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Bifunctional core-shell architecture allows stable H2 production utilizing CH4 and CO2 in a catalytic chemical looping process
被引:42
作者:

Hosseini, Davood
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机构:
Swiss Fed Inst Technol, Dept Mech & Proc Engn, Lab Energy Sci & Engn, Leonhardstr 21, CH-8092 Zurich, Switzerland Swiss Fed Inst Technol, Dept Mech & Proc Engn, Lab Energy Sci & Engn, Leonhardstr 21, CH-8092 Zurich, Switzerland

Abdala, Paula M.
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机构:
Swiss Fed Inst Technol, Dept Mech & Proc Engn, Lab Energy Sci & Engn, Leonhardstr 21, CH-8092 Zurich, Switzerland Swiss Fed Inst Technol, Dept Mech & Proc Engn, Lab Energy Sci & Engn, Leonhardstr 21, CH-8092 Zurich, Switzerland

Donat, Felix
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机构:
Swiss Fed Inst Technol, Dept Mech & Proc Engn, Lab Energy Sci & Engn, Leonhardstr 21, CH-8092 Zurich, Switzerland Swiss Fed Inst Technol, Dept Mech & Proc Engn, Lab Energy Sci & Engn, Leonhardstr 21, CH-8092 Zurich, Switzerland

Kim, Sung Min
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机构:
Swiss Fed Inst Technol, Dept Mech & Proc Engn, Lab Energy Sci & Engn, Leonhardstr 21, CH-8092 Zurich, Switzerland Swiss Fed Inst Technol, Dept Mech & Proc Engn, Lab Energy Sci & Engn, Leonhardstr 21, CH-8092 Zurich, Switzerland

Mueller, Christoph R.
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机构:
Swiss Fed Inst Technol, Dept Mech & Proc Engn, Lab Energy Sci & Engn, Leonhardstr 21, CH-8092 Zurich, Switzerland Swiss Fed Inst Technol, Dept Mech & Proc Engn, Lab Energy Sci & Engn, Leonhardstr 21, CH-8092 Zurich, Switzerland
机构:
[1] Swiss Fed Inst Technol, Dept Mech & Proc Engn, Lab Energy Sci & Engn, Leonhardstr 21, CH-8092 Zurich, Switzerland
基金:
瑞士国家科学基金会;
关键词:
Dry reforming of methane;
Hydrogen;
Bifunctional;
Core-shell;
Chemical looping;
HYDROGEN-PRODUCTION;
IN-SITU;
OXIDE;
FUEL;
GAS;
CONVERSION;
METHANE;
REDISPERSION;
PERFORMANCE;
SUPPORT;
D O I:
10.1016/j.apcatb.2019.117946
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:
We report on the development of a bifunctional catalyst (Pt) - oxygen carrier (Fe2O3) that integrates the dry reforming of methane (DRM) into the chemical looping - based production of hydrogen. The material exhibits a high and stable methane conversion ((similar to)80%) and hydrogen yield (10.8 mmol/g catalyst-oxygen carrier) with only a small quantity of impurities (CO, CO2 < 2 ppm). The structural changes of the material are followed by operando X-ray powder diffraction and X-ray absorption spectroscopy coupled with gas chromatography. Insight into the evolution of the size of the Pt nanoparticles and their interaction with CeO2 are probed by transmission electron microscopy and X-ray absorption fine structure analysis. Under DRM conditions, the Pt nanoparticles grow in size, however, their re-dispersion on the CeO2 support (via PtOx-support interaction) during air oxidation recovers their activity in the consecutive cycle.
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