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 transcript:

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

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

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

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

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

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

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

Design Decisions Pitch = 1.25 * Tube outer diameter 0 baffles

Interaction & Main Effects Plots (to find Critical Factors)

Mean Effects Plots

Pareto Charts

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

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

Optimized Specifications Tube OD = mm Shell ID = m Length = m

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

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?