2010
DOI: 10.1016/j.jcat.2010.09.014
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Solid acid catalysts based on H3PW12O40 heteropoly acid: Acid and catalytic properties at a gas–solid interface

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Cited by 144 publications
(137 citation statements)
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“…Before analysis, the samples were evacuated in situ at 250 • C for 3 h. Powder X-ray diffraction (XRD) of catalysts was measured on a PANalytical Xpert diffractometer using a monochromatic CuK˛ radiation ( = 1.542Å) in a 2Â range of 20-80 • . DRIFTS (diffuse reflectance infrared Fourier transform spectra) of adsorbed pyridine were taken on a Nicolet Nexus FTIR spectrometer as described elsewhere [22]. Catalyst samples were ground with KBr (10 wt% in KBr) and pre-treated at 150 • C/10 −5 bar for 1 h. The samples were then exposed to pyridine vapour at room temperature for 1 h, followed by pumping out at 150 • C/10 −5 bar for 1 h to remove physisorbed pyridine.…”
Section: Catalyst Characterisationmentioning
confidence: 99%
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“…Before analysis, the samples were evacuated in situ at 250 • C for 3 h. Powder X-ray diffraction (XRD) of catalysts was measured on a PANalytical Xpert diffractometer using a monochromatic CuK˛ radiation ( = 1.542Å) in a 2Â range of 20-80 • . DRIFTS (diffuse reflectance infrared Fourier transform spectra) of adsorbed pyridine were taken on a Nicolet Nexus FTIR spectrometer as described elsewhere [22]. Catalyst samples were ground with KBr (10 wt% in KBr) and pre-treated at 150 • C/10 −5 bar for 1 h. The samples were then exposed to pyridine vapour at room temperature for 1 h, followed by pumping out at 150 • C/10 −5 bar for 1 h to remove physisorbed pyridine.…”
Section: Catalyst Characterisationmentioning
confidence: 99%
“…The DRIFT spectra were recorded at room temperature (4 cm −1 resolution). Differential heats of ammonia adsorption on the catalysts were measured at 150 • C by a pulse method in a flow system using a Setaram TG-DSC 111 differential scanning calorimeter as described previously [22].…”
Section: Catalyst Characterisationmentioning
confidence: 99%
“…Despite the mild reaction conditions of this industrial process, its low conversion and selectivity requires significant advances to improve both atom and energy efficiency. A wide range of alternative catalysts have been explored including alloys, [14] clays, [18,19] zeolites, [20,21] sulphated zirconia, [16,22], Al-incorporated MCM-41 [23] and heteropolyacids (HPAs); [24][25][26][27][28] with strong solid acids conferring improved conversion and selectivity. [21,22,24,27,29] HPAs are polyoxometalate inorganic cages which possess high Brönsted acid strengths (approaching the superacidic region) and tunable redox activity depending on the particular constituent elements.…”
Section: Introductionmentioning
confidence: 99%
“…Therefore, any enhancement of Pd activity would not cause a significant increase in benzene conversion. Silica-supported HSiW catalysts were prepared by the impregnation of Aerosil 300 silica by an aqueous HSiW solution, which was then dried at 150 • C/10 −3 kPa for 1.5 h [30,31]. The integrity of the HSiW Keggin structure on the silica surface in fresh and spent catalysts was confirmed by infrared spectroscopy ( Figure S1 in the Supporting Material).…”
Section: Chemicals and Catalystsmentioning
confidence: 99%