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.
Power per share of the balance, with its part of the total fuel energy.
Thermal cost per ton of dried product for other inlet moistures, keeping final moisture and efficiency. The highlighted point is the current one.
Values per operating hour and per month, for the production report.
Take this page’s results to another calculator with the fields already filled in.
The calculation report gathers this page's inputs, results, equations, assumptions and references, with fields for project, engineer and revision. The full report also includes the charts and interpretations, in color. In the print dialog, choose Save as PDF.
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.
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.
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.
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.
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.
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.
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.
Important notice: Indus Metrics tools produce estimates and pre-sizing results from the data you enter and from published engineering methods. They do not replace design, calculations or reports signed by a licensed professional engineer (PE), nor verification against the applicable codes, standards and regulations, such as OSHA rules and the ASME codes. Material and fuel properties vary: check manufacturer data or your own process analyses before deciding. By using this site you agree to the Terms of Use.
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