Go backward to Cell Width - C2H4 Fuel
Go up to Cell Size
Go forward to Cell Length - H2 Fuel
Go backward to Cell Width - C2H4 Fuel Go up to Cell Size Go forward to Cell Length - H2 Fuel |
|
ja16a.txt Akbar (1997) [3]
Category: cell size Fuel: NH3 Sub-Category: width Oxidizer: O2 Initial Pressure: 66-81 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja16b.txt Akbar (1997) [3]
Category: cell size Fuel: NH3 Sub-Category: width Oxidizer: N2O Initial Pressure: 55-75 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja16c.txt Akbar (1997) [3]
Category: cell size Fuel: NH3 Sub-Category: width Oxidizer: N2O Initial Pressure: 60-91 kPa Diluent: Air Initial Temperature: 293 K Equivalence Ratio: 1-0.71
at157j.txt Bull (1982) [27]
Category: cell size Fuel: C2H6 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at157m.txt Bull (1982) [27]
Category: cell size Fuel: C3H8 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
ja8b.txt EDL (unpublished) [39]
Category: cell size Fuel: C3H8 Sub-Category: width Oxidizer: O2 Initial Pressure: 30-70 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja8c.txt EDL (unpublished) [39]
Category: cell size Fuel: C3H8 Sub-Category: width Oxidizer: O2 Initial Pressure: 40-80 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja8d.txt EDL (unpublished) [39]
Category: cell size Fuel: C3H8 Sub-Category: width Oxidizer: O2 Initial Pressure: 50-90 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja8e.txt EDL (unpublished) [39]
Category: cell size Fuel: C3H8 Sub-Category: width Oxidizer: O2 Initial Pressure: 50-100 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja13.txt EDL (unpublished) [39]
Category: cell size Fuel: C6H14 Sub-Category: width Oxidizer: O2 Initial Pressure: 40 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja14a.txt EDL (unpublished) [39]
Category: cell size Fuel: C6H14 Sub-Category: width Oxidizer: Air Initial Pressure: 100 kPa Diluent: H2 Initial Temperature: 293 K Equivalence Ratio: 1
ja14b.txt EDL (unpublished) [39]
Category: cell size Fuel: C6H14 Sub-Category: width Oxidizer: Air Initial Pressure: 100 kPa Diluent: C2H4 Initial Temperature: 293 K Equivalence Ratio: 1
ja14c.txt EDL (unpublished) [39]
Category: cell size Fuel: C6H14 Sub-Category: width Oxidizer: Air Initial Pressure: 100 kPa Diluent: C2H2 Initial Temperature: 293 K Equivalence Ratio: 1
ja14d.txt EDL (unpublished) [39]
Category: cell size Fuel: C6H14 Sub-Category: width Oxidizer: Air Initial Pressure: 100 kPa Diluent: CO Initial Temperature: 293 K Equivalence Ratio: 1
ja15a.txt EDL (unpublished) [39]
Category: cell size Fuel: CO Sub-Category: width Oxidizer: Air Initial Pressure: 100 kPa Diluent: H2 Initial Temperature: 293 K Equivalence Ratio: 1
ja15b.txt EDL (unpublished) [39]
Category: cell size Fuel: CO Sub-Category: width Oxidizer: Air Initial Pressure: 100 kPa Diluent: C2H2 Initial Temperature: 293 K Equivalence Ratio: 1
ja15c.txt EDL (unpublished) [39]
Category: cell size Fuel: CO Sub-Category: width Oxidizer: Air Initial Pressure: 100 kPa Diluent: C2H4 Initial Temperature: 293 K Equivalence Ratio: 1
ja17.txt EDL (unpublished) [39]
Category: cell size Fuel: C3H6O Sub-Category: width Oxidizer: O2 Initial Pressure: 7.6-23.8 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
ja18a.txt EDL (unpublished) [39]
Category: cell size Fuel: C3H6O Sub-Category: width Oxidizer: O2 Initial Pressure: 22.5 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
ja18b.txt EDL (unpublished) [39]
Category: cell size Fuel: C3H6O Sub-Category: width Oxidizer: O2 Initial Pressure: 22.5 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
ja8a.txt Kaneshige (1999) [53]
Category: cell size Fuel: C3H8 Sub-Category: width Oxidizer: O2 Initial Pressure: 15-50 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
ja9.txt Kaneshige (1999) [53]
Category: cell size Fuel: C3H8 Sub-Category: width Oxidizer: O2 Initial Pressure: 50 kPa Diluent: Ar Initial Temperature: 293 K Equivalence Ratio: 1
at13f.txt Knystautas (1984) [54]
Category: cell size Fuel: C4H10 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.7 - 1.5
at13e.txt Knystautas (1984) [54]
Category: cell size Fuel: C3H8 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.6 - 1.7
at13d.txt Knystautas (1984) [54]
Category: cell size Fuel: C2H6 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.8 - 1.3
mk7d.txt Knystautas (1982) [56]
Category: cell size Fuel: C3H8 Sub-Category: width Oxidizer: O2 Initial Pressure: 101.3 kPa Diluent: N2 Initial Temperature: 293 K Equivalence Ratio: 1
at154b.txt Knystautas (1982) [56]
