2002
DOI: 10.1002/kin.10063
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Gas‐phase ozonolysis: Rate coefficients for a series of terpenes and rate coefficients and OH yields for 2‐methyl‐2‐butene and 2,3‐dimethyl‐2‐butene

Abstract: The kinetics of the gas-phase reactions of O 3 with a series of selected terpenes has been investigated under flow-tube conditions at a pressure of 100 mbar synthetic air at 295 ± 0.5 K. In the presence of a large excess of m-xylene as an OH radical scavenger, rate coefficients k(O 3 +terpene) were obtained with a relative rate technique, (unit: cm 3 molecule −1 s −1 , errors represent 2σ ): α-pinene: (1.1 ± 0.2) × 10 −16 , 3 -carene: (5.9 ± 1.0) × 10 −17 , limonene: (2.5 ± 0.3) × 10 −16 , myrcene: (4.8 ± 0.6)… Show more

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Cited by 39 publications
(38 citation statements)
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“…Here, the exposure is calculated directly from the measured loss of the gas‐phase reference compound, MB, using the integrated rate law for its reaction with O 3 : where k is the second‐order rate constant for the reaction of O 3 with MB and is 4.1 (±0.5) × 10 −16 cm 3 /molecule/sec. [ Witter et al , 2002]. The slope of the fit to the initial data can then be used to calculate the rate of reaction of methyl oleate, γ MO , as shown previously [ Smith et al , 2002; Katrib et al , 2005]: Here, R is the gas constant, T is the temperature, is the mean speed of O 3 , and V / S A (= d /6) is the volume‐to‐surface area ratio of the particles.…”
Section: Resultsmentioning
confidence: 99%
“…Here, the exposure is calculated directly from the measured loss of the gas‐phase reference compound, MB, using the integrated rate law for its reaction with O 3 : where k is the second‐order rate constant for the reaction of O 3 with MB and is 4.1 (±0.5) × 10 −16 cm 3 /molecule/sec. [ Witter et al , 2002]. The slope of the fit to the initial data can then be used to calculate the rate of reaction of methyl oleate, γ MO , as shown previously [ Smith et al , 2002; Katrib et al , 2005]: Here, R is the gas constant, T is the temperature, is the mean speed of O 3 , and V / S A (= d /6) is the volume‐to‐surface area ratio of the particles.…”
Section: Resultsmentioning
confidence: 99%
“…In the present study, the stated purity of 3-carene was ≥ 98.5% (more details in supplementary), and the impurities at this level would not significantly affect our absolute and relative rates. Witter, et al [19] reported k(O 3 +3-carene) = 5.6 × 10 -17 cm 3 molecule -1 s -1 using relative method in a flow reactor. It is ~50% higher than the other values, for which the reason is unknown.…”
Section: Discussionmentioning
confidence: 99%
“…The needed rate coefficients k 1 − k 4 were taken from the literature (unit: cm 3 molecule −1 s −1 ; TME: tetramethylethylene; MCM: 1-methyl-cyclohexene): k 1,TME = 1.0 × 10 −15 (Witter et al, 2002); k 1,MCH = 1.65 × 10 −16 (Treacy et al, 1997); k 1,α−pinene = 1.1 × 10 −16 and k 1,limonene = 2.5 × 10 −16 (Witter et al, 2002); k 2,TME = 1.1 × 10 −10 (Atkinson, 1986); k 2,MCH = 9.6 × 10 −11 (Darnall et al, 1976); k 2,α−pinene = 5.3 × 10 −11 (Atkinson, 1986); k 2,limonene = 1.6 × 10 −10 ; k 3 = 6.7 × 10 −15 (DeMore et al, 1997) and k 4 = 1.2 × 10 −12 (Zellner, 1978). A diffusion controlled process is assumed for the H 2 SO 4 wall loss in the flow tube, k 5 = 3.65 · D(H 2 SO 4 )/r 2 .…”
Section: Simple Mechanismmentioning
confidence: 99%