Thermal Isomerization of Methylcyclopropane
J. Phys. Chem. A, Vol. 103, No. 3, 1999 363
Apparatus. The high-temperature experiments in this study
were run in a 2.54 cm diameter single-pulse shock tube; the
static reactor used for the lower temperature runs consisted of
a 100 cm3 glass cell surrounded by an aluminum furnace.
Descriptions and operating procedures for these devices have
been reported earlier.4,5 Analyses of reactant and product
samples were carried out on a Varian Model 1440-20 isothermal
gas chromatograph with FID, using a 1.5 m 5% n-octane on
Porasil C column at 43 °C in tandem with a 3 m column of
polypropylene glycol saturated with AgNO3 on 80-100 mesh
Chromosorb W at room temperature. The polypropylene glycol
column was also used alone for the separation of cyclopropane
from propene, needed for the determination of the reaction
temperature.
At the higher temperatures obtained in the shock tube,
however, the fractions of 2-methylpropene and trans-2-butene
increased. The product ratios at the highest temperature were
1.00:0.60:0.54:0.28. Whereas the cis-2-butene to trans-2-butene
ratio was 2.0 or higher at the lower temperatures in both the
previous studies1b,2 and the present investigation, at 1154 K the
amount of trans-2-butene produced approached that of cis-2-
butene, the cis to trans ratio becoming 1.1.
Arrhenius Parameters. Figure 1 shows the Arrhenius plots
for the overall reaction methylcyclopropane f products, and
for isomerization to the individual butenes from 18 shock-tube
experiments and two static reactor runs. Linear least-squares
fits for the data gave the following activation parameters:
for methylcyclopropane f all products:
Kinetic Runs. For the shock-tube runs, 45-75 Torr samples
of the methylcyclopropane-cyclopropane mixtures in argon
were placed in the driven section of the tube, and the samples
were heated for 800 ( 50 µs. The temperatures achieved in
these runs ranged from 990 to 1154 K, as determined from the
extent of conversion of cyclopropane to propene. At the end of
the reaction the product samples were collected in 25 mL glass
bulbs and analyzed chromatographically.
log(A, s-1) ) 15.37 ( 0.07
for methylcyclopropane f 1-butene:
Ea ) 64.4 ( 0.3 kcal/mol
log(A, s-1) ) 15.02 ( 0.11
Ea ) 64.5 ( 0.5 kcal/mol
for methylcyclopropane f cis-2-butene:
For the runs in the static reactor, 343 and 212 Torr sample
mixtures were heated at 695-698 K. The heating times for these
runs were 75 and 85 min, respectively. The temperatures were
measured both directly using an Omega Engineering Model 650-
J-D digital thermometer, and calculated from the extent of
conversion of cyclopropane to propene. Two samples of the
reaction products were collected simultaneously and chromato-
graphed.
log(A, s-1) ) 14.60 ( 0.07
Ea ) 63.3 ( 0.3 kcal/mol
for methylcyclopropane f trans-2-butene:
log(A, s-1) ) 14.75 ( 0.06
Ea ) 64.9 ( 0.3 kcal/mol
for methylcyclopropane f 2-methylpropene:
Calculations. Extents of conversion of methylcyclopropane
to each of the four products, and of cyclopropane to propene,
were determined from the GC peak heights, corrected for
measured sensitivity differences of the various hydrocarbons.
Rate constants were calculated assuming that both methylcy-
clopropane and cyclopropane underwent homogeneous first-
order irreversible reactions.
log(A, s-1) ) 14.81 ( 0.05
Ea ) 66.4 ( 0.2 kcal/mol
The activation energy of 64.4 kcal/mol and the log A value of
15.37 for the overall reaction agree well with values of 65.0
kcal/mol and 15.45 determined by Placzek and Rabinovitch1a
from Chesick’s data at 713-763 K;1b these values are somewhat
higher than those reported by Setser and Rabinovitch,2 62.4 kcal/
mol and 14.61, from their work at 693-748 K.
The reaction temperatures were determined from the calcu-
lated rate constants for the cyclopropane isomerization to
propene and the well-established Arrhenius parameters for this
reaction: Ea ) 65.0 kcal/mol and log(A, s-1) ) 15.2.6
For each experiment, the rate constant for total consumption
of methylcyclopropane was apportioned to rate constants for
isomerization to 1-butene, cis-2-butene, trans-2-butene, and
2-methylpropene by multiplying the overall rate constant by the
fraction of the corresponding component in the product mixture,
following the evidence that these isomerizations are parallel,
first-order reactions.1b
Assuming that most three-membered ring compounds undergo
isomerization via the formation of a diradical intermediate,
Benson and O’Neal have made a priori estimates of the
Arrhenius parameters for these reactions.3 Our experimental
values are in excellent agreement with their estimates of 64.2
kcal/mol for Ea and 15.2 for log A for methylcyclopropane
isomerization to all products. The activation energy of 65.0 kcal/
mol for the cyclopropane to propene isomerization via a diradical
is now well established.6 Substitution of a methyl group for an
H atom on one of the cyclopropane carbons is expected to lower
the strength of the adjacent carbon-carbon bond7 and should
lead to an activation energy slightly lower than 65.0 kcal/mol.
The present work extending the earlier low-temperature study
upward to 1154 K shows that the Arrhenius parameters for the
overall reaction are essentially constant over a wide range of
temperature.
The activation energy for the isomerization of methylcyclo-
propane to trans-2-butene in the present study appears to be
higher by 1.6 ( 0.4 kcal/mol than Ea for the conversion to cis-
2-butene. This difference is significantly smaller than the 4.2
kcal/mol, calculated from Chesick’s data,1b and smaller but
comparable to 2.5 ( 0.8 kcal/mol obtained by Setser and
Rabinovitch,2 in studies done over narrow temperature ranges
of 50 and 40 K. From their thermochemical calculations, O’Neal
and Benson3 predicted an activation energy of 63.0 kcal/mol
Results and Discussion
Product Distribution. In both the shock-tube and the static-
reactor runs, all four isomeric butenes (1-butene, cis-2-butene,
trans-2-butene, and 2-methylpropene) were detected as major
products, with 1-butene most abundant (over 40%) and 2-me-
thylpropene least abundant (about 11%) in the majority of the
runs. At static reactor temperatures the distribution of the
products is quite consistent with those reported by Chesick1b
and by Setser and Rabinovitch.2 For example, their relative rate
constants at 740 K for 1-butene:cis-2-butene:trans-2-butene:2-
methylpropene were 1.00:0.63:0.28:0.161b and 1.00:0.71:0.30:
0.18,2 respectively, while in the present study the relative
amounts of these products at 698 K were found to be
approximately 1.0:0.8:0.4:0.2.