Approaching Sustainable H2 Production: Sorption Enhanced Steam Reforming of Ethanol

被引:86
作者
He, Li [1 ]
Berntsen, Helene [1 ]
Chen, De [1 ]
机构
[1] Norwegian Univ Sci & Technol, Dept Chem Engn, NO-7491 Trondheim, Norway
关键词
HYDROGEN-PRODUCTION; FLUIDIZED-BED; THERMODYNAMIC ANALYSIS; HIGH-TEMPERATURE; CARBON-DIOXIDE; CALCIUM-OXIDE; BIO-ETHANOL; CO2; METHANE; DOLOMITE;
D O I
10.1021/jp906146y
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
Sorption enhanced steam reforming of ethanol (SESRE), featured by yielding high purity of H-2, from one single reaction unit, is a new reaction process with a great potential for realizing sustainable H, production. The potential of such process with a CaO-based acceptor has been assessed by thermodynamic analysis and experimental demonstration. As predicted, ethanol call be reformed at relatively low temperatures (500-600 degrees C), still yielding high-quality H-2. Another major advantage Of Coupling CO, capture to the reforming process is predicted to De low risk ill carbon formation. The SESRE reaction was carried out over a mixture of hydrotalcite-like material derived Co-Ni catalysts (Co-Ni/HTls) and calcined dolomite with a steam to carbon (S/C) ratio of 3 and temperatures ranging from 500 to 650 degrees C. The chosen reaction system was able to yield H-2, with purity fairly Close to the theoretical prediction. Particularly, the best result was obtained over 40Ni and 20Co-20Ni/HTls at 550 degrees C, where the product gas had composition of more than 99 mol % H-2 ca. 0.4 mol % CH4, 0.1 mol % CO, and 0.2 mol % CO2. Special emphasis was put Oil file effect of steam Oil file stability of the CO, acceptor during the SESRE reaction. Hydration Of CaO in the acceptor did not cause appreciable induction period, even at the low operating temperatures. However, different from a test Under dry atmosphere (CO2/argon), the acccptor showed rapid deactivation ill a multicycle operation of SESRE. A similar deactivation tend was given by a comparative test in a steam/CO2/Ar atmosphere.
引用
收藏
页码:3834 / 3844
页数:11
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