3–1000 kg/h max water evaporation
High-speed centrifugal (12k-27k rpm)
Inlet: 130–300°C / Outlet: 70–90°C
Cyclone + Bag filter (configurable)
Electric, steam, gas, or thermal oil
Adapted to factory layout & hygiene
Beyond standard milk, our drying systems are evaluated and selected based on specific feed solids, viscosity, and thermal sensitivity. Note: Sanitary grades, cleaning protocols, and regulatory compliance for infant formula must be confirmed per project design.
Milk powder spray drying atomizes concentrated liquid dairy feed into fine droplets and contacts those droplets with controlled hot air. Moisture evaporates rapidly, while dry particles are separated and collected from the exhaust air.
This process is highly suitable for continuously converting liquid dairy concentrates into stable powders because the rapid evaporation keeps the droplet temperature relatively low, protecting heat-sensitive proteins. However, fast drying does not guarantee "zero nutrient loss"—the exact retention depends heavily on operating temperatures.
The final powder quality is not determined by the dryer alone. It is a combined result of upstream feed pretreatment, concentration levels, atomization speed, inlet/outlet temperatures, air distribution within the chamber, particle residence time, and subsequent downstream processing like agglomeration or cooling.
Understanding the equipment boundary is critical. Homogenization, pasteurization, vacuum concentration, fluid-bed cooling, and packaging are upstream or downstream systems—not built-in functions of the spray drying tower itself.
Raw milk is standardized, pasteurized, and concentrated (typically via falling film evaporators) to increase total solids before drying.
The concentrated dairy feed is pumped from a buffer tank to the atomizer at a controlled rate using a screw or diaphragm pump.
A high-speed centrifugal disc or high-pressure nozzle shears the liquid into millions of fine droplets, vastly increasing the surface area.
Droplets mix with filtered, heated air in the drying chamber. Moisture evaporates instantly, leaving dry milk particles.
Dry powder falls to the chamber bottom or is carried by exhaust air to cyclone separators and bag filters for collection.
Powder is often cooled in a fluid bed (optional agglomeration step) and sifted before final hygienic packaging.
The LPG Series covers reference water-evaporation duties from 3 to 1,000 kg/h. The three configurations below represent typical small, medium and large systems for preliminary comparison. Final model selection, tower dimensions and operating conditions depend on the feed properties, required evaporation load, target powder characteristics and collection-system design.
Representative Model: LPG-5
Typical positioning: Small-volume production and preliminary process evaluation
Representative Model: LPG-100
Typical positioning: Continuous small-to-medium industrial production
Representative Model: LPG-1000
Typical positioning: High evaporation duties requiring complete utility, installation and site-layout engineering
The complete LPG range also includes LPG-25, LPG-50, LPG-150, LPG-200 and LPG-500 configurations. Contact our engineering team for the full model table and a recommendation based on your feed data.
Spray dryer capacity refers to the maximum amount of water evaporated under reference operating conditions. It is not the total liquid-feed rate or the finished-powder output. Actual performance depends on feed composition, solids concentration, inlet and outlet conditions, atomization and powder-collection configuration.
Important: Capacity is stated as maximum water evaporation, not finished powder output.
| Model | Max Water Evaporation (kg/h) | Atomizer Speed (rpm) | Transmission Power (kW) | Listed Heating Power (kW) | Tower Diameter (m) | Overall Height (m) |
|---|---|---|---|---|---|---|
| LPG-5 | 3–7 | 25,000 | 4.2 | 18 | Φ1.2 | 2.2 |
| LPG-25 | 18–25 | 18,000–27,000 | 14 | 36 | Φ1.9 | 3.6 |
| LPG-50 | 35–50 | 18,000–27,000 | 18 | 48 | Φ2.2 | 4.6 |
| LPG-100 | 75–100 | 18,000–27,000 | 23 | 72 | Φ2.56 | 5.4 |
| LPG-150 | 120–150 | 15,000–18,000 | 29 | 84 | Φ2.96 | 6.3 |
| LPG-200 | 170–210 | 15,000–18,000 | 43 | 96 | Φ3.36 | 7.0 |
| LPG-500 | 400–500 | 12,000–15,000 | 76 | 144 | Φ5.2 | 9.2 |
| LPG-1000 | 800–1000 | 12,000–15,000 | 109 | 144 | Φ7.6 | 12.4 |
A common mistake in procuring a milk powder spray dryer is confusing water evaporation capacity with finished powder output. Industrial dryers are sized based on how much water they must remove, which depends entirely on your feed's solid content.
Finished powder output (P):
P = F × S ÷ (1 - M)
Water evaporation (E):
E = F - P
*Illustrative calculation only. Example: 1000 kg/h feed at 40% solids dried to 4% moisture yields ~416 kg/h powder, requiring ~584 kg/h water evaporation (selecting an LPG-1000).
