Number of Transfer Units (NTU)
Also known as NTU method
or type the values yourself
Worked example: UA 4000 W/K against 1.5 kg/s of water → NTU 0.637. Press Try an example to run it live, then adjust anything.
Enter your known values, leave one input blank, and solves for the missing one. Tap a variable’s symbol to see what it means, with a typical value. Change any unit and the answer follows.
Where Number of Transfer Units (NTU) fits
- The effectiveness-NTU method5 formulas
See also
Capacity Rate Ratio (Cr): Both use minimum stream mass flow and minimum stream specific heat.Maximum Possible Heat Transfer (Qmax): Both use minimum stream mass flow and minimum stream specific heat.Heat Exchanger Duty (Q = U·A·F·LMTD): Both use Overall coefficient and heat transfer area.Effectiveness from NTU (Counterflow): Both use number of transfer units.Heat Loss Through an Assembly (Q = A·ΔT/R): Both use heat transfer area.Thermal Resistance of a Plane Wall: Both use heat transfer area.5 more related
Fouled Overall Coefficient: Both use Overall coefficient.Fouling Factor on an Overall Coefficient: Both use Overall coefficient.Overall Heat Transfer Coefficient (U): Both use Overall coefficient.Overall U from Total Resistance: Both use Overall coefficient.U-Factor from Total R-Value (U = 1/R): Both use Overall coefficient.Effectiveness–NTU →
UniversityThermodynamics & Heat Transfer
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Number of Transfer Units (NTU) explained
NTU is an exchanger's size measured in the only currency that matters: conductance compared with the thermal inertia of the fluid flowing through it. UA is how well the machine can transfer; ṁcₚ is how much heat the limiting stream can carry per degree. Their ratio is dimensionless and tells you immediately what class of equipment you are holding: NTU below 0.5 is a trim heater that barely touches the fluid, 1–3 is normal process duty, 3–5 is a close-approach unit, and above 5 you are in regenerator and cryogenic territory where surface becomes very expensive per degree gained.
The effectiveness-NTU method was developed by W. M. Kays and A. L. London for the compact heat exchangers of gas-turbine regenerators and published in Compact Heat Exchangers (1955): a book still on working desks seventy years later. Their motivation was practical: LMTD design demands all four terminal temperatures, but a regenerator problem usually gives you the two inlets and asks what comes out, which drives LMTD into iteration and NTU straight to an answer. Worked example: U = 500 W/(m²·K) on 8 m² against 1.5 kg/s of water gives NTU = 4000/6279 = 0.64, a small unit. Trap: ṁcₚ must be the minimum stream's, not whichever stream you measured first.
Number of Transfer Units (NTU) formula
- = Number of transfer units
- = Overall coefficient (W/(m²·K))
- = Heat transfer area (m²)
- = Minimum stream mass flow (kg/h)
- = Minimum stream specific heat (J/(kg·K))
Cite this page
formula.expert. (2026, October 31). Number of Transfer Units (NTU) Formula & Calculator. https://formula.expert/solvers/ntu-from-ua