A_plate L*D "电池面积"
D 1[m] "电池深度"
d_pore 0.5[um] "电极中的孔隙直径"
da 500[um] "阳极厚度"
dc 100[um] "阴极厚度"
dg 1[mm] "气体流道高度"
di 500[um] "互连层厚度"
din 4*dg "入口区域长度"
dm 100[um] "膜厚度"
epsg 0.4 "电极孔隙率"
epsl 0.4 "电解质体积分数"
I_avg I_avg_init "平均电池电流密度"
I_avg_final 1[A/cm^2] "扫描中的最终平均电流密度"
I_avg_init 0.01[A/cm^2] "扫描中的初始平均电流密度"
I_flow max(I_avg,0.1[A/cm^2])*A_plate "用于化学计量流量计算的总电流"
I_tot I_avg*A_plate "总电池电流"
i0_ref_H2 1[A/m^2] "氢氧化反应的参考交换电流密度"
i0_ref_O2 1[A/m^2] "氧还原反应的参考交换电流密度"
j_N2_cath j_O2_cath*x0_N2_cath/x0_O2_cath "氮摩尔流率"
j_NH3_an stoich_NH3*I_flow/(3*F_const) "氨摩尔流率"
j_O2_cath stoich_O2*I_flow/(4*F_const) "氧摩尔流率"
ka 11[W/m/K] "阳极导热系数"
kappag_GDE 1e-10[m^2] "气体渗透率，气体扩散电极"
kc 6[W/m/K] "阴极导热系数"
ki 1.1[W/m/K] "互连层导热系数"
km 2.7[W/m/K] "电解质导热系数"
L 20[mm] "平面 SOEC 长度"
M_aux RelMolecularMass_ammonia12 "氨摩尔质量"
m_cath m_O2_cath+m_N2_cath "阴极总质量流率"
m_N2_cath j_N2_cath*28[g/mol] "氮质量流率"
m_NH3_an j_NH3_an*17[g/mol] "氨质量流速"
m_O2_cath j_O2_cath*32[g/mol] "氧质量流率"
nu_aux FullerDiffusionVolume_ammonia11 "氨富勒扩散体积"
S 1e8[m^2/m^3] "电极比表面积"
stoich_NH3 1.25 "氨流量的化学计量"
stoich_O2 4 "氧流量的化学计量"
T_in 973[K] "工作温度"
Tb_aux NormalBoilingPointTemperature_ammonia13 "氨的沸点温度"
taug 3 "电极迂曲度"
W 3.7[mm] "平面 SOEC 厚度"
w0_N2_cath x0_N2_cath*28[g/mol]/(x0_N2_cath*28[g/mol]+x0_O2_cath*32[g/mol]) "入口处 N2 的初始质量分数"
w0_NH3_an 0.95 "入口处 NH3 的初始质量分数"
w0_N2_an 0.01 "入口处 N2 的初始质量分数"
w0_H2O_an 0.01 "入口处 H2O 的初始质量分数"
x0_H2_an 1-x0_N2_an-x0_H2O_an-x0_NH3_an "H2 的初始摩尔分数"
x0_H2O_an 0.0001 "H2O 的初始摩尔分数"
x0_N2_an 0.7498 "N2 的初始摩尔分数"
x0_N2_cath 0.79 "N2 的初始摩尔分数"
x0_NH3_an 0.0001 "NH3 初始摩尔分数"
x0_O2_cath 1-x0_N2_cath "O2 的初始摩尔分数"