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at193a.txt Aminallah (1993) [4]
Category: cell size Fuel: CH4 Sub-Category: length Oxidizer: O2 Initial Pressure: 120 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.7-1.3
at194c.txt Aminallah (1993) [4]
Category: cell size Fuel: CH4 Sub-Category: length Oxidizer: O2 Initial Pressure: 90-120 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at194a.txt Bauer (1985) [10]
Category: cell size Fuel: CH4 Sub-Category: length Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
mk1a.txt Bauer (1986) [12]
Category: cell size Fuel: C3H8 Sub-Category: length Oxidizer: Air Initial Pressure: 270-4600 kPa Diluent: Initial Temperature: K Equivalence Ratio: 1.13
mk1b.txt Bauer (1986) [12]
Category: cell size Fuel: C3H8 Sub-Category: length Oxidizer: Air Initial Pressure: 270-900 kPa Diluent: Initial Temperature: K Equivalence Ratio: 1.31
mk1c.txt Bauer (1986) [12]
Category: cell size Fuel: C3H8 Sub-Category: length Oxidizer: Air Initial Pressure: 1000-4500 kPa Diluent: Initial Temperature: K Equivalence Ratio: 1.41
mk1d.txt Bauer (1986) [12]
Category: cell size Fuel: C3H8 Sub-Category: length Oxidizer: Air Initial Pressure: 5300 kPa Diluent: Initial Temperature: K Equivalence Ratio: 1.61
mk3a.txt Bauer (1986) [12]
Category: cell size Fuel: C2H4 Sub-Category: length Oxidizer: Air Initial Pressure: 300-1000 kPa Diluent: Initial Temperature: K Equivalence Ratio: 0.8
mk3b.txt Bauer (1986) [12]
Category: cell size Fuel: C2H4 Sub-Category: length Oxidizer: Air Initial Pressure: 150-900 kPa Diluent: Initial Temperature: K Equivalence Ratio: 1.13
mk3c.txt Bauer (1986) [12]
Category: cell size Fuel: C2H4 Sub-Category: length Oxidizer: Air Initial Pressure: 300-1000 kPa Diluent: Initial Temperature: K Equivalence Ratio: 1.13
mk3d.txt Bauer (1986) [12]
Category: cell size Fuel: C2H4 Sub-Category: length Oxidizer: Air Initial Pressure: 200-1100 kPa Diluent: Initial Temperature: K Equivalence Ratio: 1.61
mk4a.txt Bauer (1986) [12]
Category: cell size Fuel: C2H4 Sub-Category: length Oxidizer: O2 Initial Pressure: 50-200 kPa Diluent: N2 Initial Temperature: K Equivalence Ratio: 1.01
mk4b.txt Bauer (1986) [12]
Category: cell size Fuel: C2H4 Sub-Category: length Oxidizer: O2 Initial Pressure: 70-400 kPa Diluent: N2 Initial Temperature: K Equivalence Ratio: 1.05
mk4c.txt Bauer (1986) [12]
Category: cell size Fuel: C2H4 Sub-Category: length Oxidizer: O2 Initial Pressure: 150-600 kPa Diluent: N2 Initial Temperature: K Equivalence Ratio: 1.05
mk4d.txt Bauer (1986) [12]
Category: cell size Fuel: C2H4 Sub-Category: length Oxidizer: O2 Initial Pressure: 350-900 kPa Diluent: N2 Initial Temperature: K Equivalence Ratio: 1.05
mk5a.txt Bauer (1986) [12]
Category: cell size Fuel: CH4 Sub-Category: length Oxidizer: O2 Initial Pressure: 50-230 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1.08
mk5b.txt Bauer (1986) [12]
Category: cell size Fuel: CH4 Sub-Category: length Oxidizer: O2 Initial Pressure: 300-700 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1.09
mk5c.txt Bauer (1986) [12]
Category: cell size Fuel: CH4 Sub-Category: length Oxidizer: O2 Initial Pressure: 650-1100 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1.15
at194b.txt Bull (1982) [27]
Category: cell size Fuel: CH4 Sub-Category: length Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at93a.txt Bull (1982) [22]
Category: cell size Fuel: C2H6 Sub-Category: length Oxidizer: O2 Initial Pressure: 33.8 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 0.5-2
at93b.txt Bull (1982) [22]
Category: cell size Fuel: C2H6 Sub-Category: length Oxidizer: O2 Initial Pressure: 67.5 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 0.5-2
at139a.txt Bull (1982) [27]
Category: cell size Fuel: C2H6 Sub-Category: length Oxidizer: O2 Initial Pressure: 3-30 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at139e.txt Bull (1982) [27]
Category: cell size Fuel: C2H6 Sub-Category: length Oxidizer: Air Initial Pressure: 60.8-101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at139b.txt Bull (1982) [27]
Category: cell size Fuel: C2H6 Sub-Category: length Oxidizer: O2 Initial Pressure: 10-40.5 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
at139c.txt Bull (1982) [27]
Category: cell size Fuel: C2H6 Sub-Category: length Oxidizer: O2 Initial Pressure: 10-40.5 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
at139d.txt Bull (1982) [27]
Category: cell size Fuel: C2H6 Sub-Category: length Oxidizer: O2 Initial Pressure: 40.5 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
at140a.txt Bull (1982) [27]
Category: cell size Fuel: C2H2 Sub-Category: length Oxidizer: Air Initial Pressure: 8.1-101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at140b.txt Bull (1982) [27]
Category: cell size Fuel: C2H4 Sub-Category: length Oxidizer: Air Initial Pressure: 30.4-101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at169e.txt Libouton (1975) [72]
Category: cell size Fuel: 18.46CO+H2 Sub-Category: length Oxidizer: O2 Initial Pressure: 22.7-33.3 kPa Diluent: 11.88Ar+CF3Br Initial Temperature: 293 K Equivalence Ratio: 1
at169a.txt Libouton (1975) [72]
Category: cell size Fuel: 18.46CO+H2 Sub-Category: length Oxidizer: O2 Initial Pressure: 4.7-40 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at169d.txt Libouton (1975) [72]
Category: cell size Fuel: 18.46CO+H2 Sub-Category: length Oxidizer: O2 Initial Pressure: 13.3-40 kPa Diluent: 11.88Ar+CFCl3 Initial Temperature: 293 K Equivalence Ratio: 1
at169c.txt Libouton (1975) [72]
Category: cell size Fuel: 18.46CO+H2 Sub-Category: length Oxidizer: O2 Initial Pressure: 8-33.3 kPa Diluent: 11.88Ar+CF2Cl2 Initial Temperature: 293 K Equivalence Ratio: 1
at169b.txt Libouton (1975) [72]
Category: cell size Fuel: 18.46CO+H2 Sub-Category: length Oxidizer: O2 Initial Pressure: 9.3-26.7 kPa Diluent: 11.88Ar+CF3Cl Initial Temperature: 293 K Equivalence Ratio: 1
Edited Last: May 27, 2002