期刊
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY
卷 34, 期 2, 页码 844-858出版社
PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ijhydene.2008.10.057
关键词
Anodic alumina support; CH4; Nickel catalyst; Steam reforming; Spinel; Porous anodic alumina; Electrical heating
A plate-type alumina support was synthesized through a novel anodization technology followed by a hot water treatment, which resulted in the drastically enlargement of support BET surface area from 16.5 to 204.6 g/m(2), and such BET value is even comparable to some commercial alumina supports. A high thermal stability of this kind of porous anodic alumina support was shown because as much as 63% of surface area remained after the support subjected to 700 degrees C air calcination for 50 h. Innovatively, an electrical heating pattern was allowed over this plate support due to the existence of Fe-Cr-Ni alloy interlayer among the support. Our work showed that the utilization of electrical heating pattern would shorten the reformer start-up time from 1 to 2 h to just a few minutes. With the porous anodic alumina support, a 17.9-wt% Ni catalyst with nickel aluminate layer was synthesized and its reforming reactivity was investigated during stationary and DSS SRM at 700 degrees C, under usual and electrical heating pattern. It showed excellent SRM reactivity and no deactivation was evidenced during 500 h stationary test and 100 times start-stop cycles DSS SRM test. Nevertheless, for the industrialization, some efforts should be made to alleviate the sintering of anodic supports, because after subjected to a hydrothermal treatment at 700 degrees C for 50 h, only 36% of surface area was kept. (C) 2008 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
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