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Project 2: Heat Exchanger Design Group Members: Brian Schludecker Phillip Palmer Adam Spindler Mike Hay Joe McGuire Presented 12/12/2006 to Dr. Toksoy.

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Presentation on theme: "Project 2: Heat Exchanger Design Group Members: Brian Schludecker Phillip Palmer Adam Spindler Mike Hay Joe McGuire Presented 12/12/2006 to Dr. Toksoy."— Presentation transcript:

1 Project 2: Heat Exchanger Design Group Members: Brian Schludecker Phillip Palmer Adam Spindler Mike Hay Joe McGuire Presented 12/12/2006 to Dr. Toksoy and ME 414 Class, IUPUI

2 Project Summary Design and optimization of heat exchanger Specifications & objectives Methods Results Conclusions

3 Heat Exchanger Specifications Heat exchanger length must not exceed 7 m Shell diameter must not exceed 2 m Shell mass flow rate: 120,000 kg/hr Water in shell must cool from 40 C to 25 C Water in tube enters at 20 C Ignore fouling

4 Objectives Maximize Q Minimize Weight (cost) Minimize heat exchanger pressure drop

5 Design Strategy Configure MATLAB files to analyze the heat exchanger Modify input factors until heat transfer ratio is close to 1 Run DOE in MATLAB and Minitab to calculate optimal values for system

6 Design Factors Tube outer diameter Shell inner diameter Tube length Number of tube passes Material Pitch Number of Baffles Baffle Spacing

7 Design Factors for DOE Tube outer diameter Shell inner diameter Tube length Number of tube passes Material Pitch Number of Baffles Baffle Spacing

8 Design Decisions Pitch = 1.25 * Tube outer diameter 0 baffles

9 Interaction & Main Effects Plots (to find Critical Factors)

10

11 Mean Effects Plots

12 Pareto Charts

13 Design Decisions Critical factors: Length, Shell ID, Tube OD Material: Aluminum (cost, weight) 1 pass

14 Optimized Results +/- 20%  Using guesses (from Matlab): Optimized results are not standard Size ID and OD, choose close sizes:

15 Optimized Specifications Tube OD = 0.0127 mm Shell ID = 0.5906 m Length = 3.3682 m

16 Final Results Q maximized2.099E6 W dP in shell minimized463 Pa dP in tube minimized1500 Pa Weight minimized1108 kg

17 Conclusions Minitab optimized values for ID and OD are not standard tube/shell sizes, need to adjust Minitab results Objectives achieved Further analysis possible for multiple passes/baffles Questions?


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