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The cold-side line for counterflow is plotted opposite the hot-side travel direction to reflect reverse movement through the exchanger.
| Case | Flow | Hot In | Hot Out | Cold In | Cold Out | F | Approx. LMTD |
|---|---|---|---|---|---|---|---|
| 1 | Counterflow | 150 | 95 | 30 | 70 | 1.00 | 72.13 |
| 2 | Parallel | 120 | 80 | 25 | 60 | 1.00 | 55.62 |
| 3 | Counterflow | 180 | 110 | 35 | 90 | 0.92 | 81.77 |
The logarithmic mean temperature difference gives the effective average temperature driving force across a heat exchanger. It is more accurate than a simple arithmetic mean because exchanger temperature profiles are nonlinear along the flow path.
How to calculate log mean temperature difference: First compute the two terminal temperature differences based on exchanger arrangement. Then apply the logarithmic mean formula. If a correction factor is needed for shell-and-tube or multipass service, multiply LMTD by F before using Q = UAFΔTlm.
It is the effective average temperature difference between hot and cold fluids in a heat exchanger. It accounts for temperature changes along the exchanger and is widely used in thermal design calculations.
Temperature differences change nonlinearly along exchanger length. The logarithmic mean reflects that variation, so it represents the actual thermal driving force more accurately than a simple average.
For parallel flow, compare inlet-to-inlet and outlet-to-outlet temperatures. For counterflow, compare hot inlet with cold outlet, then hot outlet with cold inlet. Those two values go into the LMTD formula.
When the two terminal temperature differences are equal, the logarithmic expression collapses to that same value. In practice, LMTD equals either terminal difference in that special case.
Real exchangers like shell-and-tube or multipass units may not behave as pure parallel or pure counterflow devices. A correction factor adjusts the ideal LMTD to better represent actual thermal performance.
Yes. If you enter heat duty, area, and temperatures, the calculator can estimate the required U value from Q = UAFΔTlm. It can also estimate heat duty if U and area are known.
Counterflow often provides a larger average driving force than parallel flow for the same terminal temperatures. That usually makes counterflow more thermally efficient and can reduce required exchanger area.
Use consistent units. Temperature differences can be in °C or K because the difference magnitude is identical. Heat duty, area, and U value should follow compatible SI or engineering unit systems.
Important Note: All the Calculators listed in this site are for educational purpose only and we do not guarentee the accuracy of results. Please do consult with other sources as well.