Table 8. Neutral chemistry.
| No. | Reaction (rxn) | Rate a | Ref. |
| Two-body collisions | |||
| 312 | He + O(1D) → O + He | 7.0 × 10–22 | 145 b |
| 313 | He + O(1S) → O + He | 7.0 × 10–22 | As rxn 312 |
| 314 | He + O2(a 1Δ) → O2 + He | 8.0 × 10–27 | 146 b |
| 315 | He + O2(b 1Σ) → O2(a 1Δ) + He | 1.0 × 10–23T00.5 | 125 c |
| 316 | 2He* → He + He+ + e | 4.5 × 10–16 | 46 and 97 |
| 317 | 2He* → He2+ + e | 1.05 × 10–15 | 46 and 97 |
| 318 | He* + He2* → 2He + He+ + e | 5.0 × 10–16 | 97 d |
| 319 | He* + He2* → He + He2+ + e | 2.0 × 10–15 | 97 d |
| 320 | He* + OH → OH+ + He + e | 6.08 × 10–16 | As rxn 321 |
| 321 | He* + H2O → He + H2O+ + e | 6.08 × 10–16 | 147 e |
| 322 | He* + H2O → He + OH+ + H + e | 1.39 × 10–16 | 147 e |
| 323 | He* + H2O2 → He + OH+ + OH + e | 6.08 × 10–16 | As rxn 321 |
| 324 | He* + O → O+ + He + e | 2.54 × 10–16 | As rxn 327 |
| 325 | He* + O(1D) → O+ + He + e | 2.54 × 10–16 | As rxn 327 |
| 326 | He* + O(1S) → O+ + He + e | 2.54 × 10–16 | As rxn 327 |
| 327 | He* + O2 → O2+ + He + e | 2.54 × 10–16 | 148 |
| 328 | He* + O2(a 1Δ) → O2+ + He + e | 2.54 × 10–16 | As rxn 327 |
| 329 | He* + O2(b 1Σ) → O2+ + He + e | 2.54 × 10–16 | As rxn 327 |
| 330 | He* + O3 → O2+ + O + He + e | 2.6 × 10–16 | 74 c |
| 331 | He2* + H2O → 2He + H2O+ + e | 2.2 × 10–15 | 149 |
| 332 | He2* + O → O+ + 2He + e | 3.6 × 10–16 | As rxn 335 |
| 333 | He2* + O(1D) → O+ + 2He + e | 3.6 × 10–16 | As rxn 335 |
| 334 | He2* + O(1S) → O+ + 2He + e | 3.6 × 10–16 | As rxn 335 |
| 335 | He2* + O2 → O2+ + 2He + e | 3.6 × 10–16 | 149 |
| 336 | He2* + O2(a 1Δ) → O2+ + 2He + e | 3.6 × 10–16 | As rxn 335 |
| 337 | He2* + O2(b 1Σ) → O2+ + 2He + e | 3.6 × 10–16 | As rxn 335 |
| 338 | He2* + O3 → O2+ + O + 2He + e | 3.6 × 10–16 | 74 c |
| 339 | H + HO2 → H2 + O2 | 5.6 × 10–18 | 88 |
| 340 | H + HO2 → 2OH | 7.2 × 10–17 | 88 |
| 341 | H + HO2 → H2O + O | 2.4 × 10–18 | 88 |
| 342 | H + H2O2 → H2O + OH | 1.7 × 10–17e–1800/Tg | 150 |
| 343 | H + H2O2 → H2 + HO2 | 2.8 × 10–18e–1890/Tg | 150 |
| 344 | H + O3 → OH + O2 | 1.4 × 10–16e–470/Tg | 151 and 152 |
| 345 | H2 + OH → H2O + H | 4.27 × 10–19T02.41e–1240/Tg | 153 |
| 346 | H2 + O(1D) → OH + H | 1.2 × 10–16 | 88 |
| 347 | H2 + O(1S) → OH + H | 1.2 × 10–16 | As rxn 346 |
| 348 | 2OH → H2O + O | 6.2 × 10–20T02.6e945/Tg | 88 |
| 349 | OH + HO2 → O2 + H2O | 4.8 × 10–17e250/Tg | 88, 154 and 155 |
| 350 | OH + H2O2 → HO2 + H2O | 2.9 × 10–18e–160/Tg | 88 |
| 351 | OH + O → H + O2 | 2.4 × 10–17e110/Tg | 88, 156 and 157 |
| 352 | OH + O(1D) → O2 + H | 2.4 × 10–17e110/Tg | As rxn 351 |
| 353 | OH + O(1S) → O2 + H | 2.4 × 10–17e110/Tg | As rxn 351 |
| 354 | OH + O3 → O2 + HO2 | 1.7 × 10–18e–940/Tg | 88 |
| 355 | H2O + O(1D) → 2OH | 1.63 × 10–16e60/Tg | 151 |
| 356 | H2O + O(1S) → O + H2O | 4.5 × 10–17 | 158 |
| 357 | H2O + O(1S) → O(1D) + H2O | 1.5 × 10–16 | 158 |
| 358 | H2O + O(1S) → 2OH | 3.05 × 10–16 | 158 |
| 359 | H2O + O2(a 1Δ) → O2 + H2O | 4.8 × 10–24 | 151 |
| 360 | H2O + O2(b 1Σ) → O2 + H2O | 3.9 × 10–18e125/Tg | 151 |
| 361 | HO2 + O → OH + O2 | 2.7 × 10–17e224/Tg | 88 and 155 |
| 362 | HO2 + O(1D) → OH + O2 | 5.2 × 10–16 | As rxn 364 |
| 363 | HO2 + O(1S) → OH + O2 | 5.2 × 10–16 | As rxn 364 |
| 364 | H2O2 + O(1D) → H2O + O2 | 5.2 × 10–16 | 159 |
| 365 | H2O2 + O(1S) → H2O + O2 | 5.2 × 10–16 | As rxn 364 |
| 366 | O + O(1D) → 2O | 8.0 × 10–18 | 160 |
