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at161a.txt Bauer (1984) [11]
Category: critical tube Fuel: CH4 Sub-Category: Oxidizer: O2 Initial Pressure: 400-2200 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1.08
at161b.txt Bauer (1984) [11]
Category: critical tube Fuel: CH4 Sub-Category: Oxidizer: O2 Initial Pressure: 200-1200 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1.09
at161c.txt Bauer (1984) [11]
Category: critical tube Fuel: CH4 Sub-Category: Oxidizer: O2 Initial Pressure: 200-1100 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1.15
at161d.txt Bauer (1984) [11]
Category: critical tube Fuel: CH4 Sub-Category: Oxidizer: O2 Initial Pressure: 500-1900 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1.09
at147a.txt Knystautas (1982) [56]
Category: critical tube Fuel: CH4 Sub-Category: Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
at147b.txt Matsui (1979) [80]
Category: critical tube Fuel: CH4 Sub-Category: Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1.3
at147c.txt Matsui (1979) [80]
Category: critical tube Fuel: CH4 Sub-Category: Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1.3
at147d.txt Matsui (1979) [80]
Category: critical tube Fuel: CH4 Sub-Category: Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1.3
mk137k.txt Matsui (1979) [80]
Category: critical tube Fuel: CH4 Sub-Category: Oxidizer: O2 Initial Pressure: 101-184 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
att2.txt Zeldovich (1956) [129]
Category: critical tube Fuel: CH4 Sub-Category: Oxidizer: O2 Initial Pressure: 106.7 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
Edited Last: May 27, 2002