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Physicochemical surface and catalystic properties of Cr2O3/Al2O3 system
Faculty
Science
Year:
1999
Type of Publication:
Article
Pages:
315-326
Authors:
Ghozza, AM, El-Shobaky, GA, Mohamed, GM, El-Shobaky, HG
DOI:
10.1016/S0927-7757(98)00859-0
Journal:
COLLOIDS AND SURFACES A-PHYSICOCHEMICAL AND ENGINEERING ASPECTS ELSEVIER SCIENCE BV
Volume:
152
Research Area:
Chemistry
ISSN
ISI:000081116800009
Keywords :
catalytic, Cr2O3/Al2O3 system, oxidation of CO by O-2, surface characteristics
Abstract:
Solid-solid interactions, surface and catalystic properties of Cr2O3/Al2O3 system were investigated using TG, DTA, XRD, nitrogen adsorption at - 196 degrees C and CO-oxidation by O-2 at 250-400 degrees C. The amount of chromium oxide was varied between 4.3 and 42.7 wt.\% Cr2O3. The results showed that heating of AI(OH), pretreated with different amounts of CrO3 at 400-900 degrees C resulted in the formation of a mixture of gamma-, k-,theta-aluminas, Cr2O5, CrO2 and alpha-Cr2O3 phases. The rise in calcination temperature to 1000 degrees C made the appearance of minute amounts of alpha-Al2O3 and Cr3O4 besides the other phases (alpha-Cr2O3 and theta-, k-Al2O3). The BET-surface area decreases by increasing the precalcination temperature in the range 400-1000 degrees C. The mixed oxide adsorbents calcined at 400-600 degrees C contain mainly narrow pores and turned to wide pores upon heating at 700-1000 degrees C. The activation energy of sintering (Delta E-s) decreases markedly from 21 to 7.6 kJ mol(-1) by increasing the amount of Cr2O3 from 4.3 to 8.3 wt.\% then increases progressively reaching to 33 kJ mol(-1) in the presence of 42.7 wt.\% Cr2O3. The catalystic activity increases as a function of Cr2O3 content. The curves relating the catalystic activity (reaction rate constant per unit surface area) and precalcination temperature exhibited a maximum at 700 or 800 degrees C depending on the amount of Cr2O3 present. The rise in both Cr2O3 content and calcination temperature did not modify the mechanism of the catalystic reaction but changed the concentration of catalystically active constituents without altering their energetic nature. (C) 1999 Elsevier Science B.V. All rights reserved.
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