| Integer | N (from Stack) | 10 | Number of volumes of each channel |
| Integer | Nseries (from Stack) | 1 | Number of modules connected in series to build a stack of SOFCs |
| Integer | NparallelFluid (from Stack) | 1 | Number of modules in fluid dynamic parallel |
| Integer | nX (from Stack) | 10 | Number of species in the fluid model |
| Boolean | constantDiffusion (from Stack) | false | True if diffusion coefficient for concnetration losses should be considered constant |
| Boolean | leak (from Stack) | false | True if a linear loss proportional to the current should be included to introduce a fuel leakeage effect |
| Boolean | nonLinConc (from Stack) | true | True if concentration losses should be considered as non linear |
| Boolean[N] | initialEquation (from Stack) | fill(true, N) | If True |
| Types.SpecificHeatCapacity | cmPEN (from Stack) | 400 | Specific heat capacity of the PEN |
| Types.SpecificHeatCapacity | cmPlate (from Stack) | 500 | Specific heat capacity of the interconnecting plate |
| Types.MolarEnergy | Eanode (from Stack) | | Anodic energy of activation for activation loss |
| Types.MolarEnergy | Ecathode (from Stack) | | Cathodic energy of activation for activation loss |
| Types.SpecificConductivityArea | kAnode (from Stack) | | Pre-exponential factor for anodic activation loss |
| Types.SpecificConductivityArea | kCathode (from Stack) | | Pre-exponential factor for cathodic activation loss |
| Types.PerUnit | porosity (from Stack) | | Porosity coefficient for anode and cathode electrodes |
| Types.Density | rhoPEN (from Stack) | 6600 | PEN density |
| Types.Density | rhoPlate (from Stack) | 8000 | Interconnecting plate density |
| Types.SpecificConductivityLength | preExp (from Stack) | 3.34e4 | Pre-exponential factor for the evaluation of membrane conductivity (original = 3.34e4) |
| Types.ElCurrent[N] | iPENmax (from Stack) | zeros(N) | Max current for each volume for leakage losses |
| Types.ElPotential | vLeak0 (from Stack) | 0 | Leakage loss at zero current |
| Types.Length | H (from Stack) | 1e-3 | Channel height |
| Types.Length | W (from Stack) | 0.05 | Channel width |
| Types.Length | totLength (from Stack) | 0.05 | Channel total length |
| Types.Length | tauAE (from Stack) | 400e-6 | Anode electrode thickness |
| Types.Length | tauCE (from Stack) | 16e-6 | Cathode electrode thickness |
| Types.Length | tauSE (from Stack) | 4e-6 | Solid electrolyte thickness |
| Types.Length | tauI (from Stack) | 3e-3 | Interconnecting plate thickness |
| Modelica.Units.SI.FaradayConstant | F (from Stack) | Modelica.Constants.F | Faraday constant C/mol |
| Types.Temperature | T_start (from Stack) | 1000 | General start temperature |
| Types.Pressure | p_start (from Stack) | 27.5e5 | |
| Types.Density | rho_start (from Stack) | 0.22 | |
| Types.CurrentDensity | j_start (from Stack) | 1.5 | |
| Types.CurrentDensity | j0Anode_start (from Stack) | 15000 | |
| Types.CurrentDensity | j0Cathode_start (from Stack) | 6000 | |
| Types.MassFlowRate | w_start (from Stack) | 1e-6 | |
| Types.Temperature[N + 1] | T_start_Anode (from Stack) | {T_start for i in 1:N + 1} | |
| Types.Temperature[N + 1] | T_start_Cathode (from Stack) | {T_start for i in 1:N + 1} | |
| Types.Temperature[N] | T_start_PEN (from Stack) | {T_start for i in 1:N} | |
| Types.Temperature[N] | T_start_Plate_Anode (from Stack) | {T_start for i in 1:N} | |
| Types.Temperature[N] | T_start_Plate_Cathode (from Stack) | {T_start for i in 1:N} | |
| Types.PerUnit[N + 1,nX] | X_start_Anode (from Stack) | ones(N + 1, nX)/nX | |
| Types.PerUnit[N + 1,nX] | X_start_Cathode (from Stack) | ones(N + 1, nX)/nX | |
| Types.Pressure[N] | p_start_Anode (from Stack) | ones(N)*p_start | |
| Types.Pressure[N] | p_start_Cathode (from Stack) | ones(N)*p_start | |
| Types.Density[N + 1] | rho_start_Anode (from Stack) | ones(N + 1)*rho_start | |
| Types.Density[N + 1] | rho_start_Cathode (from Stack) | ones(N + 1)*rho_start | |
| Types.MassFlowRate[N + 1] | w_start_Anode (from Stack) | ones(N + 1)*w_start | |
| Types.MassFlowRate[N + 1] | w_start_Cathode (from Stack) | ones(N + 1)*w_start | |
| Types.CurrentDensity[N] | j_startPEN (from Stack) | ones(N)*j_start | |
| Types.CurrentDensity[N] | j0Anode_startPEN (from Stack) | ones(N)*j0Anode_start | |
| Types.CurrentDensity[N] | j0Cathode_startPEN (from Stack) | ones(N)*j0Cathode_start | |
| Types.Pressure | p_start_homotopy_cathode_in (from Stack) | p_start_Cathode[1] | |
| Types.Pressure | p_start_homotopy_anode_in (from Stack) | p_start_Anode[1] | |
| Types.Pressure | p_start_homotopy_cathode_out (from Stack) | p_start_Cathode[end] | |
| Types.Pressure | p_start_homotopy_anode_out (from Stack) | p_start_Anode[end] | |
| Types.Temperature | T_start_homotopy_cathode_in (from Stack) | T_start_Cathode[1] | |
| Types.Temperature | T_start_homotopy_anode_in (from Stack) | T_start_Anode[1] | |
| Types.Temperature | T_start_homotopy_cathode_out (from Stack) | T_start_Cathode[end] | |
| Types.Temperature | T_start_homotopy_anode_out (from Stack) | T_start_Anode[end] | |
| Types.MassFraction[nX] | X_start_homotopy_cathode_in (from Stack) | X_start_Cathode[1, :] | |
| Types.MassFraction[nX] | X_start_homotopy_anode_in (from Stack) | X_start_Anode[1, :] | |
| Types.MassFraction[nX] | X_start_homotopy_cathode_out (from Stack) | X_start_Cathode[end, :] | |
| Types.MassFraction[nX] | X_start_homotopy_anode_out (from Stack) | X_start_Anode[end, :] | |
| Types.Pressure | deltapNomAnode (from Stack) | | |
| Types.Pressure | deltapNomCathode (from Stack) | | |
| Types.Efficiency | etaDCAC (from Stack) | 0.98 | |
| Types.MolarMass[10] | MM (from Stack) | DiffusionLosses.Utilities.ConstantsFluidAndSolid.MM | |
| Real | QlossFrac (from Stack) | 0 | |
