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PEM-Based System Fuel Preparation Air Preparation Reforming Sulfur Removal Steam Generation Water-Gas Shift CO clean-up Balance of Plant: • Compressor/Expander • Pumps • Controls • Water management • Packaging • Safety system • Start-up battery Fuel Cell Stack Balance of Plant: • Compressor/Expander • Pumps • Controls • Insulation & Packaging • Safety system • Start-up battery Air Preparation Reformate Conditioning Sulfur removal Fuel Preparation Fuel pre- processing Fuel Cell Stack SOFC-Based System Figure 1-11. Overview of subsystems and components for SOFC and PEFC systems Figure 1-12 shows a simplified layout for an SOFC-based APU. The air for reformer operation and cathode requirements is compressed and then split between the unit operations. The external water supply shown in Figure 1-12 will most likely not be needed; the anode recycle stream provides water. Unreacted anode tail gas is recuperated in a tail gas burner. Additional energy is available in a SOFC system from enthalpy recovery from tail gas effluent streams that are typically 400-600 °C. Current thinking is that reformers for transportation fuel based SOFC APUs will be of the exothermic type (i.e. partial oxidation or autothermal reforming), as no viable steam reformers are available for such fuels. 1-28PDF Image | Fuel Cell Handbook (Seventh Edition)
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