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Figure 5-27. Radiator tube configuration and dimensions in mm. for the entire fin array is 98.2%. EG side pressure drop is once again found using the Darcy- Weisbach formula (equation (5.42)). The friction factor is estimated using the Shah and Bhatti correlation (equation (5.73)), with inputs of 107.8 and 0.22 for the Reynolds number and EG channel aspect ratio, respectively. The friction factor is 0.704, the mass flux is 21.6 kg m-2 s-1, the EG density is 1,020 kg m-3, and the hydraulic diameter is 4.15 mm, yielding a pressure drop of 38.7 Pa m-1. The air side heat transfer calculations are identical to the calculations for the oil cooler model. Equations (5.36) through (5.41) are used to estimate the heat transfer coefficient for the air side of the oil cooler using the values supplied in Table 5-19 and 5-20. The air side heat transfer coefficient is found to be 111 W m-2 K-1 for the representative point. The air side heat transfer coefficient (hair) along with the heat exchanger aluminum wall thermal conductivity (kw) of 240 W m-1 K-1 and the fin thickness (tf) of 0.1 mm can then be used to solve equation (5.34) which results in an m value of 136. The resulting air side fin efficiency (f) for the representative model is 87.0%. From equation (5.29), the efficiency for the entire fin array is 90.8%. The equations for pressure drop given in the condenser section (equations (5.42) through (5.47)) are also utilized for the 131PDF Image | WASTE HEAT RECOVERY FROM A HIGH TEMPERATURE DIESEL ENGINE
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