Email
DIANREZHANKnowledge中文

KNOWLEDGE · K21

Electric versus gas dryers: compare plants, not tariffs

The comparison usually starts with a price per kWh and ends in the wrong place. A gas dryer can look cheap per unit of heat and still cost more overall once you count the flue, the combustion air, the boiler-room footprint, the permits and the heat you cannot recover from wet exhaust.

  • Energy price is one line of six
  • Gas needs a flue and an air supply
  • Electric turndown is better
  • Peak demand charges change the answer

SizingPublished 2026-10-08中文版 ↗

01The six things that actually differ

Installed cost

Electric: a cable, a panel and a bank in the airstream. Gas: burner, refractory, flue, gas train, combustion-air louvres, and a gas connection that may need a utility upgrade and a design review.

Permits and inspection

Combustion equipment brings permits, annual inspection and CO monitoring in occupied buildings. Electric brings an electrical inspection and a demand calculation instead. Which is heavier depends entirely on your jurisdiction.

Turndown

A modulating gas burner turndowns to roughly 20-25% with care; an SCR-controlled electric bank goes smoothly to 5% and below. Drying lines that idle at night and ramp in the morning live in that turndown range.

Response and control

Electric changes output in one cycle of the mains. A gas burner has a firing-rate ramp for safety, which costs minutes during a product changeover.

Moisture and exhaust

Burning gas produces water vapour — roughly 1.6 kg of water per kg of natural gas. In a drying application that water goes into the airstream you are trying to dry with.

Residual heat

Gas systems carry stack losses; electric banks can be ducted to recover almost everything downstream. Where the exhaust is hot and wet, the electric option keeps more of the energy inside the process.

None of these is a winner by itself. The reason to compare them side by side is that most of the six are fixed costs, and only the first one is the number people usually argue about.

02Running cost, done properly

Same duty, two fuels

A dryer needing 300 kW of heat: electric draws 300 kWh per hour at the meter (bank efficiency near 100%). Gas at 85% net efficiency needs about 353 kWh of fuel per hour, roughly 35.6 m³ of natural gas.

Compare your own prices

The break-even is simply kWh_price × 300 versus gas_price × 35.6 m³. If electricity costs 0.12 and gas 0.045 per kWh-equivalent, gas wins on fuel. At 0.08 per kWh-equivalent for electricity the two are level, before the other five rows.

Demand charges

Electric plants pay a capacity charge on peak kW. A 300 kW dryer that ramps at 08:00 with everything else can move the whole site into a higher demand band. Staggering the ramp or holding a small buffer temperature is often worth more than the fuel choice.

Standby

A gas dryer that keeps a burner lit and a flue warm at idle is paying during idle. An electric bank consumes nothing when it is off, which is the most underrated line in the comparison.

Put your own tariff into the two numbers above before believing anyone else's chart, including ours. The fuel comparison is genuinely close in many markets and the deciding factor is usually standby behaviour and turndown, not the unit price.

03Where electric wins outright

No gas connection within a practical distance, or a utility upgrade that costs more than the dryer.

A dryer inside an occupied or temperature-controlled building, where combustion air and flue routing dominate the layout.

Processes that must not see combustion products — food, pharma, optics, some coatings.

Hazardous areas where a naked flame or a hot combustion surface is a classification problem of its own.

Lines that idle for long stretches and need to be at temperature in minutes rather than in half an hour.

Sites with on-site generation or storage, where the marginal cost of electricity is not the retail price.

04Where gas still wins

Very large continuous duties — above roughly a megawatt of heat — in a market where gas is cheap and the site already has the infrastructure.

Plants with waste heat or low-pressure steam available for free, where a steam coil does the job and neither fuel is really being spent.

Retrofit into an existing oven whose burner openings, refractory and flue are already there, where the electric alternative means rebuilding the plenum.

Sites with weak electrical supply where a 300 kW load would trigger a substation upgrade — a supply cost that dwarfs a decade of fuel difference.

