“…The simulation is developed under the assumption of thermo-neutral conditions [54,64,79]; • at the cathode outlet of the stack, there is always a mixture of steam and hydrogen because the steam conversion in the stack is lower than 100%, therefore the yield of conversion of steam into hydrogen is fixed at 75% [54,64]; • SOEC is supposed as an isothermal steady-state system [54,62,80]; • a fraction of the cathode outlet flow is recirculated to the cathode inlet in order to exploit the hydrogen capacity of counteracting undesired oxidation of the electrodes by the action of pure steam and to preheat the fresh inlet stream [45,54,62,81,82]; • at the cathode, the flash unit is fed with steam and recycled hydrogen. At the anode, the formation of oxygen is ensured by the recombination of the oxide anions, produced on the cathode and transported through the solid electrolyte [50,83]; and • perfect thermal insulation on the stack is considered and heat losses toward the environment are neglected [54].…”