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at192b.txt Abid (1991) [1]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: O2 Initial Pressure: 1.2-14 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at157e.txt Bull (1982) [27]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
ja10a.txt EDL (unpublished) [39]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: O2 Initial Pressure: 30-80 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja10b.txt EDL (unpublished) [39]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: O2 Initial Pressure: 30-70 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja10c.txt EDL (unpublished) [39]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: O2 Initial Pressure: 60-80 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja10d.txt EDL (unpublished) [39]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: O2 Initial Pressure: 50-90 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja10e.txt EDL (unpublished) [39]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: O2 Initial Pressure: 50-100 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja11b.txt EDL (unpublished) [39]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: O2 Initial Pressure: 50 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja12.txt EDL (unpublished) [39]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: O2 Initial Pressure: 50 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
ja11a.txt Kaneshige (1999) [53]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: O2 Initial Pressure: 45-50 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
at13b.txt Knystautas (1984) [54]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.5 - 2.2
mk7c.txt Knystautas (1982) [56]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
at149a.txt Knystautas (1982) [56]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: O2 Initial Pressure: 1.3-13.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at157c.txt Moen (1984) [84]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: Air Initial Pressure: 92.5 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.55-1.1
at157f.txt Moen (1984) [84]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: Air Initial Pressure: 92.5 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
mk157g.txt Moen (1984) [84]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: Air Initial Pressure: 92.5 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: .5-.7
at203.txt Moen (1982) [85]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: Air Initial Pressure: 92.5 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.6-1.1
at158.txt Murray (1984) [90]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: .5-1.1
at128b.txt Strehlow (1969) [108]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: O2 Initial Pressure: 4.1-15.2 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at128c.txt Strehlow (1969) [108]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: O2 Initial Pressure: 4.1-35.5 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at128d.txt Strehlow (1969) [108]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: O2 Initial Pressure: 12.2-70.9 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at172d.txt Tieszen (1991) [114]
Category: cell size Fuel: C2H4 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 298-373 K Equivalence Ratio: 1
Edited Last: May 27, 2002