The honest summary: electric heating is usually the better answer for control, footprint, standby and cleanliness; gas remains the better answer for very large continuous heat on a site that already has gas. Price the supply, the permits and the standby hours, and the decision gets easier.

Send this duty over and we will run it through the same method

Medium, flow, temperatures, pressure. With those four, duty and architecture are a same-day answer.

Submit your duty →

FAQ

Common questions

01Is electric drying slower?+

No, if the bank is sized for the duty. Electric drying feels slower only when a bank sized for holding duty is asked to do a cold-start recovery in a time window designed for a burner.

02What about the carbon footprint?+

It is a grid question. Electric resistance heating converts electricity to heat at the point of use; total emissions still depend on the electricity source. A gas boiler’s emissions depend on its fuel and operating efficiency. On a decarbonising grid the electric option improves every year without you touching it, and heat-pump drying can beat both where the temperature level allows.

03Can I run both?+

Yes, and many lines do: gas for the base load, electric trim for control and for the hours when the burner is inefficient. The control logic has to be sequenced so the two do not fight, and the electric bank sized for trim rather than for full duty.

INQUIRY PREP

Come prepared, decide faster on Tubular Elements

Have these parameters ready — they feed directly into model selection, power sizing and mechanical design review.
Send your spec ↗
K13Electric heaters for paint curing and powder coating ovensHow to size an electric heater for a paint curing or powder coating oven: the four real loads, a worked tunnel example, element layout in recirculating air, and the three commissioning failures that get blamed on the heater.K14Electric heating for lithium-ion electrode coating linesSizing electric heaters for lithium-ion electrode coating dryers: sensible plus latent load per zone, dew-point-driven airflow, worked zone arithmetic, watt density in dry air and nitrogen, and the interlocks that matter.K15Electric thermal oil heaters for presses, platens and rollsHow to specify an electric thermal oil heater for presses, platens and rolls: duty and flow arithmetic, design ΔT across the plate, the 2.5 W/cm² heat-flux and 1.5-2 m/s velocity limits, circuit layout and the start-stop sequence.K16Electric heating for bitumen and asphalt storage tanksElectric heating for bitumen and asphalt storage tanks: why viscous stagnant product forces low watt density, standing-loss and melt-through sizing, element and sensing detail, and the operating habits that decide element life.K17Electric heaters for nitrogen and other inert gasesSizing electric heaters for nitrogen, argon and other inert gases: mass flow and cp arithmetic, a worked superheat example, why small kW still means high sheath temperature, velocity and pressure effects, and the interlocks.K18Immersion heaters for hydraulic oil reservoirsHow to choose an immersion heater for a hydraulic oil reservoir: viscosity targets, warm-up and standing-loss sizing, the 1-1.5 W/cm² static-oil limit, placement and control, and the four failures that destroy elements.K19Electric heating for CIP wash water and clean tanksElectric heating for CIP and wash-water tanks: kW from volume and recovery time, sheath material against caustic, acid and chlorine, watt density in tank duty, and surviving the drained phase between cycles.K20Electric reheat for cleanroom and pharmaceutical AHUsElectric reheat in cleanroom and pharmaceutical air handling: duty from airflow and ΔT, hygienic element construction, face velocity limits, SCR versus stepped control, and the interlocks and documentation a validated plant expects.K22What to send with an electric heater quotation requestThe nine data points and one sketch that make an electric heater inquiry quotable: process block, electrical block, mechanical envelope, spares, packing, documentation and what to say about what you do not know.K7What watt density should an electric heater tube use?How to calculate watt density, the working ranges for water, oil, still air and forced air, and the four mistakes that burn tubes: total power only, heated length, scaling and supply voltage.K8How to support a pipeline heater and allow for expansion?Bracket layout for pipeline heaters, expansion growth by material, why both-ends-fixed joints leak, and the cold-plus-hot commissioning checks.K9What protection settings does an electric thermal oil heater need?The four guards on electric thermal oil heaters — outlet high limit, low level, loss of circulation and sheath over-temperature — their action order, why film temperature governs, and typical missettings.