While the LPG Series uses high-speed rotating discs, we also offer the YPG Series Pressure Spray Dryer (working pressure 1.6–2.5 MPa via diaphragm pump). Neither is universally "better" for all milk powder projects; selection depends on viscosity, target particle size, and maintenance conditions.
| Comparison Factor | LPG (Centrifugal) | YPG (Pressure Nozzle) |
|---|---|---|
| Atomization Principle | High-speed rotating disc shearing | High-pressure liquid forced through orifice |
| Feed Pressure Requirement | Low (pumped to top of tower) | High (1.6–2.5 MPa via diaphragm pump) |
| Control Variables | Disc speed (rpm) & feed rate | Pump pressure & nozzle core size |
| Feed Characteristics | Handles slight viscosity variations well | Requires strict filtration; prone to blockage |
| Typical Particle Size | Finer, more uniform distribution | Often larger, hollow spheres (better flowability) |
| Maintenance Focus | Spindle bearings & dynamic balance | Nozzle wear & high-pressure pump seals |
* Note: Instant milk powder requiring specific agglomeration, fines return, or fluid-bed treatment is an optional system design subject to engineering confirmation.
We design our systems recognizing that buyers care about powder performance, not just machine structure. No single parameter guarantees quality; it requires a holistic process balance.
Operational issues often stem from a mismatch between feed properties and equipment settings. Our engineering response focuses on identifying the root cause.
| Problem | Possible Cause | Engineering Response |
|---|---|---|
| Powder sticking to chamber wall | High moisture, low exhaust temp, or improper air distribution. | May be improved by adjusting atomizer speed, increasing outlet temp, or adding air sweepers (depending on configuration). |
| Low powder collection rate | Cyclone inefficiency or bag filter blinding. | Requires checking cyclone pressure drop and pulse-jet cleaning frequency on bag filters. |
| High final moisture | Low inlet temp, high feed rate, or low feed solids. | Reduce feed rate or increase inlet temp (subject to product heat sensitivity). |
| Excessive fines and dust | Atomizer speed too high (droplets too small). | Lower RPM on centrifugal disc; optional fines return system can agglomerate dust. |
| Poor solubility / dispersibility | Overheating, lack of agglomeration, or high fine particle ratio. | Requires confirmation through feed testing; may require secondary fluid-bed drying/cooling. |
| Hopper bridging & poor discharge | Powder too warm or hygroscopic absorbing moisture. | Install pneumatic hammers or air pads; ensure dehumidified cooling air. |
We deliver tangible engineering value for dairy projects, built on
Benefit: Allows operators to fine-tune droplet size and bulk density.
Condition: Achieved via VFD control on the centrifugal atomizer, within the motor's rated RPM range.
Benefit: Maximizes powder recovery (brochure-listed ≥97%) while meeting local emission standards.
Condition: Cyclone, bag-filter, or combined setups are selected based on dust limits and budget.
Benefit: Fits into existing factory buildings without unnecessary civil modification costs.
Condition: System layout adapted to available installation height and floor space during the drawing phase.
Benefit: Reduces downtime between product changeovers.
Condition: Quick-open doors and manual cleaning points are standard; automated CIP is optional and subject to confirmed design.
Follow this 7-step engineering flow to ensure the equipment matches your dairy process.
Identify if it's whole milk, skim milk, whey, or a formulated blend. Heat sensitivity dictates temperature limits.
Determines how much water must be removed.
Define acceptable moisture, bulk density, and instant properties.
Use the mass balance formula to select the base LPG or YPG model.
Choose between centrifugal disc (LPG) and pressure nozzle (YPG) based on viscosity and particle needs.
Configure air heating (steam/electric/gas) and powder collection (cyclone/bag filter).
Finalize hygiene (e.g., CIP options), layout dimensions, and local safety standards.
For new formulations or stringent powder requirements, we advocate a "test, evaluate, scale-up" approach.
Trust is built on visible manufacturing capability. From stainless-steel fabrication to
From initial requirement analysis to lifelong support, we ensure a seamless and transparent journey for your custom drying system.
Review
Confirmation
Process & Equip
Utility confirm
Fabrication
Factory acceptance
Packing
Guidance
Operator
Spare parts
A complete spray drying system engineered, manufactured, and successfully commissioned by JEXDRY for a commercial dairy processing facility.
Submit your raw material and target parameters. Our engineers will calculate the water evaporation load, recommend an initial LPG or YPG model, and suggest heat sources, collection methods, and optional downstream configurations.
Email Us
zar@jexdry.com
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+86 137 7501 3369