06-20 1989-11-07 Exxon Research And Engineering Company Substoichiometric fuel firing for minimum NOx emissions
US5316750A (en) * 1990-07-05 1994-05-31 Eduardo Szegu Hydrocarbon combustion process in which the carbon dioxide produced is prevented from dispersing onto the atmosphere, and a plant for its implementation
US5683238A (en) * 1994-05-18 1997-11-04 Praxair Technology, Inc. Method for operating a furnace
US5895211A (en) * 1994-12-27 1999-04-20 Asea Brown Boveri Ag Method and device for supplying a gaseous fuel to a premixing burner
WO2004020901A1 (en) * 2002-08-30 2004-03-11 Alstom Technology Ltd Hybrid burner and corresponding operating method
US20050196714A1 (en) * 2002-08-30 2005-09-08 Alstom Technology, Ltd. Hybrid burner and associated operating method
US7717700B2 (en) 2002-08-30 2010-05-18 Alstom Technology Ltd. Hybrid burner and associated operating method
US20060080967A1 (en) * 2004-10-20 2006-04-20 Colket Meredith B Iii Method and system for rich-lean catalytic combustion
US7444820B2 (en) * 2004-10-20 2008-11-04 United Technologies Corporation Method and system for rich-lean catalytic combustion

Also Published As

Publication number Publication date
DE2409950B2 (en) 1978-09-28
JPS49124625A (en) 1974-11-28
JPS5237611B2 (en) 1977-09-24
FR2220043A1 (en) 1974-09-27
DE2409950A1 (en) 1974-09-05
FR2220043B1 (en) 1977-09-16

Similar Documents

Publication Publication Date Title
US3914091A (en) Combustion method for hydrocarbonic fuels with low emission of nitrogen oxides
CA2093601C (en) Premixed/high-velocity fuel jet low no x burner
US5002483A (en) Multi-stage combustion chamber for combustion of nitrogen-containing gas with reduced NOx emissions, and method for its operation
US3928961A (en) Catalytically-supported thermal combustion
US3940923A (en) Method of operating catalytically supported thermal combustion system
US5297515A (en) Fuel supply systems for engines and combustion processes therefor
US4004413A (en) Combustible mixture supply system
IT1028056B (en) PROCEDURE AND EQUIPMENT FOR THE REDUCTION OF ATMOSPHERIC POLLUTANTS THROUGH SELECTIVE RECIRCULATION OF CIMINIERA GAS
JP7385476B2 (en) Ammonia combustion equipment and ammonia fuel cell system
US5318436A (en) Low NOx combustion piloted by low NOx pilots
JPS6091115A (en) Method of reducing nox radiation when burning fuel containing nitrogen
US3897225A (en) Method and apparatus for generating a gas mixture to be formed through catalytic conversion of fuel and a gas serving as an oxygen carrier
US4500281A (en) Burning of fuels
US5085841A (en) Method for reduction of pollution from combustion chambers
KR850004259A (en) Method for producing syngas from hydrocarbon fuel
US3953576A (en) Maximizing conversion of nitrogen oxides in the treatment of combustion exhaust gases
EP0009523B1 (en) A method of at least partially burning a hydrocarbon and/or carbonaceous fuel
GB1434993A (en) Furnace and generation of heat therein by oxidising a carbon aceous fuel
US4233188A (en) Catalyst for treating exhaust gas from an internal combustion engine
GB1460312A (en) Method of and apparatus for burning hydrocarbon fuels with air
FR2241339A1 (en) Single catalysts for exhaust gas purifcn - contg. ruthenium metal or oxide and gp. IIA metal oxide on inert carrier
JPH11509307A (en) Burners with catalytic introduction combustion, especially for gas turbines
SK55397A3 (en) Method of reducing nitrogen oxides in primary burning flue gas leaving the furnace and device for carrying out this method
JPS5813906A (en) Combustion method for generating low nitrogen oxide exhaust
JPS62288420A (en) Catalytic burner