Hydrogen production performance of a 10-cell planar solid-oxide electrolysis stack

被引:97
作者
O'Brien, J. E. [1 ]
Stoots, C. M.
Herring, J. S.
Hartvigsen, J.
机构
[1] Idaho Natl Lab, Idaho Falls, ID 83415 USA
[2] Ceramatec Inc, Salt Lake City, UT 84037 USA
来源
JOURNAL OF FUEL CELL SCIENCE AND TECHNOLOGY | 2006年 / 3卷 / 02期
关键词
D O I
10.1115/1.2179435
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
An experimental study is under way to assess the performance of solid-oxide cells operating in the steam electrolysis mode for hydrogen production over a temperature range of 800-900 degrees C. Results presented in this paper were obtained from a ten-cell planar electrolysis stack, with an active area of 64 cm 2 per cell. The electrolysis cells are electrolyte supported, with scandia-stabilized zirconia electrolytes ( similar to 140 mu m thick), nickel-cermet steam/hydrogen electrodes, and manganite air-side electrodes. The metallic interconnect plates are fabricated from ferritic stainless steel. The experiments were performed over a range of steam inlet mole fractions (0.1-0.6), gas flow rates (1000-4000 seem), and current densities (0-0.38 A/cm(2)). Steam consumption rates associated with electrolysis were measured directly using inlet and outlet dewpoint instrumentation. Cell operating potentials and cell current were varied using a programmable power supply. Hydrogen production rates up to 100 Nl/h were demonstrated. Values of area-specific resistance and stack internal temperatures are presented as a function of current density. Stack performance is shown to be dependent on inlet steam flow rate.
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页码:213 / 219
页数:7
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