TY - JOUR
T1 - Toward Understanding of Temperature Dependence of an Advanced Ceramic Fuel Cell with Ni0.8Co0.15Al0.05LiO2as an Electrode
AU - Chen, Zhuo
AU - Chen, Gang
AU - Zhang, Rui
AU - Dai, Ruixin
AU - Lv, Xiaohong
AU - Geng, Shujiang
N1 - Publisher Copyright:
©
PY - 2021/8/23
Y1 - 2021/8/23
N2 - Ceramic fuel cells with Gd0.1Ce0.9O1.95 (GDC) as an electrolyte and Ni0.8Co0.15Al0.05LiO2 (NCAL)-coated foam Ni as a symmetric electrode are prepared. The effect of initial reduction temperature of the NCAL anode on the performance of the cells is investigated. When the initial test temperatures of the three cells were 550, 500, and 450 °C, respectively, the maximum power densities of the three cells at 450 °C were 0.221, 0.125, and 0.02 W·cm-2, respectively. At 450 °C, the ionic conductivities of the electrolytes in the cells with three different initial reduction temperatures were 0.288 (550 °C), 0.165 (500 °C), and 0.011 S·cm-1 (450 °C), respectively. During the test, LiOH/Li2CO3 produced by H2 reduction of the NCAL anode diffuses into the GDC electrolyte, and the interface between LiOH/Li2CO3 and GDC becomes the main channel of ion conduction. The scanning electron microscopy, X-ray photoelectron spectroscopy, Fourier transform infrared spectroscopy, and X-ray diffraction results indicated that the amount and the diffusion rate of the LiOH/Li2CO3 mixture diffused into the GDC electrolyte increased with the increase of initial reduction temperature. The LiOH/Li2CO3 mixture entering into the electrolyte will directly affect the effective area or the length of the ion conduction channel formed by the LiOH/Li2CO3 mixture and GDC in the electrolyte, thus significantly affecting the electrochemical performance of the cells.
AB - Ceramic fuel cells with Gd0.1Ce0.9O1.95 (GDC) as an electrolyte and Ni0.8Co0.15Al0.05LiO2 (NCAL)-coated foam Ni as a symmetric electrode are prepared. The effect of initial reduction temperature of the NCAL anode on the performance of the cells is investigated. When the initial test temperatures of the three cells were 550, 500, and 450 °C, respectively, the maximum power densities of the three cells at 450 °C were 0.221, 0.125, and 0.02 W·cm-2, respectively. At 450 °C, the ionic conductivities of the electrolytes in the cells with three different initial reduction temperatures were 0.288 (550 °C), 0.165 (500 °C), and 0.011 S·cm-1 (450 °C), respectively. During the test, LiOH/Li2CO3 produced by H2 reduction of the NCAL anode diffuses into the GDC electrolyte, and the interface between LiOH/Li2CO3 and GDC becomes the main channel of ion conduction. The scanning electron microscopy, X-ray photoelectron spectroscopy, Fourier transform infrared spectroscopy, and X-ray diffraction results indicated that the amount and the diffusion rate of the LiOH/Li2CO3 mixture diffused into the GDC electrolyte increased with the increase of initial reduction temperature. The LiOH/Li2CO3 mixture entering into the electrolyte will directly affect the effective area or the length of the ion conduction channel formed by the LiOH/Li2CO3 mixture and GDC in the electrolyte, thus significantly affecting the electrochemical performance of the cells.
KW - ceramic fuel cell
KW - ionic conductivity
KW - LiOH/LiCO
KW - molten salt
KW - NiCoAlLiOanode
UR - http://www.scopus.com/inward/record.url?scp=85113699312&partnerID=8YFLogxK
U2 - 10.1021/acsaem.1c01613
DO - 10.1021/acsaem.1c01613
M3 - Article
AN - SCOPUS:85113699312
SN - 2574-0962
VL - 4
SP - 8386
EP - 8394
JO - ACS Applied Energy Materials
JF - ACS Applied Energy Materials
IS - 8
ER -