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at71a.txt Knystautas (1982) [56]
Category: critical tube Fuel: C2H2 Sub-Category: Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
at22a4.txt Matsui (1979) [80]
Category: critical tube Fuel: C2H2 Sub-Category: Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1.67
at66b.txt Matsui (1979) [80]
Category: critical tube Fuel: C2H2 Sub-Category: Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1.67
at66a.txt Matsui (1979) [80]
Category: critical tube Fuel: C2H2 Sub-Category: Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
at22a1.txt Moen (1984) [84]
Category: critical tube Fuel: C2H2 Sub-Category: Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.6
at20a.txt Rinnan (1982) [102]
Category: critical tube Fuel: C2H2 Sub-Category: Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.45-0.75
mk127.txt Zeldovich (1956) [129]
Category: critical tube Fuel: C2H2 Sub-Category: Oxidizer: O2 Initial Pressure: 106.7 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
Edited Last: May 27, 2002