🌡️ LMTD Calculator
Calculate the Logarithmic Mean Temperature Difference for heat exchangers.
Inputs
Results
Temperature Profile
Calculator Description
The Logarithmic Mean Temperature Difference (LMTD) represents the effective average driving force for heat transfer in a heat exchanger, where the temperature difference between the hot and cold fluids varies along its length. Because that difference changes exponentially, a logarithmic mean is used instead of a simple arithmetic average.
What this calculator finds
This calculator computes a heat exchanger's LMTD from the inlet and outlet temperatures of the hot and cold fluids, supporting both counter-flow and parallel-flow arrangements.
Why it matters
- Sizing the required heat-transfer area A in the design equation Q = U · A · LMTD
- Comparing how counter-flow versus parallel-flow arrangements affect performance
- Evaluating the performance and verifying the heat duty of existing exchangers
Formula
LMTD Equation
The LMTD is the logarithmic mean of the temperature differences ΔT₁ and ΔT₂ at the two ends of the exchanger. How those end differences are defined depends on the flow arrangement.
- LMTD — Logarithmic mean temperature difference [°C or K]
- Counter-flow — ΔT₁ = T_h,in − T_c,out | ΔT₂ = T_h,out − T_c,in
- Parallel-flow — ΔT₁ = T_h,in − T_c,in | ΔT₂ = T_h,out − T_c,out
- T_h, T_c — Hot / cold fluid temperatures; subscripts in/out mean inlet/outlet [°C]
How the formula works
- A larger LMTD means a greater driving force, so the same duty can be handled with less area.
- For the same inlet/outlet temperatures, counter-flow always yields a larger LMTD than parallel-flow, making it more efficient.
- If ΔT₁ = ΔT₂ the log expression becomes 0/0, so LMTD is then defined as that common value (the arithmetic mean).
Worked example
In counter-flow with hot fluid 120 °C → 80 °C and cold fluid 30 °C → 70 °C, ΔT₁ = 120 − 70 = 50 °C and ΔT₂ = 80 − 30 = 50 °C. Since they are equal, LMTD = 50 °C. If instead ΔT₁ = 50 and ΔT₂ = 30, then LMTD = (50 − 30) / ln(50/30) ≈ 39.2 °C.
Useful Tips
Practical tips
- For shell-and-tube or cross-flow exchangers, apply a correction factor F: ΔT_eff = F × LMTD (F ≤ 1).
- Design for counter-flow when possible to obtain a larger LMTD and reduce heat-transfer area.
Limitations & cautions
- The LMTD method assumes a constant overall heat-transfer coefficient U and constant specific heats throughout the exchanger.
- For phase change (condensation/boiling) or strongly varying properties, split the exchanger into zones for accuracy.
- When outlet temperatures are unknown, the ε-NTU method is often more convenient than LMTD.