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at84a.txt Benedick (1986) [14]
Category: critical energy Fuel: C2H4 Sub-Category: spherical, high explosive Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: .6-3.0
at109a.txt Bull (1978) [23]
Category: critical energy Fuel: C2H4 Sub-Category: spherical, high explosive Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at109b.txt Bull (1979) [21]
Category: critical energy Fuel: C2H4 Sub-Category: spherical, high explosive Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.8
at109c.txt Hikita (1975) [50]
Category: critical energy Fuel: C2H4 Sub-Category: spherical, high explosive Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1.2
at79b.txt Matsui (1979) [80]
Category: critical energy Fuel: C2H4 Sub-Category: spherical Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1.33
at32b.txt Murray (1981) [88]
Category: critical energy Fuel: C2H4 Sub-Category: high explosive Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
Edited Last: May 27, 2002