2007
DOI: 10.1016/j.catcom.2006.11.018
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Ag/SiO2, Cu/SiO2 and Pd/SiO2 cogelled xerogel catalysts for benzene combustion: Relationships between operating synthesis variables and catalytic activity

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Cited by 50 publications
(30 citation statements)
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“…Generally, the oxidation temperatures for 90% benzene conversion are higher than 220 • C (Table 4). Noticeably, Lambert et al [51] reported an interesting result for benzene oxidation over Pd/SiO 2 xerogel catalyst (T 90 = 197 • C), as can be seen in Table 4. However, the synthesis procedures for this catalyst are very complex and the GHSV (about 800 h −1 ) was much lower than our work (32,000 h −1 ).…”
Section: Catalytic Oxidation Of Benzenementioning
confidence: 67%
“…Generally, the oxidation temperatures for 90% benzene conversion are higher than 220 • C (Table 4). Noticeably, Lambert et al [51] reported an interesting result for benzene oxidation over Pd/SiO 2 xerogel catalyst (T 90 = 197 • C), as can be seen in Table 4. However, the synthesis procedures for this catalyst are very complex and the GHSV (about 800 h −1 ) was much lower than our work (32,000 h −1 ).…”
Section: Catalytic Oxidation Of Benzenementioning
confidence: 67%
“…It is worth noting that the CO 2 selectivity of GtPd/HP 92 -80 (98.3-100%) is higher than that of ImPd/HP 92 -80 (90.6-100%) at different reaction temperatures. It is well known that a high activity of a supported catalyst often resulted from a large active surface area, i.e., a high dispersion of the active phase (small particle size) [41]. For GtPd/HP 92 -80 sample, the Pd nanoparticles are well dispersed on the inner/outer surfaces of mesoporous SBA-15, which may result in the superior catalytic activity.…”
Section: Catalytic Performance and Stability Of Synthesized Catalystsmentioning
confidence: 98%
“…As is known, achieving precise control of the Pd particle size and overall particle size distribution of catalysts is one of the most important challenges to provide excellent catalysis properties [35]. Moreover, a high activity of a supported catalyst often calls for a large active surface area, i.e., high dispersion of the active phase [36]. Herein, the Pd nanoparticles are well-dispersed in pore channels of SBA-15 and the size-restricted mesopores of host silica can effectively prevent the agglomeration of active Pd particles, which resulted in the superior activity of GtPdS-D.…”
Section: Catalytic Oxidation Of Toluenementioning
confidence: 99%