The gas phase hydrodechlorination of chlorobenzene over the temperature range 473 K O T O 573 K has been studied using a 1.5% (w/w) catalyst. Reproducible turnover fre-Ni/SiO 2 quencies are quoted and the eΓΎ ects of varying such process variables as reaction time and temperature, contact time, chlor
Isokinetic behaviour in gas phase catalytic hydrodechlorination of chlorobenzene over supported nickel
β Scribed by Mark A. Keane; Ragnar Larsson
- Publisher
- Elsevier Science
- Year
- 2007
- Tongue
- English
- Weight
- 540 KB
- Volume
- 268
- Category
- Article
- ISSN
- 1381-1169
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β¦ Synopsis
The kinetics of the hydrodechlorination (HDC) of chlorobenzene has been measured over Ni supported on a range of substrates (MgO, SiO 2 , Al 2 O 3 , Ta 2 O 5 , MgO, activated carbon (AC) and graphite) of varying BET area (9-843 m 2 g -1 ) where the Ni loading was in the range 1.5-20.3% (w/w) with catalyst preparation by impregnation and deposition-precipitation. The results of a comprehensive TEM analysis is presented wherein it is demonstrated that the supported Ni phase is present in a range of sizes and morphologies. Compensation behaviour is established for chlorobenzene HDC over these catalysts with an associated isokinetic temperature (T iso ) at 669 Β± 2 K. Application of the Selective Energy Transfer (SET) model also arrived at the same calculated T iso (669 K). The SET model is based on the premise of resonance between a vibrational mode of the catalyst and a vibrational mode of the reactant with a transferral of resonance energy from the catalyst to the reactant to generate the "activated complex" with subsequent reaction. In this reaction system, resonance results from energy transfer from the catalytic Ni-H vibration (at 940 cm -1 ) to the out-of-plane C-H vibration (at 740 cm -1 ) of the reactant. The consequence of lumping together experimental kinetic measurements that show slight variations is discussed and rationalized.
π SIMILAR VOLUMES
The catalytic hydrodechlorination of chlorobenzene with NirC, PdrC and Ni Pd rC in ethanol was studied with 2 D 98 2 13 Γ 1 4 Ε½ . and C H NMR. Two dechlorination routes of this reaction ionic and free-radical are suggested depending upon the nature of the active hydrogen species. At the same time t
Many three-phase catalytic reactions are limited by gas-liquid mass translbr. Pre'~aous works have round the transI~er rate to be increased by the presence of fine catalyst particles. Most of the studies concerned active carbon particles m aqueous media This paper inten&s to peint out and to explain