Category: cell size Fuel: C4H10 Sub-Category: width Oxidizer: Air Initial Pressure: 6.7-13.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at152.txt Knystautas (1982) [56]
Category: cell size Fuel: C2H6 Sub-Category: width Oxidizer: O2 Initial Pressure: 4-13.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at153.txt Knystautas (1982) [56]
Category: cell size Fuel: C3H6 Sub-Category: width Oxidizer: O2 Initial Pressure: 4-12 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
at154a.txt Knystautas (1982) [56]
Category: cell size Fuel: C3H8 Sub-Category: width Oxidizer: O2 Initial Pressure: 2.7-13.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1
ja19.txt Knystautas (1998) [57]
Category: cell size Fuel: C6H6 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: H2 Initial Temperature: 293 K Equivalence Ratio: 1
at37.txt Kumar (1990) [61]
Category: cell size Fuel: Deuterium Sub-Category: width Oxidizer: O2 Initial Pressure: 106.6 kPa Diluent: He Initial Temperature: 293 K Equivalence Ratio: 1
at157h.txt Moen (1984) [84]
Category: cell size Fuel: C2H6 Sub-Category: width Oxidizer: Air Initial Pressure: 92.5 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 1.0-1.3
at157k.txt Moen (1984) [84]
Category: cell size Fuel: C3H8 Sub-Category: width Oxidizer: Air Initial Pressure: 92.5 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.75-1.62
mk184d.txt Pedley (1988) [97]
Category: cell size Fuel: N2H4 Sub-Category: width Oxidizer: Initial Pressure: .7-2.6 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio:
mk168a.txt Shepherd (1986) [103]
Category: cell size Fuel: H2S Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.78-1.18
mk168b.txt Shepherd (1986) [103]
Category: cell size Fuel: H2S Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 293 K Equivalence Ratio: 0.78-1.18
at172b.txt Tieszen (1991) [114]
Category: cell size Fuel: n-octane, C8H18 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 373 K Equivalence Ratio: 1
at171b.txt Tieszen (1991) [114]
Category: cell size Fuel: C2H6 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 298-373 K Equivalence Ratio: 1
at172c.txt Tieszen (1991) [114]
Category: cell size Fuel: 1-Octene Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 373 K Equivalence Ratio: 1
at172e.txt Tieszen (1991) [114]
Category: cell size Fuel: 1,7-Octadiene Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 373 K Equivalence Ratio: 1
at172f.txt Tieszen (1991) [114]
Category: cell size Fuel: Octyne Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 373 K Equivalence Ratio: 1
at172g.txt Tieszen (1991) [114]
Category: cell size Fuel: 1,7-Octadiyne Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 373 K Equivalence Ratio: 1
at172h.txt Tieszen (1991) [114]
Category: cell size Fuel: C3H8 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 298, 373 K Equivalence Ratio: 1
at172i.txt Tieszen (1991) [114]
Category: cell size Fuel: C6H14 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 373 K Equivalence Ratio: 1
at172j.txt Tieszen (1991) [114]
Category: cell size Fuel: JP4 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 373 K Equivalence Ratio: 1
at172k.txt Tieszen (1991) [114]
Category: cell size Fuel: C10H22 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 373 K Equivalence Ratio: 1
at170a.txt Tieszen (1991) [114]
Category: cell size Fuel: Hexylnitrate Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 373 K Equivalence Ratio: .4-2
at170b.txt Tieszen (1991) [114]
Category: cell size Fuel: Nitrohexane Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 373 K Equivalence Ratio: 0.7
at170c.txt Tieszen (1991) [114]
Category: cell size Fuel: Nitroethane Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 373 K Equivalence Ratio: .35-1.0
at172l.txt Tieszen (1991) [114]
Category: cell size Fuel: 2,2,4-Trimethylpentane Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 373 K Equivalence Ratio: 1
at172m.txt Tieszen (1991) [114]
Category: cell size Fuel: Cyclooctane, C8H18 Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 373 K Equivalence Ratio: 1
at172n.txt Tieszen (1991) [114]
Category: cell size Fuel: Cis-Cyclooctene Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 373 K Equivalence Ratio: 1
at172o.txt Tieszen (1991) [114]
Category: cell size Fuel: Pentyl Ether Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 373 K Equivalence Ratio: 1
at172p.txt Tieszen (1991) [114]
Category: cell size Fuel: 1,2-Epoxydecane Sub-Category: width Oxidizer: Air Initial Pressure: 101.3 kPa Diluent: Initial Temperature: 373 K Equivalence Ratio: 1
Edited Last: May 27, 2002