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at26.txt Agafonov (1994) [2]
Category: minimum tube Fuel: H2 Sub-Category: round, confined Oxidizer: Air Initial Pressure: 100 kPa Diluent: Initial Temperature: 298 K Equivalence Ratio: .4-3.7
at27a.txt Agafonov (1994) [2]
Category: minimum tube Fuel: H2 Sub-Category: round, confined Oxidizer: O2 Initial Pressure: 100 kPa Diluent: Initial Temperature: 298 K Equivalence Ratio: .1-4.5
at27b.txt Agafonov (1994) [2]
Category: minimum tube Fuel: H2 Sub-Category: round, confined Oxidizer: O2 Initial Pressure: 100 kPa Diluent: Initial Temperature: 135 K Equivalence Ratio: .1-4.5
at28a.txt Agafonov (1994) [2]
Category: minimum tube Fuel: H2 Sub-Category: round, confined Oxidizer: O2 Initial Pressure: 100 kPa Diluent: Ar Initial Temperature: 298 K Equivalence Ratio: 1
at28b.txt Agafonov (1994) [2]
Category: minimum tube Fuel: H2 Sub-Category: round, confined Oxidizer: O2 Initial Pressure: 100 kPa Diluent: He Initial Temperature: 298 K Equivalence Ratio: 1
at28c.txt Agafonov (1994) [2]
Category: minimum tube Fuel: H2 Sub-Category: round, confined Oxidizer: O2 Initial Pressure: 100 kPa Diluent: N2 Initial Temperature: 298 K Equivalence Ratio: 1
at28d.txt Agafonov (1994) [2]
Category: minimum tube Fuel: H2 Sub-Category: round, confined Oxidizer: O2 Initial Pressure: 100 kPa Diluent: Ar Initial Temperature: 298 K Equivalence Ratio: 1
at28e.txt Agafonov (1994) [2]
Category: minimum tube Fuel: H2 Sub-Category: round, confined Oxidizer: O2 Initial Pressure: 100 kPa Diluent: He Initial Temperature: 298 K Equivalence Ratio: 1
at133.txt Pusch (1962) [100]
Category: minimum tube Fuel: CH4 Sub-Category: Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.3 - 1.5
Edited Last: May 27, 2002