Active Parameters - Foundational Fuel Chemistry Model 1.0
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Active parameters are selected from uncertainty impact ranking as follows.
| Number | Reaction | Uncertainty Factor f |
| 1 | H+O2<=>O+OH | 1.15 |
| 2 | O+H2<=>H+OH (low T) | 1.6 |
| 3 | O+H2<=>H+OH (high T) | 1.6 |
| 4 | OH+H2<=>H+H2O | 1.2 |
| 5 | 2OH<=>O+H2O | 1.4 |
| 6 | H2+M<=>2H+M(N2) | 3 |
| 6 | H2+M<=>2H+M(H2) | 3 |
| 6 | H2+M<=>2H+M(H2O) | 3 |
| 6 | H2+M<=>2H+M(CO) | 3 |
| 6 | H2+M<=>2H+M(CO2) | 3 |
| 7 | H2+AR<=>2H+AR | 2 |
| 12 | O+H+M<=>OH+M(N2) | 5 |
| 12 | O+H+M<=>OH+M(H2O) | 5 |
| 12 | O+H+M<=>OH+M(CO) | 5 |
| 12 | O+H+M<=>OH+M(CO2) | 5 |
| 13 | H2O+M<=>H+OH+M(AR) | 3.2 |
| 13 | H2O+M<=>H+OH+M(HE) | 3.2 |
| 13 | H2O+M<=>H+OH+M(N2) | 3.2 |
| 13 | H2O+M<=>H+OH+M(H2) | 3.2 |
| 13 | H2O+M<=>H+OH+M(CO) | 3.2 |
| 13 | H2O+M<=>H+OH+M(CO2) | 3.2 |
| 14 | 2H2O<=>H+OH+H2O | 3.2 |
| 15 | H+O2(+M)<=>HO2(+M) (k∞) | 2 |
| 15 | H+O2(+M)<=>HO2(+M)(AR) | 2 |
| 15 | H+O2(+M)<=>HO2(+M)(HE) | 2 |
| 15 | H+O2(+M)<=>HO2(+M)(N2) | 2 |
| 15 | H+O2(+M)<=>HO2(+M)(H2) | 2 |
| 15 | H+O2(+M)<=>HO2(+M)(O2) | 2 |
| 15 | H+O2(+M)<=>HO2(+M)(H2O) | 2 |
| 15 | H+O2(+M)<=>HO2(+M)(CO) | 2 |
| 15 | H+O2(+M)<=>HO2(+M)(CO2) | 2 |
| 16 | HO2+H<=>H2+O2 | 2 |
| 17 | HO2+H<=>2OH | 2 |
| 18 | HO2+H<=>O+H2O | 3 |
| 19 | HO2+O<=>OH+O2 | 3 |
| 20 | HO2+OH<=>H2O+O2 | 1.6 |
| 21 | HO2+OH<=>H2O+O2 | 1.35 |
| 22 | 2HO2<=>H2O2+O2 | 1.5 |
| 23 | 2HO2<=>H2O2+O2 | 2 |
| 24 | H2O2(+M)<=>2OH(+M) (k∞) | 2.5 |
| 24 | H2O2(+M)<=>2OH(+M)(AR) | 2.5 |
| 24 | H2O2(+M)<=>2OH(+M)(N2) | 2.5 |
| 24 | H2O2(+M)<=>2OH(+M)(H2) | 2.5 |
| 24 | H2O2(+M)<=>2OH(+M)(H2O) | 2.5 |
| 24 | H2O2(+M)<=>2OH(+M)(H2O2) | 2.5 |
| 24 | H2O2(+M)<=>2OH(+M)(CH2O) | 2.5 |
| 25 | H2O2+H<=>OH+H2O | 2 |
| 26 | H2O2+H<=>HO2+H2 | 2 |
| 27 | H2O2+O<=>OH+HO2 | 3 |
| 28 | H2O2+OH<=>H2O+HO2 | 2 |
| 29 | H2O2+OH<=>H2O+HO2 | 1.3 |
| 30 | CO+O(+M)<=>CO2(+M) (k∞) | 10 |
| 31 | CO+O2<=>O+CO2 | 10 |
| 32 | CO+OH<=>H+CO2 (high T) | 1.2 |
| 33 | CO+OH<=>H+CO2 (low T) | 1.5 |
| 35 | HCO+M<=>H+CO+M(AR) | 1.7 |
| 35 | HCO+M<=>H+CO+M(HE) | 1.7 |
