2014
DOI: 10.1016/j.apcatb.2014.05.014
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The oxidation of trichloroethylene over different mixed oxides derived from hydrotalcites

Abstract: ElsevierBlanch Raga, N.; Palomares Gimeno, AE.; Martínez Triguero, LJ.; Puche Panadero, M.; Fetter, G.; Bosch, P. (2014)

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Cited by 36 publications
(22 citation statements)
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“…Regarding the cobalt-containing samples, both of them presented a broad reduction peak between aluminium framework [7] or to the reduction of Co 2-x species [35]. It was observed that the beta-Co (HS) has a sharper and better defined peak than the beta-Co (IE), indicating the presence of more homogeneous cobalt species in this sample.…”
Section: Catalysts Characterizationmentioning
confidence: 88%
See 1 more Smart Citation
“…Regarding the cobalt-containing samples, both of them presented a broad reduction peak between aluminium framework [7] or to the reduction of Co 2-x species [35]. It was observed that the beta-Co (HS) has a sharper and better defined peak than the beta-Co (IE), indicating the presence of more homogeneous cobalt species in this sample.…”
Section: Catalysts Characterizationmentioning
confidence: 88%
“…It requires lower temperatures (250-550°C), generating less energetic costs and preventing the formation of non-desired by-products. Several catalysts, as metal oxides [6][7][8][9][10][11], bronzes [12] and noble metals supported on different materials [13] have been studied for the catalytic oxidation of chlorinated organic volatile compounds (CVOCs), but they have problems related with the catalyst deactivation and with the formation of toxic by-products [14]. Other materials, as acid zeolites have been described as alternative catalysts for the trichloroethylene oxidation [15].…”
Section: Introductionmentioning
confidence: 99%
“…Obviously, the 0.91Au 0.51 Pd/3DOM TiO 2 sample possessed the TCE reaction rate (50.4 µmol/(g Noble metal s)) and the highest TOF (0.96 × 10 −3 s −1 ) at 300 • C. In the past years, there have been a number of works on the oxidation of TCE over various catalysts in the literature, and their typical activities are listed in Table S2. It can be observed that the TCE oxidation rate at 250 • C (2.69 × 10 −7 mol/(g cat s)) over 0.91Au 0.51 Pd/3DOM TiO 2 was much higher than those ((1.12-1.13) × 10 −7 mol/(g cat s)) over CeMn-HT-N6A4 [36] and 1.02 wt% Ru/TiO 2 (P25) [37], those ((2.67-9.76) × 10 −8 mol/(g cat s)) over Ce 0.15 Zr 0.85 O 2 [38], LaMn 1.2 O 3 [33], 4Ce1Cr-(NH 4 ) 2 CO 3 [39], and 3.5 wt% VO x /TiO 2 -SG [40], and those ((2.67-7.05) × 10 −9 mol/(g cat s)) over 4.3 wt% Mn/H-ZSM-5 [41], 0.42 wt% Pd/Al 2 O 3 [42], and CoFeAlO x [43].…”
Section: Surface Acid Propertymentioning
confidence: 99%
“…Less-expensive catalysts, based on metallic oxides, have also been prepared as uniform catalyst or supported on high surface materials (e.g., γ-Al 2 O 3 ) [12,13]. Blanch-Raga et al reported the oxidation of TCE over different mixed oxides derived from hydrotalcites [14], with the Co(Fe/Al) catalyst being the most active (T 50% = 280 • C and T 90% = 340 • C at Gas Hourly Space Velocity, GHSV = 15,000 h −1 and [TCE] = 1000 ppm) due to its acidic and oxidative properties. Zeolites also represent an important type of active catalysts for the oxidation of TCE and many papers have reported on the synergic effect of acidic sites in zeolites [15] with metal catalysts in order to improve the performance of the whole catalytic system.…”
Section: Introductionmentioning
confidence: 99%
“…The best results (T 50% = 310 • C and T 90% = 360 • C at GHSV = 15,000 h −1 and [TCE] = 1000 ppm) were obtained by using Cu-doped zeolite, which combined the acid sites of the zeolite with the redox properties of the copper ions [17]. Notwithstanding, zeolites-based catalysts suffer some drawbacks, which include coke formation, deactivation, and formation of chlorinated by-products [14].…”
Section: Introductionmentioning
confidence: 99%