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at33a.txt Anderson (1992) [5]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 26.3-56.7 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at33b.txt Anderson (1992) [5]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 26.3-56.7 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at33c.txt Anderson (1992) [5]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 26.3-56.7 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 0.75
at58a.txt Barthel (1974) [9]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 6.7-53.3 kPa Diluent: Initial Temperature: 298 K Equivalence Ratio: 1
at58b.txt Barthel (1974) [9]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 6.7-53.3 kPa Diluent: Ar Initial Temperature: 298 K Equivalence Ratio: 1
at58c.txt Barthel (1974) [9]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 6.7-53.3 kPa Diluent: Ar Initial Temperature: 298 K Equivalence Ratio: 1
at19.txt Benedick (1984) [16]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: Air Initial Pressure: 82.7 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: .5-.7
at14.txt Ciccarelli (1994) [29]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: Air Initial Pressure: 100 kPa Diluent: Initial Temperature: 300 K Equivalence Ratio: .5-3.3
at15.txt Ciccarelli (1994) [29]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: Air Initial Pressure: 100 kPa Diluent: Initial Temperature: 500 K Equivalence Ratio: .35-2.4
at16.txt Ciccarelli (1994) [29]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: Air Initial Pressure: 100 kPa Diluent: Initial Temperature: 650 K Equivalence Ratio: .26-2.4
mk9b.txt Denisov (1960) [31]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 4-120 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
H2-Air1.txt Guirao (1982) [47]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.54 - 2.03
at182a.txt Knystautas (1988) [53]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: Cl2 Initial Pressure: 2.1-24.0 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.56
at182b.txt Knystautas (1988) [53]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: Cl2 Initial Pressure: 2.1-24.0 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.67
at182c.txt Knystautas (1988) [53]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: Cl2 Initial Pressure: 2.1-24.0 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1.5
at182d.txt Knystautas (1988) [53]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: Cl2 Initial Pressure: 2.1-24.0 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
mk7b.txt Knystautas (1982) [54]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
at74.txt Knystautas (1982) [54]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 5.3-20 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at35a.txt Kumar (1990) [59]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 106.6 kPa Diluent: He Initial Temperature: 293 K Equivalence Ratio: 1
at35b.txt Kumar (1990) [59]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 106.6 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at38a.txt Kumar (1990) [59]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 106.6 kPa Diluent: He and CO2 Initial Temperature: 295 K Equivalence Ratio: 1
at38b.txt Kumar (1990) [59]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 106.6 kPa Diluent: He and CO2 Initial Temperature: 295 K Equivalence Ratio: 1
at38c.txt Kumar (1990) [59]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 106.6 kPa Diluent: He and CO2 Initial Temperature: 295 K Equivalence Ratio: 1
at39a.txt Kumar (1990) [59]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 106.6 kPa Diluent: He and H2O Initial Temperature: 353 K Equivalence Ratio: 1
at39b.txt Kumar (1990) [59]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 106.6 kPa Diluent: He and H2O Initial Temperature: 353 K Equivalence Ratio: 1
at39c.txt Kumar (1990) [59]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 106.6 kPa Diluent: He and H2O Initial Temperature: 353 K Equivalence Ratio: 1
at39d.txt Kumar (1990) [59]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 106.6 kPa Diluent: He and H2O Initial Temperature: 353 K Equivalence Ratio: 1
at42a.txt Kumar (1990) [59]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 20-150 kPa Diluent: He Initial Temperature: 295 K Equivalence Ratio: 1
at42b.txt Kumar (1990) [59]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 20-150 kPa Diluent: He Initial Temperature: 295 K Equivalence Ratio: 1
at47a.txt Lee (1977) [66]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 5.1-30.4 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at47b.txt Lee (1977) [66]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 20.3-40.5 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at57a.txt Manzhalei (1974) [77]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 10.1-1013 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at5a.txt Stamps (1991) [103]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: Air Initial Pressure: 25.3 - 152.0 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at5b.txt Stamps (1991) [103]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: Air Initial Pressure: 20.2 - 253.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.5
