شماره ركورد كنفرانس :
4518
عنوان مقاله :
An industrial investigation into COx formation in p-Xylene oxidation reactor
Author/Authors :
Sasan Arabi (Process Engineering Department, Tondgooyan Petrochemical Co.(STPC , Mazyar Madooli Behbehani (Process Engineering Department, Tondgooyan Petrochemical Co.(STPC , Elham Amini (Process Engineering Department, Tondgooyan Petrochemical Co.(STPC
كليدواژه :
Burning side reaction , P-Xylene , Oxidation , Kinetics , Terephthalic Acid , Acetic Acid
عنوان كنفرانس :
The 7th International Chemical Engineering Congress & Exhibition (IChEC 2011
چكيده لاتين :
During the liquid-phase oxidation of P-Xylene, over-oxidation of reactant and solvent to Carbon
dioxide and Carbon monoxide is generally known as the burning side reaction. The effect of
reaction pressure and temperature on the burning side reaction was studied in this paper. Several
tests carried out in an industrial reactor which produces Terephthalic Acid by liquid-phase
oxidation of P-Xylene and the experimental data of the burning side reaction were analyzed and
reported. The yield of main reaction was kept constant by changing in catalyst concentration. The
result showed the rates of burning side reactions are reduced remarkably with decreasing in reactor
pressure and temperature. Finally, a direct relation between burning side reaction and reaction
pressure and temperature was developed and the model parameters were determined by data fitting
of the burning side reaction rate curves.