| 367 | O + O(1S) → 2O | 3.33 × 10–17e–300/Tg | 125 and 161 d |
| 368 | O + O(1S) → O(1D) + O | 1.67 × 10–17e–300/Tg | 125 and 161 d |
| 369 | O(1D) + O2 → O + O2 | 6.4 × 10–18 | 88 |
| 370 | O(1D) + O2 → O + O2(b 1Σ) | 2.56 × 10–17 | 88 |
| 371 | O(1D) + O3 → 2O2 | 1.2 × 10–16 | 88 |
| 372 | O(1D) + O3 → O2 + 2O | 1.2 × 10–16 | 88 |
| 373 | O(1S) + O3 → 2O2 | 1.2 × 10–16 | As rxn 371 |
| 374 | O(1S) + O3 → O2 + 2O | 1.2 × 10–16 | As rxn 372 |
| 375 | O2 + O2(a 1Δ) → 2O2 | 3.0 × 10–24e–200/Tg | 88 |
| 376 | O2 + O2(b 1Σ) → O2 + O2(a 1Δ) | 3.6 × 10–23T00.5 | 125 |
| 377 | 2O2(a 1Δ) → O2(b 1Σ) + O2 | 1.8 × 10–24T03.8e700/Tg | 162 and 163 |
| 378 | O2(a 1Δ) + O3 → O + 2O2 | 5.2 × 10–17e–2840/Tg | 151 |
| 379 | O2(b 1Σ) + O3 → O + 2O2 | 3.5 × 10–17e–135/Tg | 151 |
| Three-body collisions | |||
| 380 | 2He + He* → He + He2* | 2.0 × 10–46 | 164 |
| 381 | He + He* + H2O → H2O+ + 2He + e | 1.48 × 10–41 | 147 e |
| 382 | He + He* + O → O+ + 2He + e | 8.2 × 10–42 | As rxn 385 |
| 383 | He + He* + O2 → O2+ + 2He + e | 8.2 × 10–42 | 165 |
| 384 | He + H + H → H2 + He | 6.04 × 10–45T0–1.0 | 150 and 152 f |
| 385 | He + H + OH → H2O + He | 9.23 × 10–44T0–1.527e–185/Tg | 166 g |
| 386 | He + H + O → OH + He | 4.36 × 10–44T0–1.0 | 167 c |
| 387 | (He+) H + O2 → HO2 (+He) | Effective | 88 h , i |
| 388 | (He+) 2OH → H2O2 (+He) | Effective | 88 h , j |
| 389 | He + 2O → O2 + He | 3.99 × 10–47e900/Tg | 167 k |
| 390 | He + O + O2 → O3 + He | 3.66 × 10–46T0–2.6 | 88 l |
aIn m3 s–1 and m6 s–1 for two- and three-body collisions, respectively.
bValue in an upper limit in reference.
cEstimated value in reference.
dEstimated branching ratio.
eBranching ratios taken from Sanders.168
fThird body is Ar instead of He in reference. The gas efficiency factor is assumed to be 1.
gThird body is Ar instead of He in reference. The gas efficiency factor is assumed to be 0.65. This factor is calculated by dividing reaction rate coefficients for He and Ar as background gases for the same reaction measured by Zellner et al.169
hEffective rate coefficients calculated from pressure dependent rates for 1 atm and fitted by an Arrhenius expression in the temperature range 280–350 K.
iThird body is N2 instead of He in reference. The gas efficiency factor is assumed to be 0.43. This factor is calculated by dividing reaction rate coefficients for He and N2 as background gases for the same reaction measured by Hsu et al.170
jRecommended rate coefficient in reference is for N2 background gas instead of He. We apply a gas efficiency factor of 0.41 to the low-pressure limit reaction rate coefficient to account for this. This factor is calculated by dividing the room temperature rate coefficient from the given reference for He background gas (measured by Forster et al.171) by the recommended value (measured by Fulle et al.172).
kThird body is Ar instead of He in reference. The gas efficiency factor is assumed to be 0.77. This factor is calculated by dividing reaction rate coefficients for He and Ar as background gases for the same reaction measured by Campbell and Thrush.169
lThird body is N2 instead of He in reference. The gas efficiency factor is assumed to be 0.61. This factor is calculated by dividing reaction rate coefficients for He and N2 as background gases for the same reaction measured by Lin and Leu.173