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KNOWLEDGE · K12

Calculated power, weak output on site: four checks to run

The gap between drawing and site is rarely the formula. It is supply voltage, heat loss through insulation, actual flow and fouling — all measurable with instruments in an afternoon.

  • Measure phase current first
  • Check voltage on load
  • Back-calculate from ΔT and flow
  • Scan insulation with IR

Heater sizingPublished 2026-10-08中文版 ↗

01Four real causes

Supply below rated voltage

Output follows the square of voltage. At 340 V a 380 V rated heater delivers roughly 80% of its nameplate power.

Underestimated heat loss

Missing or thin insulation, plus steelwork bridging, can consume the whole design margin.

Flow away from design point

A pump or fan working somewhere else on its curve changes the duty: more medium flow, smaller temperature rise — it feels underpowered.

Fouling or a dead bank

Scale on the water side, carbon on the oil side, dust on the air side; or one control bank that never picks up.

02Voltage against output

P actual / P rated = (U actual / U rated)². End-of-line voltage drop, transformer tap position and a sagging summer grid can take 5%~10% off supply, which is 10%~19% off output. If the calculation used rated voltage while the site runs at 340~360 V, the shortfall is explained there — and with a long cable run, check the drop at the heater terminals, not at the panel.

On the loss side, thickness per the specification is not the end of it: scan the outer surface with infrared. Anywhere noticeably warmer than ambient is exporting heat. Steelwork, supports and nozzle penetrations often matter more than the insulation thickness itself.

03The four-step site order

Current

Clamp-meter each phase and compare with nameplate amps. One phase clearly low means that group is not energised.

Voltage on load

Record terminal voltage while running. No-load voltage proving fine tells you nothing.

ΔT and flow

Back-calculate the power absorbed by the medium from measured rise and flow, then compare with theoretical output.

Insulation

Walk an IR camera over the lagging and at brackets, nozzles and wall penetrations. Hot spots are heat escaping.

04Two things to re-check after the maths

Re-check two points: whether the design assumed continuous running while production is actually intermittent (cold starts need extra duty), and whether the control allows staged switching, so the plant is not paying for peak capacity at part load most of the time. Most underperforming sites end up fixed on run pattern and heat loss, not on the heater rating.

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FAQ

Common questions

01Brand-new plant and already weak output?+

Start with phase current and voltage on load. A single-phased termination and a control bank that never closes account for most new-install cases.

02Output drifting down over the years?+

Water side: scale. Oil side: carbon layer. Air side: dust and reduced airflow. All three stop the same power reaching the medium.

03Can I just raise the setpoint?+

No — that changes the target, not the capacity. The result is a longer ramp and a hotter sheath.

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