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Balance of Plant Stack, insulation and stack ba la nce Controls/ Piping/ Battery Indirect, Labor, Depr. SOFC System Cost Structure: Manufacturing Costs: $350-550/kW Figure 8-50 Projected cost structure of a 5kWnet APU SOFC system. Gasoline fueled POX reformer, Fuel cell operating at 300mW/cm2, 0.7 V, 90 percent fuel utilization, 500,000 units per year production volume. 8.7.6 Outlook and Conclusions In conclusion, both PEFC and SOFC have the potential to meet the allowable cost targets, provided successful demonstrations prove the technology. It is critical however, that for the current technologies to be commercially successful, especially in small-capacity markets, high production volumes will have to be reached. APU applications might provide such markets. It is similarly critical that the technologies be demonstrated to perform and achieve the projected performance targets, and demonstrate long life. These are the challenges ahead for the fuel cell industry in the APU market segment. 8.8 References 1. James M. Douglas, Conceptual Design of Chemical Processes, McGraw-Hill, Inc., New York, NY, 1988. 2. Max S. Peters, and Klaus D. Timmerhaus, Plant Design and Economics for Chemical Engineers, 3rd Edition, McGraw-Hill, Inc., New York, NY, 1980. 3. Warren L. McCabe, Julian C. Smith, Peter Harriot, Unit Operations of Chemical Engineering, 4th Edition, 1985. 4. M.C. Williams, and T.J. George, "Research Issues in Molten Carbonate Fuel Cells: Pressurization," presented at the 1992 IECEC, Vol. 3, pp. 263-267. 5. "Overview of 11 MW Fuel Cell Power Plant," non-published information from Tokyo Electric Power Company, September 1989. 6. T. Koshimizu, et al., "Development of 5000 kW and 1000 kW PAFC Plants," presented at the JASME-ASME Joint Conference (ICOPE-93), Tokyo, September 1993. 8-104PDF Image | Fuel Cell Handbook (Seventh Edition)
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