12000 – 13000rpm Industrial Dryer 800kg/H Spray Dry Machine LPG-1000
Industrial spray dryer with centrifugal atomization for efficient powder production. Features rapid drying for heat-sensitive materials, high powder recovery (≥95%), and customizable models. Includes 1-year warranty.
Brand Name:YiSheng
Place of Origin:CHINA
Product Custom Attributes
Highlight
12000rpm Industrial Dryer
,13000rpm Industrial Dryer
,800kg/H spray dry machine
Warranty:
One Year Free Repair Or Replacement
Type:
LPG-1000
Inlet Temperature (°C):
140–350 (Automatically Controlled)
Outlet Temperature (°C):
80–90
Water Evaporation Capacity (kg/h):
800
Revoluton Of Atomizer (rpm):
12,000–13,000
Diameter Of Atomizing Tray (mm):
180–210
Dried Powder Recovery Rate (%):
≥95
Application:
Chemical Industry
Usage:
Pharmaceutical Industry
Application Field:
Food Materials
Standard:
ROHS
Product Description
LPG-1000 spray dry machine
Descriptions:
Centrifugal spray drying is the most widely used method in the liquid processing and drying industry, ideal for transforming solutions, emulsions, suspensions, and pumpable pastes into uniform powders or granules—especially where tight control over particle size, residual moisture, bulk density, and morphology is critical (e.g., in pharma, food, chemicals, and ceramics).
The LPG series centrifugal spray dryers deliver scalable, reliable performance with these core specifications:
- Inlet temperature: 140–350 °C (PID-controlled)
- Outlet temperature: 80–90 °C (thermally gentle for sensitive materials)
- Atomization: High-speed centrifugal atomizer (12,000–25,000 rpm, mechanical or VFD-driven) for consistent droplet size
- Powder recovery rate: ≥95% via optimized cyclone and filtration
After the air is filtered by the filter, it is sent to the air heatexchanger by the blower for heating, and the heated air withcertain heat is sent to the air distributor at the top of the dryingtower. The hot air coming out of the hot air distributor entersthe drying chamber spirally and uniformly, and contacts with the centrifugally atomized feed liguid, so that the water in thefeed is vaporized, and the air containing dust enters the pulse bag separator for gas-solid separation, and the tall gas isdischarged by the ventilator.
features:
- The surface area of droplets is large, and the drving time of materials is short.
- Due to rapid drying, the humidity of the final product is not high, so the spray drying process is especially suitable fordrying heat-sensitive materials.
- Flexible operation, which can meet various product quality indicators, such as color, fragrance, taste, biological activityand final moisture content.
- Simplify the process flow, and the wet liguid can be directly made into powder in the drying tower.
| Item｜model | LPG-15 | LPG-25 | LPG-100 | LPG-150 | LPG-200 | LPG-500 | LPG-800 | LPG-1000 | LPG-2000 | LPG-3000 | LPG-4500 | LPG-6500 | |
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| Inlet Temperature (°C) | 140–350 (Automatically controlled) | ||||||||||||
| Outlet Temperature (°C) | 80–90 | ||||||||||||
| Way of Atomizing | High-speed centrifugal atomizer (Mechanical drive or variable frequency speed control available) | ||||||||||||
| Water Evaporation Capacity (kg/h) | 5 | 25 | 50 | 100 | 150 | 200 | 500 | 800 | 1000 | 2000 | 3000 | 4500 | 6500 |
| Revolution of Atomizer (rpm) | 25,000 | 22,000 | 21,500 | 18,000 | 18,000 | 16,000 | 16,000 | 12,000–13,000 | 11000-12000 | ||||
| Diameter of Atomizing Tray (mm) | 60 | 60 | 120 | 120 | 150 | 180–210 | Decided in accordance with therequirements of process | ||||||
| Max Electric Heating Power (kW) | 8 | 31.5 | 120 | 81 | 99 | ||||||||
| Dried Powder Recovery Rate (%) | ≥95 | ||||||||||||
| Length of Covered Area (m) | 1.6 | 4 | 4.5 | 5.2 | 7 | 7.5 | 12.5 | 13.5 | 14.5 | Decided in accordance theflow chart,conditionof filed and requirementsof customers | |||
| Width of Covered Area (m) | 1.1 | 2.7 | 2.8 | 3.5 | 5.5 | 6 | 8 | 12 | 14 | ||||
| Height of Tower Body (m) | 1.75 | 4.5 | 5.5 | 6.7 | 7.2 | 8 | 10 | 11 | 15 | ||||
| Hoisting Height of Nozzle (m) | — | 2.5 | 2.5 | 3.2 | 3.2 | 3.2 | 3.2 | 3.2 | 3.2 | ||||
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