## Abstract The reaction NO + O~3~ → NO~2~ + O~2~ has been studied in a 220‐m^3^ spherical stainless steel reactor under stopped‐flow conditions below 0.1 mtorr total pressure. Under the conditions used, the mixing time of the reactants was negligible compared with the chemical reaction time. The p
Measurement of the rate coefficient of the reaction CH+O2 → products in the temperature range 2200 to 2600 K
✍ Scribed by Michael Röhrig; Eric L. Petersen; David F. Davidson; Ronald K. Hanson; Craig T. Bowman
- Publisher
- John Wiley and Sons
- Year
- 1997
- Tongue
- English
- Weight
- 196 KB
- Volume
- 29
- Category
- Article
- ISSN
- 0538-8066
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✦ Synopsis
The rate coefficient of the reaction was determined by mea-CH ϩ O : products 2 suring CH-radical concentration profiles in shock-heated ethane/ 100-150 ppm 1000 ppm O 2 mixtures in Ar using cw, narrow-linewidth laser absorption at Comparing the 431.131 nm. measured CH concentration profiles to ones calculated using a detailed kinetics model, yielded the following average value for the rate coefficient independent of temperature over the range 2200-2600 K: (13.99 Ϯ 0.12) 3 Ϫ1 Ϫ1 k ϭ 10 cm mol s CHϩO2 The experimental conditions were chosen such that the calculated profiles were sensitive mainly to the reactions and For the methyl CH ϩ O : products CH ϩ M : CH ϩ H ϩ M. 2 3 2 decomposition reaction channel, the following rate-coefficient expression provided the best fit of the measured CH profiles: (16.00 Ϯ 0.12) 3 Ϫ1 Ϫ1 k ϭ 10 exp(Ϫ42900 K/T ) cm mol s CH ϩM: CHϩH ϩM 3 2 Additionally, the rate coefficient of the reaction was determined indi-CH ϩ H : CH ϩ H 2 2 rectly in the same system: 14.15(ϩ0.2,Ϫ0.6) 3 Ϫ1 Ϫ1 k ϭ 10 cm mol s
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