Platinum-tin and platinum-copper catalysts for autothermal oxidative dehydrogenation of ethane to ethylene

被引:77
作者
Yokoyama, C
Bharadwaj, SS
Schmidt, LD
机构
[1] UNIV MINNESOTA, DEPT CHEM ENGN & MAT SCI, MINNEAPOLIS, MN 55455 USA
[2] UNIV TOKYO, FAC ENGN, DEPT APPL CHEM, BUNKYO KU, TOKYO 113, JAPAN
关键词
oxidative dehydrogenation; catalytic alkane oxidation; olefin production; Pt-Sn catalysts;
D O I
10.1007/BF00806566
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The addition of various metals to Pt-coated ceramic foam monoliths was examined for the autothermal oxidative dehydrogenation of ethane to ethylene at similar to 900 degrees C at contact times of similar to 5 ms. The addition of Sn or Cu to Pt-monoliths enhanced both C2H6 conversions and C2H4 selectivities significantly, giving higher C2H4 yields. No deactivation or volatilization of the catalysts was observed. For Pt-Sn, an increase in the Sn/Pt ratio from 1/1 to 7/1 increased both the conversion and the selectivity. For Pt-Sn (Sn/Pt = 7/1) versus Pt alone the conversion increased by up to 6% and the selectivity up to 5% for an increase in optimal yield from 54.5% with Pt to 58.5% with Pt-Sn. XRD and XPS measurements showed that Pt existed in the form of PtSn and Pt3Sn alloys. The 1/1 Pt-Cu catalyst showed comparable performance, with conversion increasing by 5% and selectivity by 3%. The addition of several other metals to Pt-monoliths decreased both C2H6 conversion and C2H4 selectivity in the order, Sn > Cu > Pt alone> Ag > Mg > Ce > Ni > La > Co. For oxidative dehydrogenation of n-butane and isobutane, Pt-Sn and Pt-Cu also showed higher conversion than Pt.
引用
收藏
页码:181 / 188
页数:8
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