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292             Renewable Energy Devices and Systems with Simulations in MATLAB  and ANSYS ®
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            12.1  FUEL CELL TYPES AND OPERATION
            Fuel cells are modular, environmentally clean, sustainable, efficient, and of a versatile technology.
            Fuel cell systems have been demonstrated for clean energy, transportation, and various other appli-
            cations. A fuel cell is a device that generates electricity by a chemical reaction. It has two electrodes,
            an anode and a cathode, with an electrolyte sandwiched between them. Hydrogen is the basic fuel
            for fuel cells, and exposing the anode to hydrogen and the cathode to oxygen derived from air
            results in electricity being produced without combustion of any form. Water and heat are the only
            by-products when pure hydrogen is used as the fuel source. Although hydrogen is considered the
            primary fuel source for fuel cells, the process of fuel reforming allows for the extraction of hydrogen
            from other fuels including methanol, natural gas, petroleum, or renewable hydrocarbon sources.
            The first fuel cell was developed in 1839 by Sir William Grove, a Welsh judge and a scientist [1].
            Fuel cells are generally classified according to the nature of the electrolyte, each type requiring a
            particular type of electrolyte material. Also, each fuel cell type has its own unique characteristics
            and merits for a given application [1–3]. Table 12.1 lists different fuel cells, operating temperature,
            and electrical efficiency range.


            12.1.1  PEMFC
            The heart of the proton exchange membrane fuel cell (PEMFC) is the proton-conducting solid poly-
            mer electrolyte membrane in the form of a thin, permeable sheet. It is surrounded by two layers: a
            diffusion and a reaction layer. Under constant supply of hydrogen and oxygen, the hydrogen dif-
            fuses through the porous anode and diffusion layer up to the platinum catalyst. The reason for the
            diffusion current is the tendency of hydrogen–oxygen reaction. In the reaction layer supported by
            the catalyst and at a temperature of about 80 °C–100 °C, protons and electrons split as represented
                      +
                          −
            by H  → 2H  + 2e .
                2
              The hydrogen ion passes through the polymer membrane on its way to the cathode, while the
            only possible way for the electrons is through an outer circuit. At the three-phase boundary between
            cathode and electrolyte, the hydrogen ions react with the oxygen, which has diffused through the
            porous cathode and the electrons from the outer electrical circuit, to form water. The resultant reac-
                              −
                    +
            tion is 2H  + ½O  + 2e  → H O. Excess airflow on the cathode side helps to remove the water result-
                                   2
                         2
            ing from the reaction. The overall fuel cell reaction is 2H  + O  → 2H O + heat.
                                                                    2
                                                         2
                                                              2
            TABLE 12.1
            Fuel Cell Technologies
                           Proton Exchange   Solid Oxide   Molten Carbonate   Phosphoric   Alkaline
                          Membrane Fuel Cell  Fuel Cell   Fuel Cell   Acid Fuel Cell  Fuel Cell
            Fuel            H 2           H 2 , CO, CH 4 ,   H 2 , CO, CH 4 ,   H 2  H 2
                                           hydrocarbons  hydrocarbons
            Electrolyte     Solid polymer   Solid oxide   Lithium and   Phosphoric acid   Potassium
                            (usually Nafion)  (yttria,   potassium    (H 3 PO 4     hydroxide
                                           zirconia)     carbonate    solution)     (KOH)
            Charge carried in   H +       O 2−          CO 3 2−       H +          OH −
             electrolyte
            Operating       80–100        800–1000      650           175–200      80–120
             temperature (°C)
            Electrical      35–50         50–60         45–55         35–45        35–55
             efficiency (%)
   300   301   302   303   304   305   306   307   308   309   310