| 35 | HCO+M<=>H+CO+M(N2) | 1.7 |
| 35 | HCO+M<=>H+CO+M(H2) | 1.7 |
| 35 | HCO+M<=>H+CO+M(O2) | 1.7 |
| 35 | HCO+M<=>H+CO+M(H2O) | 1.7 |
| 35 | HCO+M<=>H+CO+M(CO) | 1.7 |
| 35 | HCO+M<=>H+CO+M(CH4) | 1.7 |
| 35 | HCO+M<=>H+CO+M(CH2O) | 1.7 |
| 36 | HCO+H<=>H2+CO | 2.5 |
| 38 | HCO+O<=>H+CO2 | 2 |
| 39 | HCO+OH<=>H2O+CO | 2 |
| 40 | HCO+O2<=>HO2+CO | 2 |
| 43 | CH+H<=>C+H2 | 1.5 |
| 46 | CH+H2<=>H+CH2 | 3 |
| 47 | CH+H2(+M)<=>CH3(+M)(AR) | 2 |
| 50 | CH+O2<=>CO2+H | 1.6 |
| 51 | CH+O2<=>CO+OH | 1.6 |
| 52 | CH+O2=>O+H+CO | 1.6 |
| 57 | CH2+OH<=>H+CH2O | 3 |
| 60 | CH2+H2<=>H+CH3 | 9 |
| 61 | CH2+O2=>OH+H+CO | 2 |
| 62 | CH2+O2=>2H+CO2 | 2 |
| 63 | CH2+O2<=>O+CH2O | 2 |
| 64 | CH2+O2<=>H2+CO2 | 2 |
| 76 | CH2(S)+H2<=>CH3+H | 2 |
| 85 | HCO+H(+M)<=>CH2O(+M) (k∞) | 3 |
| 85 | HCO+H(+M)<=>CH2O(+M)(AR) | 3 |
| 85 | HCO+H(+M)<=>CH2O(+M)(CH2O) | 3 |
| 86 | CH2O(+M)<=>H2+CO(+M)(AR) | 2.5 |
| 87 | CH2O+H<=>HCO+H2 | 2 |
| 88 | CH2O+O<=>OH+HCO | 1.6 |
| 89 | CH2O+OH<=>HCO+H2O | 2 |
| 90 | CH2O+O2<=>HO2+HCO | 3 |
| 91 | CH2O+HO2<=>HCO+H2O2 | 3 |
| 97 | CH3+H(+M)<=>CH4(+M) (k∞) | 2 |
| 97 | CH3+H(+M)<=>CH4(+M)(AR) | 3 |
| 97 | CH3+H(+M)<=>CH4(+M)(HE) | 3 |
| 97 | CH3+H(+M)<=>CH4(+M)(N2) | 3 |
| 97 | CH3+H(+M)<=>CH4(+M)(O2) | 3 |
| 97 | CH3+H(+M)<=>CH4(+M)(H2O) | 3 |
| 97 | CH3+H(+M)<=>CH4(+M)(CO) | 3 |
| 98 | CH3+O<=>H+CH2O | 1.4 |
| 99 | CH3+O=>H+H2+CO | 1.4 |
| 101 | CH3+OH<=>CH2+H2O | 2 |
| 102 | CH3+OH<=>CH2(S)+H2O | 3 |
| 103 | CH3+OH<=>H2+CH2O | 3 |
| 104 | CH3+HO2<=>O2+CH4 | 3 |
| 105 | CH3+HO2<=>OH+CH3O | 3 |
| 106 | CH3+O2<=>O+CH3O | 2 |
| 107 | CH3+O2<=>OH+CH2O | 3 |
| 109 | CH3+CH<=>H+C2H3 | 10 |
| 110 | CH3+CH2<=>H+C2H4 | 3 |
| 112 | 2CH3(+M)<=>C2H6(+M) (k∞) | 2 |
| 112 | 2CH3(+M)<=>C2H6(+M)(AR) | 2 |
| 112 | 2CH3(+M)<=>C2H6(+M)(O2) | 2 |
| 112 | 2CH3(+M)<=>C2H6(+M)(CH4) | 2 |
| 113 | 2CH3<=>H+C2H5 | 2 |
| 115 | CH3+CH2O<=>HCO+CH4 | 2 |
| 127 | CH2OH(+M)<=>H+CH2O(+M)(AR) | 2 |
| 127 | CH2OH(+M)<=>H+CH2O(+M)(H2O) | 2 |
| 130 | CH2OH+H<=>OH+CH3 | 2.5 |
| 134 | CH2OH+O2<=>HO2+CH2O | 2 |
| 136 | CH4+H<=>CH3+H2 | 1.5 |
| 137 | CH4+O<=>OH+CH3 | 1.4 |
