2014
DOI: 10.1016/s1872-2067(12)60760-8
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NaOH modified WO3/SiO2 catalysts for propylene production from 2-butene and ethylene metathesis

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Cited by 31 publications
(22 citation statements)
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“…Catalysts pretreated in the presence of either He or propene slowly transform the mono-oxo sites to dioxo sites, thereby reducing the activation period usually observed in these catalysts [ 45 ]. Interestingly WO 3 /SiO 2 catalyst ion-exchanged with NaOH also displayed a shorter induction period with a marginal decrease in the isomerization activity [ 47 ]. While the metathesis mechanism under reaction conditions is not yet fully understood, it is clear that the metathesis activity and selectivity are tunable with acidity in metal-incorporated silicates and remains to be explored in more detail, especially with regard to bimetallic formulations.…”
Section: Resultsmentioning
confidence: 99%
“…Catalysts pretreated in the presence of either He or propene slowly transform the mono-oxo sites to dioxo sites, thereby reducing the activation period usually observed in these catalysts [ 45 ]. Interestingly WO 3 /SiO 2 catalyst ion-exchanged with NaOH also displayed a shorter induction period with a marginal decrease in the isomerization activity [ 47 ]. While the metathesis mechanism under reaction conditions is not yet fully understood, it is clear that the metathesis activity and selectivity are tunable with acidity in metal-incorporated silicates and remains to be explored in more detail, especially with regard to bimetallic formulations.…”
Section: Resultsmentioning
confidence: 99%
“…The Raman spectra of the catalysts are shown in Figs and S3. The fresh SiW/SiO 2 and PW/SiO 2 catalysts calcined at 450 °C, regardless of the loading amount, show Raman characteristic bands at 807, 715 and 272 cm −1 , attributed to the symmetric stretching mode of WO, the bending mode of WO and the deformation mode of WOW in crystalline WO 3 , respectively . The characteristic peak intensity of WO 3 increases with an increase of loading, demonstrating that high loading would result in the agglomeration of WO 3 on the sample surfaces .…”
Section: Resultsmentioning
confidence: 95%
“…However, the PW Keggin structure decomposes and forms monoclinic WO 3 crystallites (JCPDS 43‐1035) at calcination temperatures of 450 and 550 °C (Fig. : patterns c and e) …”
Section: Resultsmentioning
confidence: 99%
“…The ammonia desorption peaks of the non-calcined WO 3 /SiO 2 catalysts occurred at higher temperature than the calcined catalysts, indicating the higher acid strength as stronger acidity. 8,32 In addition, increasing the pretreatment temperature caused the ammonia desorption peak to slightly shi to lower temperature, indicating lower acid strength.…”
Section: Acidity Of the Catalystsmentioning
confidence: 99%