Effect of operation conditions on Catalytic Oxidation of Phenol in Aqueous Solution

This work was conducted to study the oxidation of phenol in aqueous solution using copper based catalyst with zinc as promoter and different carrier, i.e. γ-Alumina and silica. These catalysts were prepared by impregnation method. The effect of catalyst composition, pH (5.6-9), phenol to catalyst c...

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Main Authors: Wadood T. Mohammed, Hisham A. Kadim
Format: Article
Language:English
Published: University of Baghdad/College of Engineering 2008-12-01
Series:Iraqi Journal of Chemical and Petroleum Engineering
Online Access:http://ijcpe.uobaghdad.edu.iq/index.php/ijcpe/article/view/451
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spelling doaj-f38cbd030edc40f5b2df0b76ca533c792020-11-25T02:26:34ZengUniversity of Baghdad/College of EngineeringIraqi Journal of Chemical and Petroleum Engineering1997-48842618-07072008-12-0194Effect of operation conditions on Catalytic Oxidation of Phenol in Aqueous SolutionWadood T. MohammedHisham A. Kadim This work was conducted to study the oxidation of phenol in aqueous solution using copper based catalyst with zinc as promoter and different carrier, i.e. γ-Alumina and silica. These catalysts were prepared by impregnation method. The effect of catalyst composition, pH (5.6-9), phenol to catalyst concentration ratio (2-0.5), air feed rate (30-50) ml/s, stirring speed (400-800) rpm, and temperature (80-100) °C were examined in order to find the best conditions for phenol conversion. The best operating conditions which lead to maximum phenol conversion (73.1%) are : 7.5 pH, 4/6 phenol to catalyst concentration, 40 ml/s air feed rate, 600 rpm stirring speed, and 100 °C reaction temperature. The reaction involved an induction period and a steady state activity regime. Both of the regimes exhibiting first order behavior with respect to the phenol concentration. The rate constants k1 and k2 for the initial rate and steady state activity regime are represented by k1=1.9×10-3 ((cm3liq/gcat) 0.5s-1 and k2= 2.4×10-10 ((cm3liq/gcat) 2 s-1) respectively. http://ijcpe.uobaghdad.edu.iq/index.php/ijcpe/article/view/451
collection DOAJ
language English
format Article
sources DOAJ
author Wadood T. Mohammed
Hisham A. Kadim
spellingShingle Wadood T. Mohammed
Hisham A. Kadim
Effect of operation conditions on Catalytic Oxidation of Phenol in Aqueous Solution
Iraqi Journal of Chemical and Petroleum Engineering
author_facet Wadood T. Mohammed
Hisham A. Kadim
author_sort Wadood T. Mohammed
title Effect of operation conditions on Catalytic Oxidation of Phenol in Aqueous Solution
title_short Effect of operation conditions on Catalytic Oxidation of Phenol in Aqueous Solution
title_full Effect of operation conditions on Catalytic Oxidation of Phenol in Aqueous Solution
title_fullStr Effect of operation conditions on Catalytic Oxidation of Phenol in Aqueous Solution
title_full_unstemmed Effect of operation conditions on Catalytic Oxidation of Phenol in Aqueous Solution
title_sort effect of operation conditions on catalytic oxidation of phenol in aqueous solution
publisher University of Baghdad/College of Engineering
series Iraqi Journal of Chemical and Petroleum Engineering
issn 1997-4884
2618-0707
publishDate 2008-12-01
description This work was conducted to study the oxidation of phenol in aqueous solution using copper based catalyst with zinc as promoter and different carrier, i.e. γ-Alumina and silica. These catalysts were prepared by impregnation method. The effect of catalyst composition, pH (5.6-9), phenol to catalyst concentration ratio (2-0.5), air feed rate (30-50) ml/s, stirring speed (400-800) rpm, and temperature (80-100) °C were examined in order to find the best conditions for phenol conversion. The best operating conditions which lead to maximum phenol conversion (73.1%) are : 7.5 pH, 4/6 phenol to catalyst concentration, 40 ml/s air feed rate, 600 rpm stirring speed, and 100 °C reaction temperature. The reaction involved an induction period and a steady state activity regime. Both of the regimes exhibiting first order behavior with respect to the phenol concentration. The rate constants k1 and k2 for the initial rate and steady state activity regime are represented by k1=1.9×10-3 ((cm3liq/gcat) 0.5s-1 and k2= 2.4×10-10 ((cm3liq/gcat) 2 s-1) respectively.
url http://ijcpe.uobaghdad.edu.iq/index.php/ijcpe/article/view/451
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