Unit Conversions · Engineering & science · Heat & thermodynamics

Heat Exchanger LMTD and Effectiveness Calculator

Calculate terminal temperature differences, log-mean temperature difference, duty from UA, reconciled effectiveness estimate, capacity rates, and energy-balance mismatch for parallel or counterflow data.

Unit Conversions · Engineering & science · Heat & thermodynamics

Heat Exchanger LMTD and Effectiveness Calculator

Private in-browser calculation · explicit units, solve direction, assumptions, reconciliation, and companion outputs
Heat Exchanger LMTD and Effectiveness Calculator — visual relationshipUses the current inputs
Heat Exchanger LMTD and Effectiveness Calculatorsicounterknown quantity → unit-aware physical relation → result
The visual explains this calculator’s quantity and updates from the entered values. It does not add measurement accuracy or infer missing physical data.
  1. 1EnterProvide the known values
  2. 2CalculateResults update automatically
  3. 3VerifyReview the details and units
Try an example

Every label states the corresponding SI and customary input unit. Outputs include both systems where useful.

Calculation result

Enter valid values to see the result.

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Understand the engineering model

What is Heat Exchanger LMTD and Effectiveness?

Thermodynamic calculations track energy, heat, work, temperature, phase change, resistance, and ideal limits under a declared system boundary and sign convention.

Provide both LMTD and effectiveness views while exposing crossed, impossible, or materially unreconciled terminal data instead of hiding it.

The relationship

Write the model before substituting values

See the calculation

From measurement to engineering result

Worked context

Read the output with its units

120→80 hot and 20→60 cold with equal 1,000 W/K capacity rates gives 40 kW balanced duty and a 40% reconciled effectiveness estimate.

Interpret with care

Important model boundary

This rating worksheet requires internally meaningful terminal temperatures and capacity rates. A mismatch warning means the average is only a reconciliation estimate, not an actual measured duty. Phase change, multipass correction factors, fouling, pressure drop, variable properties, leakage, and equipment selection are excluded.

A calculated value does not certify a component, material, installation, operating envelope, code requirement, or safety decision. Check measurements, signs, standards, uncertainty, and professional approval where consequences matter.

Browse Engineering & science for connected physical relationships.

Quick guide

How to use this calculator

  1. Choose the physical relationship and solve direction that match the known measurements rather than forcing unlike quantities into one formula.
  2. Enter every unit, sign, reference direction, geometry, material property, fluid property, temperature basis, coefficient, and idealization explicitly. The calculator normalizes compatible quantities internally and exposes intermediate values.
  3. Use reconciliation and companion outputs to catch entry mistakes, then retain the stated model boundary. A theoretical result is not a design approval, material certificate, equipment rating, or safety determination.

Calculation method

How the heat exchanger lmtd and effectiveness calculator works

Provide both LMTD and effectiveness views while exposing crossed, impossible, or materially unreconciled terminal data instead of hiding it.

Counterflow ΔT terms are T_h,in−T_c,out and T_h,out−T_c,in; parallel terms are inlet and outlet differences. LMTD=(ΔT₁−ΔT₂)/ln(ΔT₁/ΔT₂). Q_h=C_h(T_h,in−T_h,out), Q_c=C_c(T_c,out−T_c,in), Q_reconciled=(Q_h+Q_c)/2 only as a comparison estimate, and estimated effectiveness=Q_reconciled/(C_min(T_h,in−T_c,in)).

Worked example

Heat Exchanger LMTD and Effectiveness example

120→80 hot and 20→60 cold with equal 1,000 W/K capacity rates gives 40 kW balanced duty and a 40% reconciled effectiveness estimate.

Counterflow ΔT terms are T_h,in−T_c,out and T_h,out−T_c,in; parallel terms are inlet and outlet differences. LMTD=(ΔT₁−ΔT₂)/ln(ΔT₁/ΔT₂). Q_h=C_h(T_h,in−T_h,out), Q_c=C_c(T_c,out−T_c,in), Q_reconciled=(Q_h+Q_c)/2 only as a comparison estimate, and estimated effectiveness=Q_reconciled/(C_min(T_h,in−T_c,in)).

Supported inputs

Precision and limits

Engineering-model boundary

This rating worksheet requires internally meaningful terminal temperatures and capacity rates. A mismatch warning means the average is only a reconciliation estimate, not an actual measured duty. Phase change, multipass correction factors, fouling, pressure drop, variable properties, leakage, and equipment selection are excluded.

Units and precision

Calculations normalize compatible inputs to SI, retain working precision, and round only for display. Very small and large nonzero values use scientific notation; displayed digits cannot create accuracy beyond the entered measurements and properties.

Decision boundary

This page solves the declared idealized relationship only. Verify applicable material data, operating conditions, geometry, loads, coefficients, standards, codes, manufacturer requirements, uncertainty, and professional approval before consequential use.

Category ownership

Generic mechanics, materials, fluid, aerodynamic, wave, and thermodynamic relationships live here. Trade-specific pipe, HVAC, motor, electrical, construction, automotive, radiation, statistical, chemical, and astronomical workflows remain with their established categories.

Privacy

Entered values and results stay in this browser and are not sent to analytics or third parties.

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