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Figure 5-6. Diagram showing condenser construction with two rows of horizontal tubes separated by louvered fins. basic dimensions of the condenser design are listed in Table 5-9 and the inputs for the representative point are shown in Table 5-10. Each tube is 1.5 mm thick, 20.4 mm deep, and contains 17 channels each with a diameter of 0.761 mm (Figure 5-7). The condenser has two rows of tubes with 30 tubes per row. The cooling fins have a 1 mm pitch with 8.5 mm long 27° louvres that are spaced at 1 mm intervals as shown in Figure 5-8. All condensers have a width of 45.4 mm, with the heat exchanger length varying to meet required the heat duty for each WHR system. The condenser models are broken into two sections: single-phase and two-phase. In the first section of the condenser, the liquid ethanol is cooled to the saturation temperature using the corresponding heat transfer correlations. The phase change takes place in the second section of the condenser, which uses the appropriate heat transfer correlations for the two-phase working fluid. The air velocity through the condenser was set at 3 m s-1 for each condenser model, with the assumption that the condenser fan would be sized to provide the required air flow depending on the condenser length. The results show that the estimated maximum pressure drop for airflow through the condenser is 95.71 Pa and the greatest airflow requirement is 1,630 m3 h-1. To verify that this is a 87PDF Image | WASTE HEAT RECOVERY FROM A HIGH TEMPERATURE DIESEL ENGINE
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