FR2146433A1 - Power prodn from fuels - contg carbon, by adiabatic oxidn in combined catalytic and thermal processes - Google Patents

Power prodn from fuels - contg carbon, by adiabatic oxidn in combined catalytic and thermal processes

Info

Publication number
FR2146433A1
FR2146433A1 FR7226216A FR7226216A FR2146433A1 FR 2146433 A1 FR2146433 A1 FR 2146433A1 FR 7226216 A FR7226216 A FR 7226216A FR 7226216 A FR7226216 A FR 7226216A FR 2146433 A1 FR2146433 A1 FR 2146433A1
Authority
FR
France
Prior art keywords
oxidn
degrees
less
fuel
amt
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
FR7226216A
Other languages
French (fr)
Other versions
FR2146433B1 (en
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.)
Engelhard Minerals and Chemicals Corp
Original Assignee
Engelhard Minerals and Chemicals Corp
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 Engelhard Minerals and Chemicals Corp filed Critical Engelhard Minerals and Chemicals Corp
Publication of FR2146433A1 publication Critical patent/FR2146433A1/en
Application granted granted Critical
Publication of FR2146433B1 publication Critical patent/FR2146433B1/fr
Granted legal-status Critical Current

Links

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
    • F23C13/08Apparatus in which combustion takes place in the presence of catalytic material characterised by the catalytic material
    • 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02DCONTROLLING COMBUSTION ENGINES
    • F02D2200/00Input parameters for engine control
    • F02D2200/02Input parameters for engine control the parameters being related to the engine
    • F02D2200/06Fuel or fuel supply system parameters
    • F02D2200/0606Fuel temperature

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Gas Burners (AREA)

Abstract

Fuels which on combustion with the stoichiometric air quantity show an adiabatic flame temp. of >=1815 degrees C, are vaporised and passed with air over (1) a solid oxidn. catalyst at 815-1650 degrees C, followed by (2) a non-catalytic zone in wich a further amt. of fuel is oxidised at 815-1650 degrees C. The gas velocity before entering (1) is higher than the max. flame propagation speed and the ratio of free oxygen to fuel in the mixt. is at least 1.1 times the stoichiometric amt. for full combustion. The mixt. is in the ignitable range or on the lean side, and under the oxidn. conditions has a theoretical adiabatic flame temp. of 815-1650 degrees C. The amt. of catalyst in (1) is less than half that required for complete oxidn. of the fuel and the volume of zone (1) is less than that of zone (2). The hot gas from (2) can be used to generate power, e.g. by raising steam, or pref. in a gas turbine. A further catalytic oxidn. stage may be included after (2), pref. between stages of a gas turbine. The gas turbines are suitable for vehicle propulsion, the system producing less CO and hydrocarbon pollutants than internal combustion engines and less NO than conventional gas turbines.
FR7226216A 1971-07-21 1972-07-20 Power prodn from fuels - contg carbon, by adiabatic oxidn in combined catalytic and thermal processes Granted FR2146433A1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US16471871A 1971-07-21 1971-07-21

Publications (2)

Publication Number Publication Date
FR2146433A1 true FR2146433A1 (en) 1973-03-02
FR2146433B1 FR2146433B1 (en) 1978-11-03

Family

ID=22595783

Family Applications (1)

Application Number Title Priority Date Filing Date
FR7226216A Granted FR2146433A1 (en) 1971-07-21 1972-07-20 Power prodn from fuels - contg carbon, by adiabatic oxidn in combined catalytic and thermal processes

Country Status (5)

Country Link
JP (1) JPS5236294B1 (en)
DE (1) DE2235712C2 (en)
FR (1) FR2146433A1 (en)
IT (1) IT965920B (en)
SE (2) SE431669B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2382584A1 (en) * 1977-03-04 1978-09-29 Johnson Matthey Co Ltd Gas turbine with catalytic burner - which contains thermally stable, oxidn. resistant metal monolith with through holes in which catalytic combustion occurs
FR2613042A1 (en) * 1987-03-23 1988-09-30 Westinghouse Electric Corp METHOD FOR REDUCING THE EMISSIONS OF NITROGEN OXIDES FROM A FIXED FUEL TURBINE

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4242099A1 (en) * 1992-12-14 1994-06-16 Abb Patent Gmbh Appts., esp. gas turbine appts. - having coating on its operating parts in contact with fuel gas or waste gas to reduce pollutant emissions
SE9602688L (en) * 1996-07-08 1998-01-09 Volvo Ab Catalytic combustion chamber, and method for igniting and controlling the catalytic combustion chamber
WO2023154555A1 (en) * 2022-02-14 2023-08-17 Evoqua Water Technologies Llc Apparatus, system and method for pfas removal and mineralization

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE700618C (en) * 1939-01-04 1940-12-24 Sulzer Akt Ges Geb Gas turbine plant
DE1057074B (en) * 1956-06-19 1959-05-14 Metallgesellschaft Ag Process for the generation of hot combustion gases by catalytic combustion of fuel gases and / or vapors with oxygen or oxygen-containing gases
DE1939535C3 (en) * 1969-08-02 1974-08-01 Siemens Ag, 1000 Berlin Und 8000 Muenchen Device for the flameless catalytic combustion of hydrocarbons in sintered stones

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2382584A1 (en) * 1977-03-04 1978-09-29 Johnson Matthey Co Ltd Gas turbine with catalytic burner - which contains thermally stable, oxidn. resistant metal monolith with through holes in which catalytic combustion occurs
FR2613042A1 (en) * 1987-03-23 1988-09-30 Westinghouse Electric Corp METHOD FOR REDUCING THE EMISSIONS OF NITROGEN OXIDES FROM A FIXED FUEL TURBINE

Also Published As

Publication number Publication date
DE2235712C2 (en) 1982-09-16
SE431669B (en) 1984-02-20
JPS5236294B1 (en) 1977-09-14
FR2146433B1 (en) 1978-11-03
DE2235712A1 (en) 1973-02-01
IT965920B (en) 1974-02-11
SE7714927L (en) 1977-12-29

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