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at192a.txt Abid (1991) [1]
Category: cell size Fuel: CH4 Sub-Category: width Oxidizer: O2 Initial Pressure: 6.5-12 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at193b.txt Aminallah (1993) [4]
Category: cell size Fuel: CH4 Sub-Category: width Oxidizer: O2 Initial Pressure: 120 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.7-1.3
at176a.txt Beeson (1991) [13]
Category: cell size Fuel: CH4 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at13a.txt Knystautas (1984) [53]
Category: cell size Fuel: CH4 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at73.txt Knystautas (1982) [55]
Category: cell size Fuel: CH4 Sub-Category: width Oxidizer: O2 Initial Pressure: 8-13.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at199a.txt Laberge (1993) [61]
Category: cell size Fuel: CH4 Sub-Category: width Oxidizer: O2 Initial Pressure: 8-26.7 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at57d.txt Manzhalei (1974) [78]
Category: cell size Fuel: CH4 Sub-Category: width Oxidizer: O2 Initial Pressure: 30.4-912 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at157a.txt Moen (1984) [83]
Category: cell size Fuel: CH4 Sub-Category: width Oxidizer: Air Initial Pressure: 92.5 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at184a.txt Pedley (1988) [97]
Category: cell size Fuel: CH4 Sub-Category: width Oxidizer: O2 Initial Pressure: 7-13 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at128a.txt Strehlow (1969) [107]
Category: cell size Fuel: CH4 Sub-Category: width Oxidizer: O2 Initial Pressure: 15.2-50.7 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at171a.txt Tieszen (1991) [112]
Category: cell size Fuel: CH4 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 298-373 K Equivalence Ratio: 1
ja6a.txt Akbar (1997) [3]
Category: cell size Fuel: CH4 Sub-Category: width Oxidizer: O2 Initial Pressure: 70-72 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja6b.txt Akbar (1997) [3]
Category: cell size Fuel: CH4 Sub-Category: width Oxidizer: O2 Initial Pressure: 102 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja7a.txt Akbar (1997) [3]
Category: cell size Fuel: CH4 Sub-Category: width Oxidizer: N2O Initial Pressure: 57-72 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja7b.txt Akbar (1997) [3]
Category: cell size Fuel: CH4 Sub-Category: width Oxidizer: N2O Initial Pressure: 77-87 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja7c.txt Akbar (1997) [3]
Category: cell size Fuel: CH4 Sub-Category: width Oxidizer: N2O Initial Pressure: 92-97 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja7d.txt Akbar (1997) [3]
Category: cell size Fuel: CH4 Sub-Category: width Oxidizer: N2O Initial Pressure: 102 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja7e.txt Akbar (1997) [3]
Category: cell size Fuel: CH4 Sub-Category: width Oxidizer: N2O Initial Pressure: 86-97 kPa Diluent: Air Initial Temperature: 293 K Equivalence Ratio: ?
Edited Last: August 31, 1999