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Absolute rate constant for the reaction of Phenyl radical with Acetylene
Author(s) -
Yu T.,
Lin M. C.,
Melius C. F.
Publication year - 1994
Publication title -
international journal of chemical kinetics
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.341
H-Index - 68
eISSN - 1097-4601
pISSN - 0538-8066
DOI - 10.1002/kin.550261105
Subject(s) - chemistry , reaction rate constant , acetylene , torr , kinetic energy , atmospheric pressure , total pressure , adduct , atmospheric temperature range , analytical chemistry (journal) , thermodynamics , computational chemistry , kinetics , organic chemistry , physics , oceanography , quantum mechanics , geology
The absolute rate constant for the reaction of phenyl radical with acetylene has been measured at 20 torr total pressure in the temperature range of 297 to 523 K using the cavity‐ring‐down technique. These new kinetic data could be quantitatively correlated with the data obtained earlier with a relative rate method under low‐pressure (10 −3 –10 −2 torr) and high‐temperature (1000–1330 K) conditions. These kinetic data were analyzed in terms of the RRKM theory employing the thermochemical and molecular structure data computed with the BAC‐MP4 technique. The calculated results reveal that the total rate constant for the C 6 H 5 + C 2 H 2 reaction ( k t ) is pressure‐independent, whereas those for the formation of C 6 H 5 C 2 H ( k b ) and the C 6 H 5 C 2 H 2 adduct ( k c ) are strongly pressure‐dependent. A least‐squares analysis of the calculated values for 300–2000 K at the atmospheric pressure of N 2 or Ar can be given by\documentclass{article}\pagestyle{empty}\begin{document}$$ k_b = 9.5 \times {\rm 10}^{{\rm - 42}} T^{9.33} \exp \left({- 1,713/T} \right) $$\end{document}\documentclass{article}\pagestyle{empty}\begin{document}$$ k_C = 1.8 \times {\rm 10}^{{\rm - 7}} T^{-1.63} \exp \left({- 2,711/T} \right) $$\end{document}and\documentclass{article}\pagestyle{empty}\begin{document}$$ k_t = 4.1 \times {\rm 10}^{{\rm - 18}} T^{1.77} \exp \left({- 1,152/T} \right) $$\end{document}all in units of cm 3 /s. The latter equation effectively represents the two sets of experimental data. © 1994 John Wiley & Sons, Inc.

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