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mk30.txt Atkinson (1980) [7]
Category: critical energy Fuel: H2 Sub-Category: spherical, high explosive Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: .95-1.5
at34b.txt Benedick (1986) [14]
Category: critical energy Fuel: H2 Sub-Category: spherical, high explosive Oxidizer: Air Initial Pressure: 83.99 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.48-3.4
at34c.txt Benedick (1986) [14]
Category: critical energy Fuel: H2 Sub-Category: spherical, high explosive Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.5-3.1
at24.txt Guirao (1982) [48]
Category: critical energy Fuel: H2 Sub-Category: spherical, high explosive Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.85-1.86
at181a.txt Knystautas (1988) [55]
Category: critical energy Fuel: H2 Sub-Category: spherical, spark Oxidizer: Cl2 Initial Pressure: 8 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at181b.txt Knystautas (1988) [55]
Category: critical energy Fuel: H2 Sub-Category: spherical, spark Oxidizer: Cl2 Initial Pressure: 16 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
mk82a.txt Lee (1977) [68]
Category: critical energy Fuel: H2 Sub-Category: cylindrical Oxidizer: O2 Initial Pressure: 12.2-50.7 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at55a.txt Litchfield (1962) [73]
Category: critical energy Fuel: H2 Sub-Category: spherical, spark Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: .5-1.2
at55b.txt Litchfield (1962) [73]
Category: critical energy Fuel: H2 Sub-Category: spherical, exploding wire Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: .27-2
at123a.txt Macek (1963) [75]
Category: critical energy Fuel: H2 Sub-Category: spherical, exploding wire Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: CH4 Initial Temperature: 297 K Equivalence Ratio: 0.82
at123b.txt Macek (1963) [75]
Category: critical energy Fuel: H2 Sub-Category: spherical, exploding wire Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: CH3Cl Initial Temperature: 297 K Equivalence Ratio: 0.82
at123d.txt Macek (1963) [75]
Category: critical energy Fuel: H2 Sub-Category: spherical, exploding wire Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: CCl4 Initial Temperature: 297 K Equivalence Ratio: 0.82
at123e.txt Macek (1963) [75]
Category: critical energy Fuel: H2 Sub-Category: spherical, exploding wire Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: CHCl3 Initial Temperature: 297 K Equivalence Ratio: 0.82
at123f.txt Macek (1963) [75]
Category: critical energy Fuel: H2 Sub-Category: spherical, exploding wire Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Cl2 Initial Temperature: 297 K Equivalence Ratio: 0.82
at124b.txt Macek (1963) [75]
Category: critical energy Fuel: H2 Sub-Category: spherical, exploding wire Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: C2H6 Initial Temperature: 297 K Equivalence Ratio: 0.82
at124c.txt Macek (1963) [75]
Category: critical energy Fuel: H2 Sub-Category: spherical, exploding wire Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: i-C4H10 Initial Temperature: 297 K Equivalence Ratio: 0.82
at124d.txt Macek (1963) [75]
Category: critical energy Fuel: H2 Sub-Category: spherical, exploding wire Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: n-C4H10 Initial Temperature: 297 K Equivalence Ratio: 0.82
at124e.txt Macek (1963) [75]
Category: critical energy Fuel: H2 Sub-Category: spherical, exploding wire Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: C3H8 Initial Temperature: 297 K Equivalence Ratio: 0.82
at126a.txt Macek (1963) [75]
Category: critical energy Fuel: H2 Sub-Category: spherical, exploding wire Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Isobutene Initial Temperature: 297 K Equivalence Ratio: 0.82
at126b.txt Macek (1963) [75]
Category: critical energy Fuel: H2 Sub-Category: spherical, exploding wire Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Trans-butene-2 Initial Temperature: 297 K Equivalence Ratio: 0.82
at126c.txt Macek (1963) [75]
Category: critical energy Fuel: H2 Sub-Category: spherical, exploding wire Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Propylene Initial Temperature: 297 K Equivalence Ratio: 0.82
at126d.txt Macek (1963) [75]
Category: critical energy Fuel: H2 Sub-Category: spherical, exploding wire Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Butene-1 Initial Temperature: 297 K Equivalence Ratio: 0.82
at126e.txt Macek (1963) [75]
Category: critical energy Fuel: H2 Sub-Category: spherical, exploding wire Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Ethylene Initial Temperature: 297 K Equivalence Ratio: 0.82
at53.txt Makeev (1983) [76]
Category: critical energy Fuel: H2 Sub-Category: spherical, high explosive Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.68-2.1
at67a.txt Matsui (1979) [80]
Category: critical energy Fuel: H2 Sub-Category: spherical Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.6 - 1.2
at49a.txt Zitoun (1995) [130]
Category: critical energy Fuel: H2 Sub-Category: spherical Oxidizer: O2 Initial Pressure: 50-80 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at49b.txt Zitoun (1995) [130]
Category: critical energy Fuel: H2 Sub-Category: spherical Oxidizer: O2 Initial Pressure: 36-70 kPa Diluent: Initial Temperature: 123 K Equivalence Ratio: 1
Edited Last: May 27, 2002