Stable and selective catalysts for propane dehydrogenation operating at thermodynamic limit

被引:311
作者
Motagamwala, Ali Hussain [1 ,2 ,3 ]
Almallahi, Rawan [1 ,2 ]
Wortman, James [1 ,2 ]
Igenegbai, Valentina Omoze [1 ,2 ]
Linic, Suljo [1 ,2 ]
机构
[1] Univ Michigan, Dept Chem Engn, Ann Arbor, MI 48109 USA
[2] Univ Michigan, Catalysis Sci & Technol Inst, Ann Arbor, MI 48109 USA
[3] Shell Chem Co, Shell Technol Ctr Houston, 1N3 Highway 6 South, Houston, TX 77082 USA
基金
美国国家科学基金会;
关键词
OXIDATIVE DEHYDROGENATION; GALLIUM OXIDE; SN; PERFORMANCE; SURFACE; TIN; CLUSTERS; PROPENE; SILICA; DEACTIVATION;
D O I
10.1126/science.abg7894
中图分类号
O [数理科学和化学]; P [天文学、地球科学]; Q [生物科学]; N [自然科学总论];
学科分类号
07 ; 0710 ; 09 ;
摘要
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 PDH catalyst at thermodynamically limited conversion levels, with excellent stability and selectivity to propylene (>99%). Atomic mixing of Pt and Sn in the precursor is preserved upon reduction and during catalytic operation. The benign interaction of these nanoparticles with the silicon dioxide support does not lead to Pt-Sn segregation and formation of a tin oxide phase that can occur over traditional catalyst supports.
引用
收藏
页码:217 / +
页数:36
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