Wet air oxidation and catalytic wet air oxidation for refinery spent caustics degradation

The work focuses on evaluating wet air oxidation and catalytic wet air oxidation technique to degrade refinery spent caustics (original cod is 250,781 mg/l) in a milder operation conditions (150-200°c,0.2-2.5mpa). the results show that: in non-catalyst wao,the highest cod degradation conversion could reach about 75% when 200°c,2mpa oxygen and 300rpm were used. at every temperature,the reaction procedures follow pseudo-first order equations and the activation energy is 45.5 kj/mol. the reactivity of three main contaminants in wastewater is on the order of sulphide > petroleum > volatile phenol. the cod degradation conversion could improve to about 95% when composite catalyst mnox-ceox/γ-al2o3 (w mn/wγ-al2o3=0.5 and wce/w mnox/γ-al2o3=0.4) was used. the pseudo-first order equations also could be applied for catalyst system and its activation energy decreases to 27.2 kj/mol. the catalyst could improve the degradation efficiency of petroleum and volatile phenol. their conversions could increase to 85% and 74% respectively after catalyst used.