Calculate coaxial heat exchanger missing ΔT1, ΔT2, U, area or Q using the LMTD method and unit conversions in °C/°F, W/m²K, m², and W.

Coaxial Heat Exchanger Calculator

Enter any 4 values to calculate the missing variable. Use ΔT1 ≥ ΔT2 (terminal temperature differences) for the LMTD method.

Coaxial Heat Exchanger Formula

The calculator uses the log mean temperature difference method for a coaxial heat exchanger. The main heat transfer equation is:

Q = U*A*LMTD

The log mean temperature difference is calculated as:

LMTD = (DeltaT1 - DeltaT2) / ln(DeltaT1 / DeltaT2)

If the two terminal temperature differences are equal, the calculator uses the limiting case:

LMTD = DeltaT

Rearranged forms used to solve for missing values are:

U = Q / (A*LMTD)
A = Q / (U*LMTD)
LMTD = Q / (U*A)
  • Q = heat transfer rate, in W, kW, or MW
  • U = overall heat transfer coefficient, in W/m²K or BTU/hr·ft²·°F
  • A = heat transfer area, in m² or ft²
  • LMTD = log mean temperature difference
  • DeltaT1 = higher terminal temperature difference
  • DeltaT2 = lower terminal temperature difference
  • ln = natural logarithm

To calculate Q, the calculator first finds LMTD from DeltaT1 and DeltaT2, then multiplies U, A, and LMTD.

To calculate U, it divides Q by the product of A and LMTD.

To calculate A, it divides Q by the product of U and LMTD.

To calculate DeltaT1 or DeltaT2, it first calculates the required LMTD from Q / (U*A), then solves the LMTD equation numerically. The calculator assumes DeltaT1 is greater than or equal to DeltaT2.

Common Unit Conversions for Coaxial Heat Exchanger Calculations

The calculator converts all inputs to base SI units before applying the formula.

Quantity Input unit Base unit Conversion
Temperature difference °F °C or K difference ΔT(°C) = ΔT(°F) × 5/9
Overall heat transfer coefficient BTU/hr·ft²·°F W/m²K 1 BTU/hr·ft²·°F = 5.678263 W/m²K
Area ft² 1 ft² = 0.09290304 m²
Heat transfer rate kW W 1 kW = 1000 W
Heat transfer rate MW W 1 MW = 1,000,000 W

Typical Overall Heat Transfer Coefficient Ranges

Use these ranges only as rough checks. Actual U values depend on fluids, flow regime, wall material, fouling, and whether phase change occurs.

Service type Typical U range Notes
Liquid to liquid, water-like fluids 500 to 2000 W/m²K Common range for clean, turbulent flow
Oil to water 100 to 800 W/m²K Oil-side resistance often controls the result
Gas to liquid 20 to 300 W/m²K Gas-side heat transfer is usually lower
Condensing vapor to liquid 1000 to 6000 W/m²K Can be high when condensation is efficient

Example Calculations

Example 1: Calculate heat transfer rate

Suppose a coaxial heat exchanger has:

  • DeltaT1 = 60 °C
  • DeltaT2 = 30 °C
  • U = 750 W/m²K
  • A = 4 m²

First calculate LMTD:

LMTD = (60 - 30) / ln(60 / 30) = 43.28 °C

Then calculate Q:

Q = 750*4*43.28 = 129842 W

The heat transfer rate is about 129.84 kW.

Example 2: Calculate required heat transfer area

Suppose you need:

  • Q = 100 kW
  • U = 500 W/m²K
  • DeltaT1 = 50 °C
  • DeltaT2 = 25 °C

Convert Q to watts:

100 kW = 100000 W

Calculate LMTD:

LMTD = (50 - 25) / ln(50 / 25) = 36.07 °C

Calculate area:

A = 100000 / (500*36.07) = 5.55 m^2

The required heat transfer area is about 5.55 m².

FAQs

What are DeltaT1 and DeltaT2 in a coaxial heat exchanger?

DeltaT1 and DeltaT2 are the terminal temperature differences between the hot and cold fluids at the two ends of the exchanger. For the calculator, enter the larger terminal difference as DeltaT1 and the smaller terminal difference as DeltaT2. Both values must be positive.

Why does the calculator use LMTD instead of a simple average temperature difference?

The temperature difference between the two fluids changes along the exchanger length. LMTD gives the correct effective temperature difference for steady-state heat exchanger calculations when the terminal temperature differences are known. A simple arithmetic average can give a less accurate result, especially when DeltaT1 and DeltaT2 are far apart.

What does it mean if there is no solution for DeltaT1 or DeltaT2?

When solving for a missing terminal temperature difference, the required LMTD must be physically consistent with the known terminal difference. With DeltaT1 greater than or equal to DeltaT2, LMTD cannot be less than DeltaT2 or greater than DeltaT1. If the calculator reports no solution, check Q, U, A, and the terminal temperature difference values.