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the electrolyte and seals, and high pressure favors carbon deposition and methane formation in the fuel gas. Reactant Utilization and Gas Composition: Reactant utilization and gas composition have major impacts on fuel cell efficiency. It is apparent from the Nernst equations in Table 2-2 that fuel and oxidant gases containing higher partial pressures of electrochemical reactants produce a higher cell voltage. Utilization (U) refers to the fraction of the total fuel or oxidant introduced into a fuel cell that reacts electrochemically. In low-temperature fuel cells, determining the fuel utilization is relatively straightforward when H2 is the fuel, because it is the only reactant involved in the electrochemical reaction,4 i.e. Uf = H2,in − H2,out = H2,consumed (2-40) H2,in H2,in where H2,in and H2,out are the flow rates of H2 at the inlet and outlet of the fuel cell, respectively. However, hydrogen can be consumed by various other pathways, such as by chemical reaction (i.e., with O2 and cell components) and loss via leakage out of the cell. These pathways increase the apparent utilization of hydrogen without contributing to the electrical energy produced by the fuel cell. A similar type of calculation is used to determine the oxidant utilization. For the cathode in MCFCs, two reactant gases, O2 and CO2, are utilized in the electrochemical reaction. The oxidant utilization should be based on the limiting reactant. Frequently O2, which is readily available from make-up air, is present in excess, and CO2 is the limiting reactant. A significant advantage of high-temperature fuel cells such as MCFCs is their ability to use CO as a fuel. The anodic oxidation of CO in an operating MCFC is slow compared to the anodic oxidation of H2; thus, the direct oxidation of CO is not favored. However, the water gas shift reaction CO+H2OoH2 +CO2 (2-41) reaches equilibrium rapidly in MCFCs at temperatures as low as 650°C (1200°F) to produce H2.5 As H2 is consumed, the reaction is driven to the right because both H2O and CO2 are produced in equal quantities in the anodic reaction. Because of the shift reaction, fuel utilization in MCFCs can exceed the value for H2 utilization, based on the inlet H2 concentration. For example, for an anode gas composition of 34% H2, 22% H2O, 13% CO, 18% CO2, and 12% N2, a fuel utilization of 80% (i.e., equivalent to 110% H2 utilization) can be achieved even though this would require 10% more H2 (total of 37.6%) than is available in the original fuel. The high fuel utilization is possible because the shift reaction provides the necessary additional H2 that is oxidized at the anode. In this case, the fuel utilization is defined by 4. Assumes no gas cross-over or leakage out of the cell. 5. Example 9-5 in Section 9 illustrates how to determine the amount of H2 produced by the shift reaction. 2-21PDF Image | Fuel Cell Handbook (Seventh Edition)
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