Abstract
HCFC-133a (l-chloro-2,2,2-trifluoroethane) was thermally chlorinated in an integral reactor under atmospheric pressure in a temperature range between 573 and 723 K. From the analysis of the data it was confirmed that the reaction was a two-step series-parallel reaction and each step was a second-order reaction. The ratio of the second-step rate constant to the first-step rate constant did not change with temperature and its value was 1.13. The activation energy was 106 kJ/g-mol. These results indicate that the product distribution is the sole function of conversion of HCFC-133a.
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Abbreviations
- A:
-
HCFC-133a
- B:
-
Cl2
- C i :
-
concentration of component i (i=A, B, R or S)
- C to :
-
concentration of component i at. reactor inlet [kg-mol/m3]
- E:
-
activation energy [kJ/g-mol]
- {F}inAo :
-
molar feed rate of A [kg-mol/s]
- F(X A :
-
function of {X}inA defined by Eq. (16)
- k1, k2 :
-
rate constants [m3/kg-mol·s]
- R:
-
HCFC-123, or gas law constant
- ri :
-
reaction rate for compound i [kg-mol/m3·s]
- S:
-
CFC-113a
- SR :
-
selectivity of R
- t:
-
time [s]
- V:
-
volume of reactor [m3]
- v :
-
volumetric feed rate [m3/s]
- X A :
-
conversion of A [-]
- α:
-
k2/k1 [-]
- τ:
-
space time ( = V/v) [s]
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Yoon, K.J., Shim, G.I., Park, K.Y. et al. A kinetic study on thermal chlorination of l-chloro-2,2,2-trifluoroethane. Korean J. Chem. Eng. 10, 220–225 (1993). https://doi.org/10.1007/BF02705271
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DOI: https://doi.org/10.1007/BF02705271