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Cell Length
at193a.txt Aminallah (1993) [3]
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Category: | cell size | Fuel: | CH4 |
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Sub-Category: | length | Oxidizer: | O2 |
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Initial Pressure: | 120 kPa | Diluent: | |
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Initial Temperature: | 293 K | Equivalence Ratio: | 0.7-1.3 |
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at194a.txt Bauer (1985) [9]
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Category: | cell size | Fuel: | C3H8 |
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Sub-Category: | length | Oxidizer: | O2 |
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Initial Pressure: | 101.3 kPa | Diluent: | |
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Initial Temperature: | 293 K | Equivalence Ratio: | |
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at194b.txt Bull (1982) [25]
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Category: | cell size | Fuel: | C3H8 |
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Sub-Category: | length | Oxidizer: | O2 |
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Initial Pressure: | 101.3 kPa | Diluent: | |
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Initial Temperature: | 293 K | Equivalence Ratio: | |
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at93a.txt Bull (1982) [20]
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Category: | cell size | Fuel: | C2H6 |
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Sub-Category: | length | Oxidizer: | O2 |
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Initial Pressure: | 33.8 kPa | Diluent: | N2 |
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Initial Temperature: | 293 K | Equivalence Ratio: | 0.5-2 |
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at93b.txt Bull (1982) [20]
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Category: | cell size | Fuel: | C2H6 |
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Sub-Category: | length | Oxidizer: | O2 |
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Initial Pressure: | 67.5 kPa | Diluent: | N2 |
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Initial Temperature: | 293 K | Equivalence Ratio: | 0.5-2 |
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mk2.txt Bull (1982) [25]
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Category: | cell size | Fuel: | H2 |
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Sub-Category: | length | Oxidizer: | Air |
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Initial Pressure: | 8.1 - 101.3 kPa | Diluent: | |
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Initial Temperature: | 293 K | Equivalence Ratio: | 1 |
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at139a.txt Bull (1982) [25]
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Category: | cell size | Fuel: | C2H6 |
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Sub-Category: | length | Oxidizer: | O2 |
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Initial Pressure: | 3-30 kPa | Diluent: | |
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Initial Temperature: | 293 K | Equivalence Ratio: | 1 |
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at139e.txt Bull (1982) [25]
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Category: | cell size | Fuel: | C2H6 |
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Sub-Category: | length | Oxidizer: | Air |
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Initial Pressure: | 60.8-101.3 kPa | Diluent: | |
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Initial Temperature: | 293 K | Equivalence Ratio: | 1 |
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at139b.txt Bull (1982) [25]
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Category: | cell size | Fuel: | C2H6 |
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Sub-Category: | length | Oxidizer: | O2 |
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Initial Pressure: | 10-40.5 kPa | Diluent: | N2 |
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Initial Temperature: | 293 K | Equivalence Ratio: | 1 |
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at139c.txt Bull (1982) [25]
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Category: | cell size | Fuel: | C2H6 |
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Sub-Category: | length | Oxidizer: | O2 |
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Initial Pressure: | 10-40.5 kPa | Diluent: | N2 |
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Initial Temperature: | 293 K | Equivalence Ratio: | 1 |
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at139d.txt Bull (1982) [25]
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Category: | cell size | Fuel: | C2H6 |
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Sub-Category: | length | Oxidizer: | O2 |
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Initial Pressure: | 40.5 kPa | Diluent: | N2 |
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Initial Temperature: | 293 K | Equivalence Ratio: | 1 |
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at140a.txt Bull (1982) [25]
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Category: | cell size | Fuel: | C2H2 |
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Sub-Category: | length | Oxidizer: | Air |
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Initial Pressure: | 8.1-101.3 kPa | Diluent: | |
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Initial Temperature: | 293 K | Equivalence Ratio: | 1 |
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at140b.txt Bull (1982) [25]
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Category: | cell size | Fuel: | C2H4 |
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Sub-Category: | length | Oxidizer: | Air |
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Initial Pressure: | 30.4-101.3 kPa | Diluent: | |
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Initial Temperature: | 293 K | Equivalence Ratio: | 1 |
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at189.txt Lefebvre (1993) [60]
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Category: | cell size | Fuel: | H2 |
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Sub-Category: | length | Oxidizer: | O2 |
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Initial Pressure: | 26.7 kPa | Diluent: | Ar+CF3H |
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Initial Temperature: | 293 K | Equivalence Ratio: | 1 |
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at169e.txt Libouton (1975) [61]
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Category: | cell size | Fuel: | 18.46CO+H2 |
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Sub-Category: | length | Oxidizer: | O2 |
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Initial Pressure: | 22.7-33.3 kPa | Diluent: | 11.88Ar+CF3Br |
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Initial Temperature: | 293 K | Equivalence Ratio: | 1 |
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at169a.txt Libouton (1975) [61]
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Category: | cell size | Fuel: | 18.46CO+H2 |
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Sub-Category: | length | Oxidizer: | O2 |
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Initial Pressure: | 4.7-40 kPa | Diluent: | Ar |
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Initial Temperature: | 293 K | Equivalence Ratio: | 1 |
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at169d.txt Libouton (1975) [61]
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Category: | cell size | Fuel: | 18.46CO+H2 |
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Sub-Category: | length | Oxidizer: | O2 |
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Initial Pressure: | 13.3-40 kPa | Diluent: | 11.88Ar+CFCl3 |
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Initial Temperature: | 293 K | Equivalence Ratio: | 1 |
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at169c.txt Libouton (1975) [61]
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Category: | cell size | Fuel: | 18.46CO+H2 |
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Sub-Category: | length | Oxidizer: | O2 |
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Initial Pressure: | 8-33.3 kPa | Diluent: | 11.88Ar+CF2Cl2 |
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Initial Temperature: | 293 K | Equivalence Ratio: | 1 |
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at169b.txt Libouton (1975) [61]
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Category: | cell size | Fuel: | 18.46CO+H2 |
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Sub-Category: | length | Oxidizer: | O2 |
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Initial Pressure: | 9.3-26.7 kPa | Diluent: | 11.88Ar+CF3Cl |
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Initial Temperature: | 293 K | Equivalence Ratio: | 1 |
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at70a.txt Nzeyimana (1991) [80]
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Category: | cell size | Fuel: | H2 |
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Sub-Category: | length | Oxidizer: | O2 |
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Initial Pressure: | 26.7 kPa | Diluent: | Ar+CF4 |
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Initial Temperature: | 293 K | Equivalence Ratio: | 0.8 |
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at70b.txt Nzeyimana (1991) [80]
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Category: | cell size | Fuel: | H2 |
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Sub-Category: | length | Oxidizer: | O2 |
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Initial Pressure: | 26.7 kPa | Diluent: | Ar+CF4 |
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Initial Temperature: | 293 K | Equivalence Ratio: | 1 |
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at70c.txt Nzeyimana (1991) [80]
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Category: | cell size | Fuel: | H2 |
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Sub-Category: | length | Oxidizer: | O2 |
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Initial Pressure: | 26.7 kPa | Diluent: | Ar+CF4 |
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Initial Temperature: | 293 K | Equivalence Ratio: | 1.2 |
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mikek@galcit.caltech.edu
