2021
DOI: 10.1126/science.abg7894
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Stable and selective catalysts for propane dehydrogenation operating at thermodynamic limit

Abstract: Intentional (“on-purpose”) propylene production through nonoxidative propane dehydrogenation (PDH) holds great promise for meeting the increasing global demand for propylene. For stable performance, traditional alumina-supported platinum-based catalysts require excess tin and feed dilution with hydrogen; however, this reduces per-pass propylene conversion and thus lowers catalyst productivity. We report that silica-supported platinum-tin (Pt1Sn1) nanoparticles (<2 nanometers in diameter) can operate as a PD… Show more

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Cited by 245 publications
(193 citation statements)
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“…This is supported by the results of TEM and H 2 -O 2 titration ( Figure 3 and Table 1 ). Noteworthy, besides the band at 2060 cm −1 , a weak adsorption band was detected over PtCe/SiO 2 at 1820 cm −1 , ascribed to the bridge-bonded CO on two neighboring Pt atoms [ 24 ]. However, it disappeared in the case of PtSnCe/SiO 2 , accompanying a decreased intensity of the linear adsorption peak at 2060 cm −1 .…”
Section: Resultsmentioning
confidence: 99%
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“…This is supported by the results of TEM and H 2 -O 2 titration ( Figure 3 and Table 1 ). Noteworthy, besides the band at 2060 cm −1 , a weak adsorption band was detected over PtCe/SiO 2 at 1820 cm −1 , ascribed to the bridge-bonded CO on two neighboring Pt atoms [ 24 ]. However, it disappeared in the case of PtSnCe/SiO 2 , accompanying a decreased intensity of the linear adsorption peak at 2060 cm −1 .…”
Section: Resultsmentioning
confidence: 99%
“…However, it disappeared in the case of PtSnCe/SiO 2 , accompanying a decreased intensity of the linear adsorption peak at 2060 cm −1 . The disappeared bridge-bonded CO over PtSnCe/SiO 2 suggests that the SnO 2 breaks the ensemble of Pt atoms and forms a checkerboard Pt-Sn surface structure [ 24 , 50 ] because CO does not adsorb at the bridge sites between Sn and Pt. The decreased intensity of the peak at 2060 cm −1 , in comparison with PtCe/SiO 2 , can be explained as the reduced surface coverage of CO due to the presence of SnO 2 [ 51 ].…”
Section: Resultsmentioning
confidence: 99%
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“…A mixture of PtSn and Pt3Sn alloys was also obtained by direct reduction method, i.e., without conventional calcination, of Pt-Sn/Al2O3 catalyst [37]. Good performance has also been reported with Pt1Sn1/SiO2 catalysts, in which the interaction with the support prevents the Pt-Sn segregation and formation of a tin oxide phase [38].…”
Section: Bimetallic and Promoted Catalystsmentioning
confidence: 99%
“…However, these methods cannot meet the fast-increasing demand of propylene for the low selectivity to propylene and the rapid consumption of fossil resources [9]. Therefore, to develop more efficient technologies for fabricating of propylene such as dehydrogenation of propane (DHP) [10], methanolto-olefins (MTO) [11], coal-to-olefins (CTO) [12], Fischer-Tropsch to Olefins (FTO) [13], and C4 olefin disproportionation technology [14] is highly important. Among them, the DHP technology, as an on-purpose route to obtain propylene, has gradually become the main force to produce propylene in recent years (Figs.…”
Section: Introductionmentioning
confidence: 99%