Oxidative Coupling of Methane over Hybrid Membrane/Catalyst Active Centers: Chemical Requirements for Prolonged Lifetime

被引:18
|
作者
Igenegbai, Valentina Omoze [1 ,2 ]
Almallahi, Rawan [1 ,2 ]
Meyer, Randall J. [3 ]
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] ExxonMobil Res & Engn Co, Corp Strateg Res, Annandale, NJ USA
基金
美国国家科学基金会;
关键词
MEMBRANE REACTOR; CERAMIC MEMBRANE; GAS-PHASE; OXIDE; PERFORMANCE; CONVERSION; STABILITY;
D O I
10.1021/acsenergylett.9b01075
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
Solid oxide membrane/catalyst hybrid systems have been proposed as a promising platform for selective oxidative coupling of methane to form higher value C2+ products. In these hybrid systems, the membrane controls the local chemical potential of reacting oxygen atoms while the catalyst allows for selective reaction of these oxygen atoms with methane to form the desired C-2 products. One critical challenge with these systems is that due to relatively low local O-2/CH4 ratios, they can promote carbon-induced catalyst deactivation. Herein, we demonstrate that a BaCe0.8Gd0.2O3-delta based membrane/catalyst system can achieve excellent carbon resistance at low O-2/CH4 ratios, and high and stable selectivity (over 80%) to C2+ products (ethane, ethylene, propane, and propylene). Our analysis of the system suggests that its high carbon resistance is due to its relatively high oxygen storage/release capacity which suppresses carbon deposition in the system.
引用
收藏
页码:1465 / 1470
页数:11
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