Study of steam electrolysis using a microtubular ceramic reactor

被引:32
作者
Hashimoto, S. [1 ]
Liu, Y. [1 ]
Mori, M. [1 ]
Funahashi, Y. [2 ]
Fujishiro, Y.
机构
[1] CRIEPI, Kanagawa 2400196, Japan
[2] AIST, FCRA, Moriyama Ku, Nagoya, Aichi 4638561, Japan
关键词
Steam electrolysis; Reversible cell operation; Hydrogen production; SOEC; Waste heat utilization; MICRO-TUBULAR SOFCS; HYDROGEN-PRODUCTION; PERFORMANCE; FABRICATION; OPERATION;
D O I
10.1016/j.ijhydene.2008.11.037
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
Steam electrolysis was carried out using a microtubular ceramic reactor with the following cell configuration: La0.6Sr0.4CO0.2Fe0.8O3-delta (LSCF)-Ce0.8Gd0.2O1.9 (CGO) electrode/CGO buffer layer/(ZrO2)(0.89)(SC2O3)(0.1)(CeO2)(0.01) (ScSZ) electrolyte/Ni-ScSZ electrode supporting tube. 10% H-2/Ar gas was used as steam carrier gas, and 18% steam was supplied to the ceramic reactors. The cell performance was as follows: 1.43 V at 0.1 A cm(-2) and 650 degrees C (Area specific resistance: 4.7 Omega cm(2)) or 1.37 V at 0.1 A cm(-2) and 700 degrees C (4.3 Omega cm(2)). During steam electrolysis, hydrogen production proportionally increased with current density according to Faraday's law, and heat generation at a low current density was observed by an electrochemical technique. Voids and Zr diffusion from the ScSZ electrolyte were confirmed in the CGO buffer layer. Such factors near the surface probably influenced the increase in ohmic loss and electrode polarization. (C) 2008 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:1159 / 1165
页数:7
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