Highly efficient high temperature electrolysis

被引:350
作者
Hauch, Anne [1 ]
Ebbesen, Sune Dalgaard [1 ]
Jensen, Soren Hojgaard [1 ]
Mogensen, Mogens [1 ]
机构
[1] Tech Univ Denmark, Fuel Cells & Solid State Dept, DK-4000 Roskilde, Denmark
关键词
D O I
10.1039/b718822f
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
High temperature electrolysis of water and steam may provide an efficient, cost effective and environmentally friendly production of H-2 Using electricity produced from sustainable, non-fossil energy sources. To achieve cost competitive electrolysis cells that are both high performing i.e. minimum internal resistance of the cell, and long-term stable, it is critical to develop electrode materials that are optimal for steam electrolysis. In this article electrolysis cells for electrolysis of water or steam at temperatures above 200 degrees C for production of H-2 are reviewed. High temperature electrolysis is favourable from a thermodynamic point of view, because a part of the required energy can be supplied as thermal heat, and the activation barrier is lowered increasing the H-2 production rate. Only two types of cells operating at high temperature (above 200 degrees C) have been described in the literature, namely alkaline electrolysis cells (AEC) and solid oxide electrolysis cells (SOEC). In the present review emphasis is on state-of-the art electrode materials and development of new materials for SOECs. Based on the state-of-the-art performance for SOECs H-2 production by high temperature steam electrolysis using SOECs is competitive to H-2 production from fossil fuels at electricity prices below 0.02-0.03 is an element of per kWh. Though promising SOEC results on H-2 production have been reported a substantial R&D is still required to obtain inexpensive, high performing and long-term stable electrolysis cells.
引用
收藏
页码:2331 / 2340
页数:10
相关论文
共 81 条
  • [21] Hydrogen evolution reaction in alkaline solution - Catalytic influence of Pt supported on graphite vs Pt inclusions in graphite
    Fournier, J
    Brossard, L
    Tilquin, JY
    Cote, R
    Dodelet, JP
    Guay, D
    Menard, H
    [J]. JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1996, 143 (03) : 919 - 926
  • [22] Photoelectrochemical cells
    Grätzel, M
    [J]. NATURE, 2001, 414 (6861) : 338 - 344
  • [23] GUAN J, 2006, DEFC3604 GO14351 DOE
  • [24] Degradation of anode supported SOFCs as a function of temperature and current load
    Hagen, A
    Barfod, R
    Hendriksen, PV
    Liu, YL
    Ramousse, S
    [J]. JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2006, 153 (06) : A1165 - A1171
  • [25] ALKALINE WATER ELECTROLYSIS ANODE MATERIALS
    HALL, DE
    [J]. JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1985, 132 (02) : C41 - C48
  • [26] HALLGEIR O, 1999, NORD WORKSH HYDR EL
  • [27] H2-H2O-Ni-YSZ electrode performance -: Effect of segregation to the interface
    Hansen, KV
    Norrman, K
    Mogensen, M
    [J]. JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2004, 151 (09) : A1436 - A1444
  • [28] Operation of High Temperature Steam Electrolyzer Module
    Hartvigsen, J.
    Elangovan, S.
    O'Brien, J.
    Stoots, C.
    Herring, J.
    [J]. SOLID OXIDE FUEL CELLS 10 (SOFC-X), PTS 1 AND 2, 2007, 7 (01): : 357 - 363
  • [29] HARTVIGSEN J, 2004, P 6 EUR SOL OX FUEL, P378
  • [30] Performance and durability of solid oxide electrolysis cells
    Hauch, A.
    Jensen, S. H.
    Ramousse, S.
    Mogensen, M.
    [J]. JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2006, 153 (09) : A1741 - A1747