Department of Chemistry and Biochemistry, Florida International University, Miami, Florida 33199, USA.
J Phys Chem A. 2010 Jul 29;114(29):7682-92. doi: 10.1021/jp911604f.
Ab initio G3(MP2,CC)//B3LYP/6-311G** calculations have been performed to investigate the potential energy surface and mechanism of the reaction of phenyl radical with 1,2-butadiene followed by kinetic RRKM-ME calculations of the reaction rate constants and product branching ratios at various temperatures and pressures. The results show that the reaction can proceed by direct hydrogen abstraction to produce benzene and C(4)H(5) radicals or by addition of phenyl to different carbon atoms in CH(2)CCHCH(3) followed by isomerizations of C(10)H(11) adducts and their dissociation by H or CH(3) losses. The H abstraction channels are found to be kinetically preferable and to contribute 70-90% to the total product yield in the 300-2500 K temperature range, with the products including C(6)H(6) + CH(2)CHCCH(2) (approximately 40%), C(6)H(6) + CH(3)CHCCH (5-31%), and C(6)H(6) + CH(2)CCCH(3) (24-20%). The phenyl addition channels are calculated to be responsible for 10-30% of the total product yield, with their contribution decreasing as the temperature increases. The products of the addition channels include collisionally stabilized C(10)H(11) adducts, 1-phenyl-2-buten-2-yl, 3-phenyl-2-buten-2-yl, and 2-phenyl-2-buten-1-yl/2-phenyl-1-buten-3-yl, which are favored under low temperatures, as well as their dissociation products, 1-phenyl-propyne + CH(3), phenylallene + CH(3), and 2-phenyl-1,3-butadiene + H, preferred at higher temperatures. Indene is predicted to be a very minor reaction product at the temperatures relevant to combustion, with the maximal calculated yield of only 2% at 700 K and 7.6 Torr. Our calculations showed that at typical combustion temperatures product branching ratios are practically independent of pressure, and collisional stabilization of reaction intermediates does not play a significant role. Three-parameter modified Arrhenius expressions have been generated for the total reaction rate constants and rate constants for the most important product channels, which can be utilized in future kinetic modeling of reaction networks related to the growth of hydrocarbons in combustion processes.
已通过从头算 G3(MP2,CC)//B3LYP/6-311G** 计算研究了苯基自由基与 1,2-丁二烯反应的势能面和反应机理,并在不同温度和压力下进行了反应速率常数和产物分支比的 RRKM-ME 动力学计算。结果表明,该反应可以通过直接氢提取生成苯和 C(4)H(5)自由基,或者通过苯基加成到 CH(2)CCHCH(3)中的不同碳原子上,然后通过 C(10)H(11)加合物的异构化及其通过 H 或 CH(3)损失的解离来进行。氢提取通道被发现是动力学上有利的,在 300-2500 K 的温度范围内,对总产物产率的贡献为 70-90%,产物包括 C(6)H(6) + CH(2)CHCCH(2)(约 40%)、C(6)H(6) + CH(3)CHCCH(5-31%)和 C(6)H(6) + CH(2)CCCH(3)(24-20%)。苯基加成通道被计算负责总产物产率的 10-30%,随着温度的升高,其贡献减小。加成通道的产物包括碰撞稳定的 C(10)H(11)加合物、1-苯基-2-丁烯-2-基、3-苯基-2-丁烯-2-基和 2-苯基-2-丁烯-1-基/2-苯基-1-丁烯-3-基,它们在低温下是有利的,以及它们的解离产物 1-苯基丙炔+CH(3)、苯基丙二烯+CH(3)和 2-苯基-1,3-丁二烯+H,在较高温度下是有利的。茚被预测为在与燃烧相关的温度下是一种非常次要的反应产物,在 700 K 和 7.6 Torr 时最大计算产率仅为 2%。我们的计算表明,在典型的燃烧温度下,产物分支比实际上与压力无关,反应中间体的碰撞稳定化没有起到重要作用。已生成了用于总反应速率常数和最重要产物通道的速率常数的三参数修正 Arrhenius 表达式,可用于未来与燃烧过程中烃类增长相关的反应网络的动力学建模。