| 138 | CH4+OH<=>CH3+H2O | 1.2 |
| 139 | CH4+HO2<=>CH3+H2O2 | 2.5 |
| 141 | CH4+CH2<=>2CH3 | 2 |
| 142 | CH4+CH2(S)<=>2CH3 | 1.4 |
| 172 | HCCO+O2<=>OH+2CO | 5 |
| 176 | C2H2(+M)<=>H2CC(+M)(AR) | 3 |
| 178 | C2H2+O<=>H+HCCO | 2 |
| 179 | C2H2+O<=>CO+CH2 | 3.2 |
| 185 | H2CC+O2<=>2HCO | 5 |
| 188 | CH2CO+H<=>CH3+CO | 3 |
| 199 | C2H3+H<=>H2CC+H2 | 4 |
| 204 | C2H3+O2<=>HCO+CH2O | 2 |
| 205 | C2H3+O2<=>CH2CHO+O | 3 |
| 237 | C2H4(+M)<=>H2+H2CC(+M) (k∞) | 2 |
| 237 | C2H4(+M)<=>H2+H2CC(+M)(AR) | 2 |
| 237 | C2H4(+M)<=>H2+H2CC(+M)(CH4) | 2 |
| 238 | C2H4+H(+M)<=>C2H5(+M) (k∞) | 2 |
| 238 | C2H4+H(+M)<=>C2H5(+M)(N2) | 2 |
| 238 | C2H4+H(+M)<=>C2H5(+M)(H2O) | 2 |
| 239 | C2H4+H<=>C2H3+H2 | 2.5 |
| 240 | C2H4+O<=>CH3+HCO | 2 |
| 243 | C2H4+OH<=>C2H3+H2O | 2 |
| 249 | C2H5+H(+M)<=>C2H6(+M)(AR) | 2 |
| 254 | C2H5+O2<=>HO2+C2H4 | 2 |
| 258 | C2H6+H<=>C2H5+H2 | 1.4 |
| 259 | C2H6+O<=>OH+C2H5 | 2 |
| 260 | C2H6+OH<=>C2H5+H2O | 1.6 |
| 261 | C2H6+CH<=>CH3+C2H4 | 3 |
| 264 | C2H6+CH3<=>C2H5+CH4 | 1.5 |
| 999 | flw_1a [OH]0 (nominal: 100 ppm) | 10 |
| 999 | flw_2a [OH]0 (nominal: 100 ppm) | 10 |
| 999 | flw_3a [OH]0 (nominal: 10 ppm) | 2 |
| 999 | flw_4a [OH]0 (nominal: 40 ppm) | 10 |
Special treatment is required for unimolecular reactions. In active parameter analysis, absolute low-pressure limit reaction rates with each collider was assumed to have the same uncertainty factor as the base rate coefficient (usually with N2 or Ar). In the optimization, however, third-body efficiencies relative to the base collider are considered as independent variables within a reasonable range. For the H+O2+M reaction, th ranges of relative third-body efficiencies are (expressed in the nomalized rate variable) He: ±0.3; Ar: ±0.2; O2: ±0.3; H2O: ±7; CO2: ±1.4; H2: ±1. For other, generic relative efficiencies, the ranges are: Ar, He: -0.2/+0.3; O2: ±0.2; CO: ±0.5; H2O ±3; CH4, CO2: ±1; H2: ±30%. Uncertainty factors of third body efficiencies are obtained by averaging the upper and lower bounds mentioned above.
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