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Spray Dryer Evaporation & Sizing Calculator engineering
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Spray Dryer Evaporation & Sizing Calculator

Calculate spray dryer water evaporation capacity, dry powder yield, required drying air SCFM, thermal efficiency, and heat duty.

Liquid Feed Slurry / Solution

Drying Air Temperatures

Spray Drying Sizing Results

Evaporation Capacity
-- lb/hr
-- GPH water
Powder Production
-- lb/hr
-- kg/hr
Thermal Efficiency
--%
(Tin - Tout)/(Tin - Tamb)
Process Air Flow: -- SCFM
Heater Duty: -- MMBTU/h (-- kW)
Specific Heat: -- BTU / lb H2O
Increasing feed solids by pre-evaporating in a falling film evaporator cuts spray dryer size and gas fuel consumption exponentially.

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Frequently Asked Questions

Why is pre-concentration critical before spray drying?

Evaporating water thermally in a spray dryer requires approximately 1,800 to 2,500 BTU per pound of water. In contrast, mechanical vapor recompression (MVR) or multiple-effect evaporators remove water for 150 to 300 BTU per pound—roughly 80-90% cheaper. Maximizing feed solids prior to atomization saves massive fuel expense.

What is the relationship between droplet size and spray dryer chamber height?

Droplets must completely dry to non-sticky powder before striking the chamber walls or bottom cone. Drying time scales with the square of droplet diameter (t ~ d²). Coarse atomization (150-250 microns) produces excellent free-flowing, dust-free granules but requires a tall, wide drying tower with high residence time.

What governs the selection of inlet vs outlet drying air temperatures?

Inlet temperature is capped by heat sensitivity of the product (e.g. 320°F-380°F for milk powder or pharmaceuticals to avoid caramelization/denaturation; up to 900°F for inorganic catalysts or ceramics). Outlet temperature is dictated by the equilibrium relative humidity needed to reach target residual moisture.