2004
DOI: 10.1016/j.cattod.2004.06.127
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The novel and highly selective fumed silica-supported VPO for partial oxidation of n-butane to maleic anhydride

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Cited by 22 publications
(6 citation statements)
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“…The peaks (Figure 5) below 700 °C and above 700 °C are attributed to the removal of lattice oxygen related to V 5+ and V 4+ species, respectively. 32,33 Only the removal of lattice oxygen related to V 5+ can be observed clearly; the results are in good agreement with XRD measurements. When the six catalysts are compared, the reduction temperature of VPO/γ-Al 2 O 3 is the lowest and even lower than that of pure VPO (529 and 752 °C; the profile is presented in Figure S4).…”
Section: Resultssupporting
confidence: 81%
“…The peaks (Figure 5) below 700 °C and above 700 °C are attributed to the removal of lattice oxygen related to V 5+ and V 4+ species, respectively. 32,33 Only the removal of lattice oxygen related to V 5+ can be observed clearly; the results are in good agreement with XRD measurements. When the six catalysts are compared, the reduction temperature of VPO/γ-Al 2 O 3 is the lowest and even lower than that of pure VPO (529 and 752 °C; the profile is presented in Figure S4).…”
Section: Resultssupporting
confidence: 81%
“…Therefore, H 2 -TPR was applied for identifying the vanadium oxidation state in various samples. As shown in Figure , the TPR profiles could be deconvoluted into two or three components via curve-fitting analysis, and the derived peaks below 700 °C and beyond 700 °C were attributed to the reduction of V 5+ and V 4+ species, respectively. , The H 2 consumption was calibrated and listed in Table S1 (SI). According to our previous study, the two reduction peaks below 700 °C in Figure were due to the reduction of different V 5+ -phases.…”
Section: Resultsmentioning
confidence: 99%
“…There are other supports such as MCM-41, Al-MCM-41, fumed silica, silica, alumina, titania, phosphoric acid treated zirconia which are also used as the supports for VPO catalyst. [30][31][32][33] It is well documented that the use of a support for metal oxide catalysts favours enhancement of active phase dispersion and also imparts stability to the catalysts. The use of supported catalyst during glycerol dehydration reaction have several advantages such as the enhancement of dispersion of the active phase on the support, the distribution of the pore size of the support and the acidity of the catalyst.…”
Section: Introductionmentioning
confidence: 99%