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Accordingly, the maximum obtainable temperature of combustion air depends not only on the tolerance of materials used, such as heat-resistance alloys and refractory, but also on heat losses of the system. 6 Conceptual temperature histories and fluctuation intensity. 9 The typical regenerative heat exchanger for preheating combustion air was a bed packed with ceramic balls. The size varies depending on the cycle time between 30 s to several minutes, which determines the amount of heat storage. 15 However, if the hot gas flow escaping through a shortcut of minimum pressure drop occurs in the bed, it gives rise to uneven temperature distribution in a cross section, resulting in inefficiency of the regenerator.
If all of the heat loss and waste from a heating furnace can be eliminated, for example, all the heat generated from fuel will be transferred to the material being heated in the furnace. Therefore, the high efficiency of waste heat recovery is one of the most promising measures available to suppress CO2 emission, that is, to reduce greenhouse gases. The higher the efficiency of the regenerator, the less CO2 emitted. Although available heat in exhaust gases can be transferred efficiently to the incoming cold combustion air using an infinitely long heat exchanger, the actual heat transfer rate is limited by the geometry of heat exchangers.
S. H. A. Rahbar. AFRC Spring Meeting. Kingston, 1994. F. J. Weinberg. Combustion Science and Technology, 121:3, 1996. T. Niioka. Private communication, 1998. M. Matsumoto et al. 11th IFRF Members Conf. IFRF, 1995. M. Flamme and H. Kremer. Int. Gas Research Conf. Orlando, FL, 1992. M. Flamme. 4th Int. Conf. on Technologies and Combustion for a Clean Environment. Lisbon, 1997. 14. T. Hasegawa, R. Tanaka, and K. Kishimoto. AFRC/JFRC Int. , p. N. 9C, 1994. 15. L. M. Dearden et al. J. Inst. , 69:23, 1996.
Akin On the Conservation of Force