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at162a.txt Bauer (1984) [11]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: O2 Initial Pressure: 350-880 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 3
at162b.txt Bauer (1984) [11]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: O2 Initial Pressure: 150-600 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 3
at162c.txt Bauer (1984) [11]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: O2 Initial Pressure: 100-400 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 3
at163a.txt Bauer (1984) [11]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: O2 Initial Pressure: 100 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1.05
mk142a.txt Knystautas (1982) [56]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
at56c.txt Makris (1994) [77]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Initial Temperature: K Equivalence Ratio: .5-2.7
at137g.txt Matsui (1979) [80]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: O2 Initial Pressure: 14.6-101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at56d.txt Matsui (1979) [80]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at80b.txt Matsui (1979) [80]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1.5
at80c.txt Matsui (1979) [80]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 2
at66c.txt Matsui (1979) [80]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1.5
at22b.txt Moen (1984) [84]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.6
at22c.txt Moen (1982) [85]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: .7-1
at77a.txt Moen (1985) [87]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: CF4 Initial Temperature: 293 K Equivalence Ratio: 0.88
at77b.txt Moen (1985) [87]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: CF3Br Initial Temperature: 293 K Equivalence Ratio: 0.88
at77c.txt Moen (1985) [87]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: CF3Br Initial Temperature: 293 K Equivalence Ratio: 0.88
at77d.txt Moen (1985) [87]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: CO2 Initial Temperature: 293 K Equivalence Ratio: 0.88
at200c.txt Moen (1981) [83]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
at31c.txt Rinnan (1982) [102]
Category: critical tube Fuel: C2H4 Sub-Category: Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.6-.78
Edited Last: May 27, 2002