The gas phase pyrolysis of phenol
β Scribed by A. B. Lovell; K. Brezinsky; I. Glassman
- Publisher
- John Wiley and Sons
- Year
- 1989
- Tongue
- English
- Weight
- 623 KB
- Volume
- 21
- Category
- Article
- ISSN
- 0538-8066
No coin nor oath required. For personal study only.
β¦ Synopsis
Phenol pyrolysis has been studied in a turbulent flow reactor by analyzing concentration-time profiles of three major decomposition products: carbon monoxide, cyclopentadiene, and benzene. Experimental conditions were P = 1 atm, T = 1064 -1162 K, and initial phenol concentrations of 500-2016 ppm. The major experimental observations were that the decomposition product profiles were nearly linear as a function of time and that the overall rate of carbon monoxide production was greater than that of cyclopentadiene. The rate difference is explained by a mechanism which includes a radical combination reaction of cyclopentadienyl and phenoxy. With literature and approximate rate coefficient data, the mechanism reproduced the experimental observations very well. The mechanism and data provide estimates of rate coefficients for the phenol decomposition initiation step, abstraction of hydrogen from phenol by cyclopentadienyl, and the phenoxy-cyclopentadienyl combination, all of which have not been available in the literature.
π SIMILAR VOLUMES
## Abstract The pyrolysis of gaseous neopentyl bromide to 2βmethylβ2βbutene, 2βmethylβ1βbutene, and hydrogen bromide was studied under conditions of maximal inhibition by cyclohexene over the temperature range of 389β444Β°C. This reaction was shown to beconsistent with a firstβorder homogeneous mole
The gas-phase pyrolysis kinetics of primary, secondary and tertiary 2-phenoxycarboxylic acids were studied over the temperature range 240.1-409.9 Β°C and pressure range 16.3-67.8 Torr. The elimination reactions, carried out in seasoned vessels and in the presence of the free radical chain inhibitor c