diff --git a/examples/soec_syngas.md b/examples/soec_syngas.md
new file mode 100644
index 0000000..a1f834e
--- /dev/null
+++ b/examples/soec_syngas.md
@@ -0,0 +1,117 @@
+# SOEC Co-Electrolysis
+
+This example shows a 1D isothermal SOEC (Solid oxide electrolyzer cell) model.
+Converting CO2 and H2 into syngas.
+
+The operating parameters chosen here are not necessary realistic. Under the example
+condition the formation of solid carbon is very likely.
+
+```python
+import gaspype as gp
+from gaspype.constants import R, F
+import numpy as np
+import matplotlib.pyplot as plt
+```
+
+Calculation of the local equilibrium compositions on the fuel and air
+side in counter flow along the fuel flow direction:
+```python
+utilization = 0.95
+air_dilution = 0.2
+t = 700 + 273.15  # K
+p = 1e5  # Pa
+
+fs = gp.fluid_system('H2, H2O, O2, CH4, CO, CO2')
+feed_fuel = gp.fluid({'H2O': 2, 'CO2': 1}, fs)
+
+o2_full_conv = np.sum(gp.elements(feed_fuel)[['C' ,'O']] * [-1/2, 1/2])
+
+feed_air = gp.fluid({'O2': 1, 'N2': 4}) * o2_full_conv * utilization * air_dilution
+
+conversion = np.linspace(0, utilization, 128)
+perm_oxygen = o2_full_conv * conversion * gp.fluid({'O2': 1})
+
+fuel_side = gp.equilibrium(feed_fuel - perm_oxygen, t, p)
+air_side  = gp.equilibrium(feed_air  + perm_oxygen, t, p)
+```
+
+Plot compositions of the fuel and air side:
+```python
+fig, ax = plt.subplots()
+ax.set_xlabel("Conversion")
+ax.set_ylabel("Molar fraction")
+ax.plot(conversion, fuel_side.get_x(), '-')
+ax.legend(fuel_side.species)
+
+fig, ax = plt.subplots()
+ax.set_xlabel("Conversion")
+ax.set_ylabel("Molar fraction")
+ax.plot(conversion, air_side.get_x(), '-')
+ax.legend(air_side.species)
+```
+
+Calculation of the oxygen partial pressures:
+```python
+o2_fuel_side = gp.oxygen_partial_pressure(fuel_side, t, p)
+o2_air_side = air_side.get_x('O2') * p
+```
+
+Plot oxygen partial pressures:
+```python
+fig, ax = plt.subplots()
+ax.set_xlabel("Conversion")
+ax.set_ylabel("Oxygen partial pressure / Pa")
+ax.set_yscale('log')
+ax.plot(conversion, np.stack([o2_fuel_side, o2_air_side], axis=1), '-')
+ax.legend(['o2_fuel_side', 'o2_air_side'])
+```
+
+Calculation of the local nernst potential between fuel and air side:
+```python
+z_O2 = 4
+nernst_voltage = R*t / (z_O2*F) * np.log(o2_air_side/o2_fuel_side)
+```
+
+Plot nernst potential:
+```python
+fig, ax = plt.subplots()
+ax.set_xlabel("Conversion")
+ax.set_ylabel("Voltage / V")
+ax.plot(conversion, nernst_voltage, '-')
+print(np.min(nernst_voltage))
+```
+
+The model uses between each node a constant conversion. Because
+current density depends strongly on the position along the cell
+the constant conversion does not relate to a constant distance.
+
+![Alt text](../../media/soc_inverted.svg)
+
+To calculate the local current density (**node_current**) as well
+as the total cell current (**terminal_current**) the (relative)
+physical distance between the nodes (**dz**) must be calculated:
+```python
+cell_voltage = 1.3  # V
+ASR = 0.2  # Ohm*cm²
+
+node_current = (nernst_voltage - cell_voltage) / ASR  # mA/cm² (Current density at each node)
+
+current = (node_current[1:] + node_current[:-1]) / 2  # mA/cm² (Average current density between the nodes)
+
+dz = 1/current / np.sum(1/current)  # Relative distance between each node
+
+terminal_current = np.sum(current * dz) # mA/cm² (Total cell current per cell area)
+
+print(f'Terminal current: {terminal_current:.2f} A/cm²')
+```
+
+Plot the local current density:
+```python
+z_position = np.concatenate([[0], np.cumsum(dz)])  # Relative position of each node
+
+fig, ax = plt.subplots()
+ax.set_xlabel("Relative cell position")
+ax.set_ylabel("Current density / A/cm²")
+ax.plot(z_position, node_current, '-')
+```
+
diff --git a/examples/soec_methane.md b/examples/sofc_methane.md
similarity index 91%
rename from examples/soec_methane.md
rename to examples/sofc_methane.md
index 55e6576..0f643ce 100644
--- a/examples/soec_methane.md
+++ b/examples/sofc_methane.md
@@ -1,8 +1,8 @@
-# SOEC with Methane
+# SOFC with Methane
 
-This example shows a 1D isothermal SOEC (Solid oxide electrolyzer cell) model.
+This example shows a 1D isothermal SOFC (Solid oxide fuel cell) model.
 
-The operating parameters chosen here are not necessary realistic
+The operating parameters chosen here are not necessary realistic.
 
 ```python
 import gaspype as gp
@@ -16,15 +16,15 @@ side in counter flow along the fuel flow direction:
 ```python
 fuel_utilization = 0.90
 air_utilization = 0.5
-t = 800 + 273.15 #K
-p = 1e5 #Pa
+t = 800 + 273.15  # K
+p = 1e5  # Pa
 
 fs = gp.fluid_system('H2, H2O, O2, CH4, CO, CO2')
 feed_fuel = gp.fluid({'CH4': 1, 'H2O': 0.1}, fs)
 
 o2_full_conv = np.sum(gp.elements(feed_fuel)[['H', 'C' ,'O']] * [1/4, 1, -1/2])
 
-feed_air = gp.fluid({'O2': 1, 'N2': 4}) * o2_full_conv / air_utilization
+feed_air = gp.fluid({'O2': 1, 'N2': 4}) * o2_full_conv * fuel_utilization / air_utilization
 
 conversion = np.linspace(0, fuel_utilization, 32)
 perm_oxygen = o2_full_conv * conversion * gp.fluid({'O2': 1})
@@ -70,7 +70,7 @@ z_O2 = 4
 nernst_voltage = R*t / (z_O2*F) * np.log(o2_air_side/o2_fuel_side)
 ```
 
-#Plot nernst potential:
+Plot nernst potential:
 ```python
 fig, ax = plt.subplots()
 ax.set_xlabel("Conversion")
@@ -89,8 +89,8 @@ To calculate the local current density (**node_current**) as well
 as the total cell current (**terminal_current**) the (relative)
 physical distance between the nodes (**dz**) must be calculated:
 ```python
-cell_voltage = 0.77 #V
-ASR = 0.2 #Ohm*cm²
+cell_voltage = 0.77  # V
+ASR = 0.2  # Ohm*cm²
 
 node_current = (nernst_voltage - cell_voltage) / ASR  # mA/cm² (Current density at each node)