1992
DOI: 10.1135/cccc19920853
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Fries Rearrangement of Phenyl Acetate over ZSM-5 Based Catalysts

Abstract: Catalysts based on samples of ZSM-5, differing in Si/Al ratio were applied in the Fries rearrangement of phenyl acetate. Experiments were carried out in batch reactors at 180 °C and continuously at various temperatures both in liquid phase and gas phase. A reaction scheme is proposed.

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Cited by 13 publications
(4 citation statements)
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“…Consequently, a high-performance catalyst for the Fries rearrangement is expected to have a stabilizing capacity for the cations. Increasing selectivity for the Fries rearrangement [26,27] as well as increasing p/o ratio of hydroxyacetophenone [77] with decreasing reaction temperature agrees with this interpretation. Liquid phase reaction exhibited better selectivity for the Fries rearrangement compared with the gas phase reaction [27], in which no solvation for the cations is present.…”
Section: Reaction Mechanismsupporting
confidence: 82%
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“…Consequently, a high-performance catalyst for the Fries rearrangement is expected to have a stabilizing capacity for the cations. Increasing selectivity for the Fries rearrangement [26,27] as well as increasing p/o ratio of hydroxyacetophenone [77] with decreasing reaction temperature agrees with this interpretation. Liquid phase reaction exhibited better selectivity for the Fries rearrangement compared with the gas phase reaction [27], in which no solvation for the cations is present.…”
Section: Reaction Mechanismsupporting
confidence: 82%
“…Rapid deactivation of zeolitic catalysts particularly in the gas phase reaction owing to coke formation has been reported in the initial stage of this reaction [27]. The deactivation was increased by an increase in the reaction temperature; a similar temperature effect is also reported on H-ZSM-5 for this reaction [26]. The catalytic activity will henceforth be discussed at 3 h after reaction started.…”
Section: Development Of Catalytic Activitymentioning
confidence: 81%
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“…Because the carbonyl oxygen strongly coordinates to the Lewis acid center [39], hydrolysis of the Lewis acid is necessary for the isolation of the products. In order to overcome this disadvantage, solid Brønsted acids such as H-Beta zeolite [40][41][42][43], H-Y zeolite [42,44,45], H-ZSM-5 [40][41][42][44][45][46][47], HF/Al 2 O 3 [44], and Nafion-H [48], a resin containing the -CF 2 CF 2 SO 3 H group, are used as the catalyst. However, the selectivity for o-and p-hydroxyacetophenone is not high, and in almost all cases the main product is the decomposition product, phenol.…”
Section: Decomposition Of Phenyl Acetate (Equation (3)) [37]mentioning
confidence: 99%