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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(equation (5.8)). Using equation (5.9), the minimum heat capacity rate of 17.6 W K-1 and the ethanol temperature at point 3 of 180°C, the exhaust temperature at point 3 is 213°C. Finally, the exhaust temperature at point 4 is found using equation (5.10). With a single-phase evaporator heat transfer rate of 0.46 kW, and exhaust mass flow rate of 16.3 g s-1, an exhaust heat capacity of 1.08 kJ kg-1 K-1, and the exhaust temperature of 213.1°C at point 3, the exhaust temperature at point 4 is 187.0°C. The heat transfer in the two-phase portion of the evaporator is determined in a similar manner: Qevap,tp  mwf,evap hwf,5  hwf,4  (5.11) Qevap,tp  mexh hexh,2  hexh,3  (5.12) Using the ethanol mass flow rate of 5.25 g s-1, the ethanol enthalpy of 850 kJ kg-1 at point 4, and the ethanol enthalpy of 1,354 kJ kg-1 at point 5, the two-phase evaporator heat flow rate is 2.65 kW. With the two-phase heat flow rate, exhaust mass flow rate of 16.3 g s-1, and exhaust enthalpy of 198 kJ kg-1 at point 3, the exhaust enthalpy at point 2 is 361 kJ kg-1. The working fluid state at the superheater outlet is defined by setting the maximum superheat temperature as listed in Table 5-2, coupled with the high-side system pressure. The enthalpy and entropy are calculated using the known temperature and pressure at point 6. The superheater heat transfer rate and effectiveness are found as follows: Qsh  mwf hwf,6  hwf,5  Qsh  mexh hexh,1  hexh,2  (5.13) (5.14) (5.15) (5.16) For the representative point, equation (5.13) can be used along with the ethanol mass flow of 5.25 g s-1, the ethanol enthalpy of 1,354 kJ kg-1 at point 5, and the ethanol enthalpy of 1,846 kJ kg-1 at Qsh,max Csh,minTexh,1Twf,5 Q ε Q sh sh sh,max 80

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