at64c.txt Strehlow (1969) [108]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 13.2-32.4 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 0.36
at64b.txt Strehlow (1969) [108]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 13.2-32.4 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 2.12
at64a.txt Strehlow (1969) [108]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 13.2-32.4 kPa Diluent: 3.75Ar+N2 Initial Temperature: 293 K Equivalence Ratio: 1
at62a.txt Strehlow (1969) [105]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 5.6-32.4 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at69f.txt Strehlow (1967) [107]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 14-47 kPa Diluent: He Initial Temperature: 293 K Equivalence Ratio: 1
at69c.txt Strehlow (1967) [107]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 8-47 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at69d.txt Strehlow (1967) [107]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 10-40 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at69e.txt Strehlow (1967) [107]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 8-40 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at69g.txt Strehlow (1967) [107]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 24-46 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at62b.txt Strehlow (1969) [105]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 9.1-40.5 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at65.txt Strehlow (1969) [108]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 1.3-7.3 kPa Diluent: Ar Initial Temperature: 600 - 800 K Equivalence Ratio: 1
at3a.txt Tieszen (1986) [109]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: Air Initial Pressure: 150 - 300 kPa Diluent: Initial Temperature: 373 K Equivalence Ratio: 0.35 - 3
at3b.txt Tieszen (1986) [109]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: Air Initial Pressure: 150 - 304 kPa Diluent: steam Initial Temperature: 373 K Equivalence Ratio: .5 - 2
at3c.txt Tieszen (1986) [109]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: Air Initial Pressure: 150 - 304 kPa Diluent: steam Initial Temperature: 373 K Equivalence Ratio: .8 - 2
at3d.txt Tieszen (1986) [109]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: Air Initial Pressure: 150 - 304 kPa Diluent: steam Initial Temperature: 373 K Equivalence Ratio: .93 - 1.04
at4.txt Tieszen (1986) [109]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 298 K Equivalence Ratio: 0.4 - 5
mk8a.txt Voitsekhovskii (1966) [121]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 13-85 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at21a.txt Desbordes (1990) [35]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 50.7-101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at21b.txt Zitoun (1995) [126]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 50.7-101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at21c.txt Zitoun (1995) [126]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 50.7-101.3 kPa Diluent: Initial Temperature: 123 K Equivalence Ratio: 1
ja1a.txt Kaneshige (1999) [51]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 100 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja1b.txt EDL (unpublished) [38]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 100 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja1c.txt Kaneshige (1999) [51]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 10-101.5 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja1d.txt Kaneshige (1999) [51]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 26.5-101.5 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja1e.txt Kaneshige (1999) [51]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 26.5-101.5 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja2.txt EDL (unpublished) [38]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 100 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
ja3.txt EDL (unpublished) [38]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 100 kPa Diluent: He Initial Temperature: 293 K Equivalence Ratio: 1
ja4.txt EDL (unpublished) [38]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: O2 Initial Pressure: 100 kPa Diluent: CO2 Initial Temperature: 293 K Equivalence Ratio: 1
ja5a.txt Pfahl (1998) [96]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: N2O Initial Pressure: 70.9 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.06-5.7
ja5b.txt Pfahl (1998) [96]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: N2O Initial Pressure: 70.9 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 0.11-4.0
ja5c.txt Pfahl (1998) [96]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: N2O + O2 Initial Pressure: 70.9 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 0.231-1.667
ja5d.txt Akbar (1997) [3]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: N2O Initial Pressure: 100 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja5e.txt Akbar (1997) [3]
Category: cell size Fuel: H2 Sub-Category: width Oxidizer: N2O Initial Pressure: 100 kPa Diluent: Air Initial Temperature: 293 K Equivalence Ratio: 0.07-0.39
Edited Last: August 30, 1999