Characterization of sepiolite as a support of silver catalyst in soot combustion
Turkish sepiolite–zirconium oxide mixtures were applied as a support for the silver catalyst in a soot combustion. Sepiolite–Zr–K–Ag–O catalyst was characterized by XRD, N2 adsorption, SEM, TPR-H2 and EGA-MS. The combustion of soot was studied with a thermobalance (TG-DTA). The modification resulted...
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Published in: | Applied clay science Vol. 32; no. 3-4; pp. 291 - 296 |
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Main Authors: | , , , , , |
Format: | Journal Article |
Language: | English |
Published: |
Lausanne
Elsevier B.V
01-05-2006
Amsterdam Elsevier Science New York, NY |
Subjects: | |
Online Access: | Get full text |
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Summary: | Turkish sepiolite–zirconium oxide mixtures were applied as a support for the silver catalyst in a soot combustion. Sepiolite–Zr–K–Ag–O catalyst was characterized by XRD, N2 adsorption, SEM, TPR-H2 and EGA-MS. The combustion of soot was studied with a thermobalance (TG-DTA). The modification resulted in a partial degradation of the sepiolite structure, however, the morphology was preserved. The adsorption of N2 of the modified sepiolite is a characteristic for mesoporous materials with a wide distribution of pores. The specific surface area SBET equals 83 m2/g and the pores volume is 0.23 cm3/g. The basic character of the surface centers of sepiolite is indicated by CO2 desorption (TPD-MS) at 170 °C and at about 620 °C due to a surface carbonates decomposition. The thermodesorption of oxygen at 650–850 °C indicates the decomposition of AgOx phases at the surface. The presence of AgOx phases is also confirmed by TPR-H2 spectrum (low temperature reduction peak at 130 and 180 °C). The high-temperature reduction at about 570 °C is probably related to Ag–O–M phases on the support.
The soot combustion takes place at T50=575 °C. Without silver (sepiolite–Zr–K–O) T50=560 °C but sepiolite modified with silver (sepiolite–Zr–K–Ag–O) undergoes the same process at T50=490 °C. |
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ISSN: | 0169-1317 1872-9053 |
DOI: | 10.1016/j.clay.2006.03.005 |