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at195d.txt Aminallah (1993) [4]
Category: critical energy Fuel: CH4 Sub-Category: cylindrical, exploding wire Oxidizer: O2 Initial Pressure: 100 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: .7-1.3
at195e.txt Aminallah (1993) [4]
Category: critical energy Fuel: CH4 Sub-Category: cylindrical, exploding wire Oxidizer: O2 Initial Pressure: 120 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: .7-1.3
at177a.txt Beeson (1991) [13]
Category: critical energy Fuel: CH4 Sub-Category: spherical Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at210a.txt Bull (1976) [26]
Category: critical energy Fuel: CH4 Sub-Category: spherical, high explosive Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
at209a.txt Desbordes (1973) [33]
Category: critical energy Fuel: CH4 Sub-Category: cylindrical Oxidizer: O2 Initial Pressure: 100 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at210b.txt Kogarko (1965) [60]
Category: critical energy Fuel: CH4 Sub-Category: spherical, high explosive Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: N2 Initial Temperature: K Equivalence Ratio: 1
at79a.txt Matsui (1979) [80]
Category: critical energy Fuel: CH4 Sub-Category: spherical Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: .7-1.7
at195c.txt Nicholls (1979) [92]
Category: critical energy Fuel: CH4 Sub-Category: cylindrical, high explosive Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 298 K Equivalence Ratio: 1
at115.txt Wolanski (1981) [128]
Category: critical energy Fuel: CH4 Sub-Category: planar Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: .8-1.4