In this communication, we describe p-xylene oxidation with molecular oxygen at 373 K and atmospheric pressure using N-hydroxyimide catalysts. p-Xylene conversion was rather high over the first 2 h of reaction and complete by the end of the experiment. The product distribution curves versus reaction time are typical of consecutive reactions. The main intermediate product is p-toluic acid. Peak concentration and the shape of its concentration profile depend heavily on the N-hydroxyimide catalyst used. This effect seems to be related to the NO-H bond dissociation energy (BDE) of the N-hydroxyimides employed
A simple and mild (room temperature) process for oxidation of o-, m- or p-xylene to the correspondin...
Fundamental disappearance kinetics parameters have been obtained for four compounds individually sub...
4,4′-(4,4′-Isopropylidenediphenoxy)bis(N-hydroxyphthalimide), which is a new lipophilic analogue of ...
In this communication, we describe p-xylene oxidation with molecular oxygen at 373 K and atmospheric...
A facile and precise batch oxidation reaction system allows continuous monitoring of the oxidation r...
The kinetics of the vapor phase oxidation of p-xylene over ferric molybdate catalyst were studied in...
439-441Liquid phase oxidation of p-xylene has been carried out in the presence of potassium salts ...
A lumped kinetic model for the liquid-phase oxidation of p-xylene to terephthalic acid catalyzed by ...
Catalytic vapor-phase oxidation of p-xylene was studied in an isothermal plug flow reactor using mix...
Rates of oxidation of p-xylene were measured in the temperature range 320 to 420 °C using tin vanada...
A semibatch gas-liquid reactor model based on a lumped kinetic scheme for the liquid-phase oxidation...
A lumped kinetic scheme for the liquid-phase oxidation of p-xylene to terephthalic acid catalyzed by...
A mixture of benzaldehyde and xylene was used as the oxidation sample. The mixture was benzaldehyde/...
Large-scale chemical processes to produce terephthalic acid via p-xylene partial oxidation typically...
The influence of catalyst concentration, i.e. cobalt naphthenate, on product distribution and kinet...
A simple and mild (room temperature) process for oxidation of o-, m- or p-xylene to the correspondin...
Fundamental disappearance kinetics parameters have been obtained for four compounds individually sub...
4,4′-(4,4′-Isopropylidenediphenoxy)bis(N-hydroxyphthalimide), which is a new lipophilic analogue of ...
In this communication, we describe p-xylene oxidation with molecular oxygen at 373 K and atmospheric...
A facile and precise batch oxidation reaction system allows continuous monitoring of the oxidation r...
The kinetics of the vapor phase oxidation of p-xylene over ferric molybdate catalyst were studied in...
439-441Liquid phase oxidation of p-xylene has been carried out in the presence of potassium salts ...
A lumped kinetic model for the liquid-phase oxidation of p-xylene to terephthalic acid catalyzed by ...
Catalytic vapor-phase oxidation of p-xylene was studied in an isothermal plug flow reactor using mix...
Rates of oxidation of p-xylene were measured in the temperature range 320 to 420 °C using tin vanada...
A semibatch gas-liquid reactor model based on a lumped kinetic scheme for the liquid-phase oxidation...
A lumped kinetic scheme for the liquid-phase oxidation of p-xylene to terephthalic acid catalyzed by...
A mixture of benzaldehyde and xylene was used as the oxidation sample. The mixture was benzaldehyde/...
Large-scale chemical processes to produce terephthalic acid via p-xylene partial oxidation typically...
The influence of catalyst concentration, i.e. cobalt naphthenate, on product distribution and kinet...
A simple and mild (room temperature) process for oxidation of o-, m- or p-xylene to the correspondin...
Fundamental disappearance kinetics parameters have been obtained for four compounds individually sub...
4,4′-(4,4′-Isopropylidenediphenoxy)bis(N-hydroxyphthalimide), which is a new lipophilic analogue of ...