WASTE HEAT RECOVERY FROM A HIGH TEMPERATURE DIESEL ENGINE

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WASTE HEAT RECOVERY FROM A HIGH TEMPERATURE DIESEL ENGINE ( waste-heat-recovery-from-high-temperature-diesel-engine )

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 σ 0.5  gρ ρ The Laplace number (La) for the ethanol at the representative point is 2.01, yielding a Chisolm number (Ch) of 1.43. Thus, the value of the square of the friction multiplier (Φl) is 350.1. Therefore, the two-phase pressure drop per unit length is 7.84 kPa m-1. Similar to the single-phase section, the required length of each two-phase slice was found from the area formulae in equations (5.30), (5.31), (5.52), and (5.53) as well as the thermal resistance formula in equation (5.28). For the representative point, the required inner tube surface area is 0.031 m2 and the required outer tube surface area is 0.034 m2, yielding a required length of 0.013 m. To fully condense the ethanol from vapor at 90°C to liquid at 90° requires a two-phase condenser section of 0.271 m. The single-phase section of the representative condenser required 0.036 m to cool the ethanol to the saturation temperature for a total condenser length of 0.307 m. Figure 5-10 plots the cumulative condenser length against the cumulative condenser heat duty, Figure 5-10. Cumulative condenser length vs. cumulative heat duty starting with vapor inlet and ending with 100% liquid ethanol. La   lg Dh   (5.66) 101

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