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at108a.txt Freiwald (1962) [45]
Category: critical energy Fuel: C2H2 Sub-Category: high explosive Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: .7-4.1
at108b.txt Kogarko (1965) [60]
Category: critical energy Fuel: C2H2 Sub-Category: spherical, high explosive Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at82c.txt Lee (1977) [68]
Category: critical energy Fuel: C2H2 Sub-Category: spherical Oxidizer: O2 Initial Pressure: 4.1-12.2 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at82b.txt Lee (1977) [68]
Category: critical energy Fuel: C2H2 Sub-Category: cylindrical Oxidizer: O2 Initial Pressure: 6.1-40.5 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at44a.txt Matsui (1979) [80]
Category: critical energy Fuel: C2H2 Sub-Category: spherical Oxidizer: O2 Initial Pressure: kPa Diluent: Initial Temperature: K Equivalence Ratio: 0.7 - 2.1
at54a.txt Vasil'ev (1982) [121]
Category: critical energy Fuel: C2H2 Sub-Category: cylindrical Oxidizer: O2 Initial Pressure: 2.7-5.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at105a.txt Vasil'ev (1980) [123]
Category: critical energy Fuel: C2H2 Sub-Category: cylindrical, high explosive Oxidizer: Air Initial Pressure: 30.4-101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
Edited Last: May 27, 2002