2007
DOI: 10.1016/j.apcata.2007.06.003
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The acid properties of H-ZSM-5 as studied by NH3-TPD and 27Al-MAS-NMR spectroscopy

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Cited by 325 publications
(183 citation statements)
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“…8. Two notable peaks, at 250°C representing the weak acid sites and 450°C representing the strong acid ones [30,31]. According to the areas of the NH 3 -TPD profiles, the relative acid densities can be calculated and estimated, indicating that the total acid densities of ZSM-5 zeolites were slightly increased after alkali-and acid-treatment.…”
Section: Acidity Of Zeolitesmentioning
confidence: 99%
“…8. Two notable peaks, at 250°C representing the weak acid sites and 450°C representing the strong acid ones [30,31]. According to the areas of the NH 3 -TPD profiles, the relative acid densities can be calculated and estimated, indicating that the total acid densities of ZSM-5 zeolites were slightly increased after alkali-and acid-treatment.…”
Section: Acidity Of Zeolitesmentioning
confidence: 99%
“…Microcalorimetry, [14][15][16] temperature-programmed desorption (TPD), 17,18 infrared (IR) [19][20][21][22][23][24][25][26][27] and nuclear magnetic resonance (NMR) spectroscopy 17,28 are among other experimental techniques some of the most frequently used ones. A fundamental challenge of zeolite acidity characterisation is that different experimental techniques provide different aspects of the zeolite acidity, which includes type, number, location and strength of acid sites.…”
mentioning
confidence: 99%
“…Fig.3. In Fig.3 curve a, the reduction peak at 197 °C can be attributed to the reduction of ruthenium oxide [24] . When the addition amount of lanthanum was 3%, the reduction temperature of ruthenium oxide increased from 197 °C [25] for the monometallic Ru catalyst to 261 °C for 4%Ru-3%La/γ-Al 2 O 3 (I) and the reduction peak intensity of ruthenium oxide became weak( Fig.3 curve b).…”
Section: Characterization Of Catalystsmentioning
confidence: 95%
“…Because of the weak polarity and intrinsic steric hindrance of carboxylic group [7] , the hydrogenation of carboxylic acids and esters is very difficult. For instance, the hydrogenation of esters over copper-based catalysts, which are widely used in industry [8] , is carried out at a high temperature of 200-300 °C and a high hydrogen pressure of [20][21][22][23][24][25][26][27][28][29][30] MPa. Therefore, to develop an active catalyst system for the hydrogenation of esters to the corresponding alcohols under a mild condition is of great importance in research as well as in industry.…”
Section: Introductionmentioning
confidence: 99%