Selective and Stable In-Promoted Fe Catalyst for Syngas Conversion to Light Olefins

被引:13
|
作者
He, Yang [1 ]
Shi, Hanzhong [1 ]
Johnson, Olusola [1 ]
Joseph, Babu [1 ]
Kuhn, John N. [1 ]
机构
[1] Univ S Florida, Dept Chem Biol & Mat Engn, Tampa, FL 33620 USA
关键词
FTS; In-promoted Fe catalysts; limited hydrogenation ability; light olefin production; limited CO2 activation; SSITKA; FISCHER-TROPSCH SYNTHESIS; PARTICLE-SIZE; PROPANE DEHYDROGENATION; INTERMETALLIC COMPOUNDS; BIMETALLIC CATALYSTS; SURFACE REACTIVITIES; ETHYLENE ADSORPTION; CARBON-DIOXIDE; SYNTHESIS GAS; NANOPARTICLES;
D O I
10.1021/acscatal.1c04334
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
A selective and stable alumina-supported In-promoted Fe catalyst (10 mol % In based on Fe) was discovered for converting syngas (2:1 H-2/CO ratio) to olefins with high selectivity (45% with CO2 included) and a remarkable stability (72 h run) at a CO conversion of 10% at 400 degrees C and 5 bar. The X-ray photoelectron spectroscopy results indicated that incorporating In into Fe catalysts changed the chemical bonding state of Fe and Fe/In composition near the surface layers, which affected the catalytic reactivity. Steady-state isotopic transient kinetic analysis showed that more stable CHx fragments are present on the catalyst surface when incorporating In into Fe, which can promote C-C coupling reaction toward olefins. Our study demonstrates that introducing In into Fe catalysts on Al2O3 support can lower CO activation abilities. It has more impacts on lowering hydrogenation activity, which permits more C-C couplings and like of "ene" hydrogenation. Moreover, weakening CO adsorption both in terms of sites and strength encouraged CO toward hydrocarbons rather than CO2.
引用
收藏
页码:15177 / 15186
页数:10
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