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starting with the superheated vapor at the inlet. The relationship appears to be nearly linear in the two-phase section with each slice requiring the same length to achieve a quality change of 0.05. The total pressure drop for ethanol is 1.76 kPa and the total air side pressure drop is 95.7 Pa. The ethanol pressure drop results in a decrease of the saturation temperature from 90°C to 89.7°C. The next section will describe the model used for the exhaust evaporator. 5.3.2 Evaporator Model The evaporator design differed significantly from that of the condenser, with a counter- flow configuration and rectangular channels (Figure 5-11). The counter-flow design was chosen to keep the size reasonable while trying to extract the maximum heat from the exhaust gases. Because the exhaust approaches the temperature of the ethanol near its liquid saturation point, this design will allow a much smaller heat exchanger and higher effectiveness than for a cross-flow configuration. The exhaust enters the evaporator at one end and runs through the center channels. The liquid ethanol enters at the opposite end of the evaporator and flows in the outside channels in the opposite direction of the exhaust, becoming 100% vapor at the outlet. The details and dimensions of the evaporator model are shown in Table 5-11, and the inputs for the representative Figure 5-11. Diagram showing the counter-flow evaporator configuration. 102PDF Image | WASTE HEAT RECOVERY FROM A HIGH TEMPERATURE DIESEL ENGINE
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