Gas phase catalytic hydroprocessing of trichlorophenols
โ Scribed by Eun-Jae Shin; Mark A Keane
- Publisher
- Wiley (John Wiley & Sons)
- Year
- 2000
- Tongue
- English
- Weight
- 150 KB
- Volume
- 75
- Category
- Article
- ISSN
- 0268-2575
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โฆ Synopsis
The catalytic hydrodechlorination of four trichlorophenol (TCP) isomers (2,3,5-TCP, 2,3,6-TCP, 2,4,5-TCP and 2,4,6-TCP) was studied in the gas phase using an Ni/SiO 2 catalyst over the temperature range 473 K T 573 K. The catalyst was 100% selective in removing chlorine(s), leaving the hydroxyl group and benzene ring intact. Dechlorination proceeds via stepwise and concerted routes and the relative importance of each is dependent on the nature of the isomer where steric rather than resonance effects appear to determine the ultimate product distribution. Dechlorination efยฎciency is quantiยฎed in terms of phenol yield, chlorine removal rate and the ultimate partitioning of chlorine in the parent organic or product inorganic host. The reaction pathways, with associated pseudo-ยฎrst order rate constants, for the conversion of 2,3,6-TCP and 2,4,6-TCP are presented. The effect of time and temperature on process selectivity is discussed and the nature of catalyst deactivation is considered.
๐ SIMILAR VOLUMES
The catalytic hydrodechlorination reactions of hexachlorobenzene and all of its dechlorinated intermediates were examined in a differential microflow reactor. A presulfided NiMo&Al& catalyst and a reaction temperature of 325ยฐC were used in all of the exoeriments. The dechlorination rate data and Dro
## Abstract The hydrodechlorination reactions of chlorobenzene and 1,2โdichlorobenzene on a NiMo/ฮณAl~2~O~3~ catalyst were examined in a differential microflow reactor. The NiMo catalyst had high activity and selectivity for dechlorination; no hydrogenation of the aromatic ring was detected. The dec