Designing a test heat exchanger
As the physical layout of the exchanger cannot be determined until the area is known the design of an exchanger is of necessity a trial and error procedure. The steps in a typical design procedure are given below:
- Define the duty: heat transfer rate, fluid flow-rates, temperatures.
- Collect together the fluid physical properties required: density, viscosity, thermal conductivity.
- Decide on the type of exchanger to be used.
- Select a value for the overall coefficient, U.
- Calculate the mean temperature difference, Δtm .
- Calculate the area required from equation Q = UA Δtm
- Decide the exchanger layout.
- Calculate the individual coefficients.
- Calculate the U and compare it with selected U value. If the calculated value differs significantly then return to step 6.
- Optimize the design: repeat steps 4 to 10, as necessary, to determine the cheapest exchanger that will satisfy the duty. Usually that will be one with the smallest area.
Typical values of the overall heat-transfer coefficient for various types of heat exchanger are given below:
Shell and tube exchangers |
||
Hot fluid | Cold fluid | U (W/m2 oC) |
Heat exchangers | ||
Water | Water | 800-1500 |
Steam | Water | 1500-4000 |
Coolers | ||
Organic solvents | Water | 250-750 |
Light oils | Water | 350-900 |
Heavy oils | Water | 60-300 |
Gases | Water | 20-300 |
Condensers | ||
Aqueous vapors | Water | 1000-1500 |
Organic vapors | Water | 700-1500 |
Organics (some non-condensables) | Water | 500-700 |
Vacuum condensers | Water | 200-500 |
Jacketed vessels | ||
Water | Dilute aqueous sol. | 200-500 |
Water | Light organics | 200-300 |