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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 1-14. Projected cost structure of a 5kWnet APU SOFC system. Gasoline fueled POX reformer, Fuel cell operating at 300mW/cm2, 0.7 V, 90 % fuel utilization, 500,000 units per year production volume. Outlook and Conclusions In conclusion, both PEFC and SOFC have the potential to meet allowable cost targets, provided successful demonstrations prove the technology. It is critical however, that for these 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. 1.8.6 DerivativeApplications Because of the modular nature of fuel cells, they are attractive for use in small portable units, ranging in size from 5 W or smaller to 100 W power levels. Examples of uses include the Ballard fuel cell, demonstrating 20 hour operation of a portable power unit (32), and an IFC military backpack. There has also been technology transfer from fuel cell system components. The best example is a joint IFC and Praxair, Inc., venture to develop a unit that converts natural gas to 99.999% pure hydrogen based on using fuel cell reformer technology and pressure swing adsorption process. 1.9 References 1. A.J. Appleby, F.R. Foulkes, Fuel Cell Handbook, Van Nostrand Reinhold, New York, NY, 1989. 1-32PDF Image | Fuel Cell Handbook (Seventh Edition)
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