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Figure 4-1. Figure 5-1. Figure 5-2. Figure 5-3. Figure 5-4. Figure 5-5. Figure 5-6. Figure 5-7. Figure 5-8. Figure 5-9. Figure 5-10. Figure 5-11. Figure 5-12. Figure 5-13. Figure 5-14. Figure 5-15. Figure 5-16. Figure 5-17. Figure 5-18. Figure 5-19. Regression analysis results for 3100 rpm and 18 N-m of torque used to determine correlations between parameters and coolant temperature and their significance using a 95% confidence interval. ............................................................................ 67 Diagram for state-of-the-art WHR system. ............................................................. 69 Diagram for high-temperature coolant WHR systems. ........................................... 70 Flow chart for thermodynamic analysis. ................................................................. 71 Graphic representation of WHR system optimization strategy. WHR system output is maximized through increasing superheat (up to 375°C maximum) while maintaining at least a 5° CAT in the exhaust evaporator........................................ 75 Diagram showing the cross-flow condenser configuration as well as single-phase and two-phase sections............................................................................................ 86 Diagram showing condenser construction with two rows of horizontal tubes separated by louvered fins....................................................................................... 87 Condenser tube configuration and dimensions in mm. ........................................... 90 Left: Cross-section of condenser fin showing louver angle and pitch. Right: Side view of condenser assembly showing louver length and fin pitch.......................... 90 Plot of ethanol heat transfer coefficient in the condenser vs. the cumulative heat duty. The plot starts with the single-phase section (first point) and proceeds through the two-phase section as the cumulative heat duty increases. The representative point is the first point in the two-phase section..................................................... 100 Cumulative condenser length vs. cumulative heat duty starting with vapor inlet and ending with 100% liquid ethanol. ......................................................................... 101 Diagram showing the counter-flow evaporator configuration. ............................. 102 Diagram showing evaporator construction with ethanol channels on the outside and exhaust channels running in the center.................................................................. 105 Left: Cross-section of ethanol channels in evaporator. Right: Cross-section of exhaust channels in exhaust evaporator. ............................................................... 106 Plot of ethanol heat transfer coefficient in the evaporator vs. the cumulative heat duty. The plot starts with the single-phase section (first point) and proceeds through the two-phase section as the cumulative heat duty increases................................ 110 Cumulative evaporator length vs. cumulative heat duty starting with liquid inlet and ending with 100% ethanol vapor........................................................................... 112 Diagram showing cross-flow superheater configuration. ..................................... 115 Diagram showing superheater construction with ethanol channels on the outside and exhaust channels running in the center........................................................... 115 Left: Cross-section of ethanol channels in superheater. Right: Cross-section of exhaust channels in superheater. ........................................................................... 116 Diagram showing counter-flow recuperator configuration. .................................. 119 xiPDF Image | WASTE HEAT RECOVERY FROM A HIGH TEMPERATURE DIESEL ENGINE
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