2003
DOI: 10.1007/bf02704219
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Temperature-programmed desorption of water and ammonia on sulphated zirconia catalysts for measuring their strong acidity and acidity distribution

Abstract: Temperature-programmed desorption (TPD) of water and ammonia over ZrO 2 and sulphated ZrO 2 prepared by different methods has been investigated for measuring strong acidity and acidity distribution on sulphated zirconia-type solid super-acid catalysts. The TPD of water provides a simple reliable method for this purpose because of the high stability of water molecules under redox conditions.

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Cited by 16 publications
(4 citation statements)
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“…CZ‐supported metal oxides catalysts are generally free of Brønsted acid sites [35] . As the sample activation was carried out at 500 °C, insignificant signals above 500 °C were likely from dehydration of the sample and hence were not included for total NH 3 uptake calculations [36] …”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…CZ‐supported metal oxides catalysts are generally free of Brønsted acid sites [35] . As the sample activation was carried out at 500 °C, insignificant signals above 500 °C were likely from dehydration of the sample and hence were not included for total NH 3 uptake calculations [36] …”
Section: Resultsmentioning
confidence: 99%
“…[35] As the sample activation was carried out at 500°C, insignificant signals above 500°C were likely from dehydration of the sample and hence were not included for total NH 3 uptake calculations. [36] The CZ support contained some Lewis acid sites (LAS) as indicated by the release of the adsorbed NH 3 . The addition of 2-3 wt% of metal oxide clusters to the CZ support increased the LAS concentration by 80-220 % as indicated by the greater NH 3 uptake (Table 1).…”
Section: Temperature Programmed Desorption Of Ammonia (Nh 3 -Tpd)mentioning
confidence: 99%
“…We determine the strength of water adsorption in six porous oxides (extruded pellets) used as supports and catalysts: TiO 2 ‐a (anatase), TiO 2 ‐r (rutile) (supplied by Evonik‐Degussa), ZrO 2 , γ‐Al 2 O 3 , θ‐Al 2 O 3 and SiO 2 . We chose water as the adsorbate because it is central to aqueous‐phase heterogeneous catalytic processes and, in the context of this work, has the additional advantages of not decomposing during thermally driven desorption 45…”
Section: Methodsmentioning
confidence: 99%
“…We chose water as the adsorbate because it is central to aqueousphase heterogeneous catalytic processes and, in the context of this work, has the additional advantages of not decomposing during thermally driven desorption. [45] The TPD energy distributions for water desorbing from the porous oxides are shown in Figure 2. Due to the uncertainty associated with the tail of the TPD curves, we determine the maximum activation energy of desorption (E max ) where the integral area of the desorption curves is 95 % of the total, see Figure 2.…”
Section: Tpd Experimentsmentioning
confidence: 99%