The esterification reaction between ethyl alcohol and acetic acid, catalysed by sulfuric acid, has been investigated over a wide range of temperatures and catalyst concentrations.

In this paper, the homogenous and heterogeneous catalyzed esterification kinetics and the results of the operation in a packed bed reactive distillation column are presented.

The esterification reaction between ethyl alcohol and acetic acid, catalysed by sulfuric acid, has been investigated over a wide range of temperatures and catalyst concentrations.

To investigate the effect of HPA catalyst loading on the conversion of ethanol in the esterification reaction between ethanol and acetic acid, the mole ratio of ethanol to acetic acid was fixed at 1:2, and the reaction temperature was set at 358 K (reflux temperature).

The reaction kinetics of the esterification of acetic acid with ethanol, catalyzed both homogeneously by the acetic acid, and heterogeneously by Amberlyst 15, have been investigated.

The kinetics of the esterification reaction between ethanol and acetic acid catalyzed by sulfuric acid was investigated. Experiments were carried out in a batch reactor over a range of temperatures and catalyst concentrations.

The reaction kinetics was investigated using IH and NIH models and the effect of reaction temperature, catalyst concentration, and initial reactant molar ratio were analyzed.

The reaction kinetics of the esterification of acetic acid with ethanol, catalyzed both homogeneously by the acetic acid, and heterogeneously by Amberlyst 15, have been investigated.

In the present work, esterification reaction between acetic acid and ethanol was conducted in an isothermal batch reactor in the presence of a homogeneous acid catalyst sulphuric acid.

The Esterification kinetics of acetic acid with ethanol in the presence of sulphuric acid as a homogenous catalyst was studied with batch experiments at four different temperatures and at a different molar ratio of ethanol to acetic acid with 5% catalyst loading.