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Heat Exchanger Duty Calculator - Q, LMTD, UA Product & Approach

Calculate heat transfer duty, log mean temperature difference, and required surface area for shell-and-tube and plate exchangers

Enter hot-side and cold-side temperatures, flow rates, fluid placeholders, and counterflow or parallel-flow arrangement to calculate a steady-state screening result. The app reports hot-side duty, cold-side duty, average duty Q, LMTD, UA product, approach temperature, effectiveness, duty-balance warnings, and source pointers. It does not calculate exchanger surface area, U-value selection, fouling factors, correction factors, pressure drop, phase change, shell-and-tube geometry, TEMA design, ASME pressure-vessel compliance, or manufacturer rating.

Pro Tip: Use the duty-balance result as an instrument and assumption check. If hot-side and cold-side duties disagree, review flow measurement, temperature probes, density/Cp basis, heat loss, side labels, and phase behavior before comparing the result to design data or trend history.

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Heat Exchanger Duty Calculator

How It Works

  1. Enter Measured Stream Conditions

    Enter hot-side and cold-side inlet temperature, outlet temperature, and flow rate. The app assumes steady-state single-phase flow and constant local fluid properties.

  2. Select Fluid Placeholders

    Choose water, 25% glycol, or 50% glycol for each side. Glycol rows are broad local placeholders and must be replaced by current product data for decision use.

  3. Choose Arrangement

    Select counterflow or parallel flow. The app calculates only ideal terminal-temperature LMTD for these two arrangements and does not apply shell-pass, crossflow, or TEMA correction factors.

  4. Review Warnings First

    Check temperature-cross, small-approach, high-effectiveness, and duty-imbalance warnings before using the Q, LMTD, UA product, or effectiveness values as an estimate.

Built For

  • Plant teams checking whether measured hot-side and cold-side duties are in the same range before deeper troubleshooting
  • Maintenance planners preparing exchanger trend notes for engineering review
  • Process and facilities engineers doing an initial steady-state heat-duty screen before manufacturer or thermal-rating work
  • HVAC and hydronic technicians estimating water or glycol-side duty while keeping product-data and pump-effect caveats visible
  • Energy auditors documenting preliminary heat-recovery opportunities without treating the app as final design software

Features & Capabilities

Two-Sided Duty Check

Calculates hot-side and cold-side duty from local density, Cp, flow, and temperature change, then reports the duty balance as a warning path.

Ideal LMTD Calculator

Calculates LMTD for counterflow and parallel-flow terminal temperatures only, with warnings for zero or negative terminal driving force.

UA Product Output

Reports Qavg divided by LMTD as a UA product. The app does not split U from area A or select either value.

Source Boundary Export

Reports and PDF exports carry ASHRAE, TEMA, ASME, and glycol-product source pointers plus explicit limits for design, pressure, fouling, and manufacturer decisions.

Comparison

Area Included in App Requires External Review
Thermal duty Q from local flow, density, Cp, and temperature change Instrument accuracy, phase behavior, heat loss, current fluid properties
Temperature driving force Ideal counterflow or parallel-flow LMTD Crossflow, shell-pass, multipass, or correction-factor methods
UA product Qavg divided by LMTD Separate U-value, surface area, fouling, geometry, and manufacturer rating
Fluid rows Water plus broad 25% and 50% glycol placeholders Current product data, concentration test, viscosity, pump head, SDS, compatibility
Safety and code Source warnings and citations TEMA, ASME BPVC, API, relief, inspection, repair, AHJ, and qualified review

Assumptions

  • Steady-state single-phase liquid streams with constant flow rates and terminal temperatures.
  • Local constant Cp and density rows are used for water and glycol placeholders.
  • Average duty is the arithmetic average of hot-side and cold-side duty.
  • LMTD is ideal counterflow or parallel flow only; no correction factor is applied.
  • UA is reported as a product and is not split into U and area A.

Limitations

  • Does not calculate exchanger type, surface area, U-value, fouling factors, pressure drop, Reynolds number, viscosity effects, or pump impact.
  • Does not model condensers, evaporators, reboilers, two-phase flow, phase change, flashing, boiling, or steam quality.
  • Does not perform shell-and-tube geometry, baffle, vibration, nozzle-load, metallurgy, corrosion, relief, pressure-boundary, or inspection checks.
  • Does not determine cleaning interval, repair method, purchase acceptance, manufacturer rating, TEMA/API/ASME compliance, or AHJ approval.

References

  • ASHRAE Handbook source pointers for heat-transfer equations and current fundamentals context.
  • TEMA Standards Eleventh Edition source pointer for shell-and-tube exchanger standards context.
  • ASME BPVC Section VIII Division 1 source pointer for pressure-vessel scope and boundaries.
  • Dow DOWFROST and DOWTHERM SR-1 source pointers for glycol product-data context.

Frequently Asked Questions

It calculates steady-state hot-side duty, cold-side duty, average duty Q, ideal LMTD for counterflow or parallel flow, a UA product, approach temperature, and a simple effectiveness screen from local constant fluid properties.
No. It reports UA as a product. Selecting U, separating area A, applying fouling factors, and confirming installed surface area require exchanger data, current sources, and qualified review.
No. The app supports only ideal counterflow and parallel-flow LMTD. Multi-pass shell-and-tube, crossflow, air-cooled, and complex arrangements need an appropriate correction-factor method or thermal-rating software.
Use it only as one trend input. Cleaning decisions should also consider clean baseline, pressure drop, process impact, fouling mechanism, inspection history, safety, chemicals, downtime, and manufacturer or engineering review.
No. The glycol rows are local placeholders. Replace them with current product technical data at the tested concentration and operating temperature before using the result for pump, heat-transfer, chemical, or safety decisions.
Disclaimer: This app provides a preliminary steady-state screening calculation. It is not heat exchanger design software, manufacturer rating software, TEMA compliance, ASME pressure-vessel design, API/AHJ approval, glycol product validation, cleaning authorization, repair approval, or safety approval.

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