“…The cathode exhaust gases contain a large amount of thermal energy which is used for preheating the inlet air stream and supplying the steam needed by the reformer, because the overall temperature of the FC should maintain constant and also the temperature of the reactants is lower than the needed working temperature by the FC. The performance of MCFCs from different points of view and in more detail are studied in Refs 30,39,41,47,48,51. Anode potential (U an ), cathode potential (U cat ), ohm overpotential (U ohm ), and theoretical maximum potential (U t ) of MCFC can be calculated as follows, respectively 91 : where, j is the current density, p H 2 , an is the partial pressure of hydrogen at the anode, p CO 2 , an is the partial pressure of carbon dioxide at the anode, p H 2 O, an is the partial pressure of water at the anode, p O 2 , cat is the partial pressure of oxygen at the cathode, p CO 2 , cat is the partial pressure of carbon dioxide at the cathode, R is the universal gas constant, T is the operating temperature of the MCFC, En act is the activation energy, F is the Faraday constant, n e is the number of electrons, and U i is the ideal standard potential.…”