Catalytic Decomposition of HO over Manganese Oxides Supported on an Active Alumina

A series of manganese oxides loaded on to an active alumina support was prepared by impregnation methods and the resulting samples preheated in air at 400°C, 650°C or 900°C for 6 h. The amount of manganese, expressed as Mn 2 O 3 , was varied between 3.7 wt% and 55.3 wt%. The kinetics of the decompos...

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Main Authors: Nasr-Allah M. Deraz, M.A. El-Sayed, A. Abd. El-Aal
Format: Article
Language:English
Published: Hindawi - SAGE Publishing 2001-09-01
Series:Adsorption Science & Technology
Online Access:https://doi.org/10.1260/0263617011494385
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spelling doaj-8e119133a68d4c08bf8ab3605cfec9812021-04-02T11:44:59ZengHindawi - SAGE PublishingAdsorption Science & Technology0263-61742048-40382001-09-011910.1260/0263617011494385Catalytic Decomposition of HO over Manganese Oxides Supported on an Active AluminaNasr-Allah M. Deraz0M.A. El-Sayed1A. Abd. El-Aal2 Physical Chemistry Department, National Research Center, Dokki, Cairo, Egypt Chemistry Department, Faculty of Science, Zagazig University, Zagazig, Egypt Chemistry Department, Faculty of Science, Zagazig University, Zagazig, EgyptA series of manganese oxides loaded on to an active alumina support was prepared by impregnation methods and the resulting samples preheated in air at 400°C, 650°C or 900°C for 6 h. The amount of manganese, expressed as Mn 2 O 3 , was varied between 3.7 wt% and 55.3 wt%. The kinetics of the decomposition of H 2 O 2 in an aqueous medium were studied in the presence of these oxides. The catalytic activities increased initially as the amounts of manganese present increased, attaining a maximum value at 13.4 wt% Mn 2 O 3 and then decreasing on increasing both the amount of manganese above this limit and the precalcination temperature from 400°C to 900°C. The specific surface areas of the various catalysts were determined by BET analysis of the nitrogen adsorption isotherms. The S BET values varied from 244 m 2 /g to 80 m 2 /g both as a function of the extent of loading and the precalcination temperature. However, the activation energy for sintering, ΔE S , increased on increasing the amount of Mn 2 O 3 present. The apparent activation energy for H 2 O 2 decomposition conducted over the various solids was found to be virtually unaffected by a change in the amount of manganese present.https://doi.org/10.1260/0263617011494385
collection DOAJ
language English
format Article
sources DOAJ
author Nasr-Allah M. Deraz
M.A. El-Sayed
A. Abd. El-Aal
spellingShingle Nasr-Allah M. Deraz
M.A. El-Sayed
A. Abd. El-Aal
Catalytic Decomposition of HO over Manganese Oxides Supported on an Active Alumina
Adsorption Science & Technology
author_facet Nasr-Allah M. Deraz
M.A. El-Sayed
A. Abd. El-Aal
author_sort Nasr-Allah M. Deraz
title Catalytic Decomposition of HO over Manganese Oxides Supported on an Active Alumina
title_short Catalytic Decomposition of HO over Manganese Oxides Supported on an Active Alumina
title_full Catalytic Decomposition of HO over Manganese Oxides Supported on an Active Alumina
title_fullStr Catalytic Decomposition of HO over Manganese Oxides Supported on an Active Alumina
title_full_unstemmed Catalytic Decomposition of HO over Manganese Oxides Supported on an Active Alumina
title_sort catalytic decomposition of ho over manganese oxides supported on an active alumina
publisher Hindawi - SAGE Publishing
series Adsorption Science & Technology
issn 0263-6174
2048-4038
publishDate 2001-09-01
description A series of manganese oxides loaded on to an active alumina support was prepared by impregnation methods and the resulting samples preheated in air at 400°C, 650°C or 900°C for 6 h. The amount of manganese, expressed as Mn 2 O 3 , was varied between 3.7 wt% and 55.3 wt%. The kinetics of the decomposition of H 2 O 2 in an aqueous medium were studied in the presence of these oxides. The catalytic activities increased initially as the amounts of manganese present increased, attaining a maximum value at 13.4 wt% Mn 2 O 3 and then decreasing on increasing both the amount of manganese above this limit and the precalcination temperature from 400°C to 900°C. The specific surface areas of the various catalysts were determined by BET analysis of the nitrogen adsorption isotherms. The S BET values varied from 244 m 2 /g to 80 m 2 /g both as a function of the extent of loading and the precalcination temperature. However, the activation energy for sintering, ΔE S , increased on increasing the amount of Mn 2 O 3 present. The apparent activation energy for H 2 O 2 decomposition conducted over the various solids was found to be virtually unaffected by a change in the amount of manganese present.
url https://doi.org/10.1260/0263617011494385
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