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Industrial drying: moisture balance and thermal cost

Enter the feed rate, inlet and outlet moisture and the dryer type to see how much water leaves per hour, how much energy that takes, how much fuel the dryer burns and what each ton of dried product costs.

Pre-sizing and estimating tool: results do not replace design, calculations or reports signed by a licensed professional, nor verification against the applicable codes and standards.

Preliminary estimateRevised 11/02/2026
Material and moisture
Dryer
Energy

The dryer type suggests a typical efficiency; replace it with a measured value whenever you can. With the air balance, the efficiency comes out as a result.

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—Thermal cost per ton of dried product
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Where the energy goes

Power per share of the balance, with its part of the total fuel energy.

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Cost versus inlet moisture

Thermal cost per ton of dried product for other inlet moistures, keeping final moisture and efficiency. The highlighted point is the current one.

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Mass and energy balance

Values per operating hour and per month, for the production report.

Next step

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Method, assumptions and references

Equations used

Dry basis X = w ÷ (1 − w); wet basis w = X ÷ (1 + X)
Dry matter Ms = m₀ · (1 − w₀); product mf = Ms ÷ (1 − wf); water evaporated = m₀ − mf (1,000 kg from 30% to 10% → 222.2 kg)
Useful heat = Ms·cp_s·(T_out − T_in) + m_water,final·4.18·(T_out − T_in) + m_evap·[4.18·(T_evap − T_in) + h_fg(T_evap)]
Source energy = useful heat ÷ η_dryer or ṁ_air · 1.02 · (T_air − T_amb) ÷ η_heater; specific consumption = energy ÷ water evaporated
Fuel = energy ÷ LHV (ISO 18125 for wet biomass); steam = energy ÷ h_fg(p); cost/t = hourly cost ÷ dried product (t/h)

Assumptions and limits

  • Continuous operation (or the average of a batch), only water evaporated (no volatiles), latent heat of pure water at the evaporation temperature (IAPWS-IF97); bound water in hygroscopic materials takes slightly more energy than free water.
  • Efficiencies by dryer type are approximate literature ranges and vary widely with material, final moisture, air recirculation and equipment condition; measure yours. In the air balance, humid air specific heat is taken as 0.244 Btu/(lb·°F) and the air outlet temperature is estimated without wall losses.
  • It does not compute drying time or kinetics (constant and falling rate) nor size the dryer; it is for balances, budgets and tracking consumption.

Standards and technical documents

  • Mujumdar, A. S. (ed.). Handbook of Industrial Drying, 4th ed. CRC Press, 2014
  • Kudra, T. Energy aspects in drying. Drying Technology, 22(5), 2004, p. 917–932
  • Kemp, I. C. Fundamentals of energy analysis of dryers. In: Tsotsas, E.; Mujumdar, A. S. (eds.) Modern Drying Technology, Vol. 4. Wiley-VCH, 2012
  • Green, D. W.; Perry, R. H. Perry’s Chemical Engineers’ Handbook, 8th ed. McGraw-Hill, 2008, Section 12 (psychrometry, evaporative cooling and solids drying)
  • ISO 18125: Solid biofuels — Determination of calorific value
  • IAPWS-IF97: Industrial Formulation 1997 for the Thermodynamic Properties of Water and Steam

U.S. regulations

  • NFPA 86: Standard for Ovens and Furnaces (Class A ovens and dryers)
  • NFPA 652: Standard on the Fundamentals of Combustible Dust; NFPA 61 for agricultural and food processing facilities
  • OSHA 29 CFR 1910.272: Grain handling facilities (dryers and dust)

Frequently asked questions

What does this calculator do?

It runs the mass and energy balance of a dryer: how much water leaves per hour, how much dried product is left, how much energy that takes and how much fuel and money the dryer uses per hour, per month and per ton. Use it to budget drying a new material, compare fuels, track dryer efficiency and show what wetter raw material costs.

How do I calculate water evaporated?

Dry matter goes in and out unchanged. 1,000 lb at 30% moisture (wet basis) holds 700 lb of dry matter; at 10%, those 700 lb become 700 ÷ 0.90 = 777.8 lb of product. The difference, 222.2 lb, is the water evaporated. Simply taking 20% of 1,000 lb (200 lb) is wrong: the correct math goes through dry matter.

What is the difference between wet basis and dry basis?

Wet basis divides water by total mass and is what moisture balances read; dry basis divides by dry mass and is common for lumber and grain. To convert, db = wb ÷ (1 − wb): 30% wb equals 42.9% db and 10% wb equals 11.1% db. Pick the basis in the first field; when you switch, the calculator converts the values entered.

Where does the energy go and which efficiency should I use?

Useful heat adds heating of the solid and the water plus the latent heat to evaporate (about 1,024 Btu/lb at 122 °F); in the example, 0.51 MMBtu/h, 89% of it for evaporation. Divided by dryer efficiency it gives fuel energy: a direct rotary dryer at 55% needs 0.93 MMBtu/h, or about 1,005 scf/h of natural gas. Typical ranges by type (tray 35–40%, rotary 40–70%, fluid bed 40–80%) come from the literature; measure yours from a day of real fuel use.

How do I read the example cost and specific consumption?

With natural gas at $6 per MMBtu, the dryer spends $6.22 an hour, $8.00 per short ton of dried product and about $2,490 a month over 400 hours. Specific consumption is 2,095 Btu per pound of water evaporated, inside the typical 1,646 to 2,881 Btu/lb for direct rotary dryers; above the range, look for air leaks, poor insulation or excess exhaust.

What does extra moisture in the raw material cost?

A lot, because water to evaporate grows faster than moisture. In the example, material arriving at 35% instead of 30% raises cost from $8.00 to $10.56 per short ton of dried product, 32% more. Covering the yard, letting material drain before drying and negotiating moisture discounts usually pay back quickly.

What are the limits and the safety precautions?

This is an average steady-state balance for water only; it does not compute drying time, kinetics or dryer size, and the typical efficiency is only a starting point. Wood, grain and food dusts can form explosive clouds and catch fire in the dryer: housekeeping, temperature control and explosion protection should follow your hazard analysis under NFPA 652 and NFPA 61, and fired dryers fall under NFPA 86.