FZG Vacuum Tray Dryer for New-Energy Lithium-Ion Battery Materials: Nickel-Manganese-Cobalt Hydroxide Precursor
FZG Vacuum Tray Dryer is evaluated for nickel-manganese-cobalt hydroxide precursor in new-energy lithium-ion battery materials. The defined feed is washed hydroxide precursor cake. Review the material-specific operating requirements below alongside the original equipment specifications.
Nickel-Manganese-Cobalt Hydroxide Precursor: Application and Process Requirements
For nickel-manganese-cobalt hydroxide precursor, preserve precursor chemistry and particle morphology; washing salts are not removed by drying. Start with washed hydroxide precursor cake, and identify the volatile phase and incoming variability before choosing a cycle.
Feed, Quality and Downstream Interface
| Review item | Nickel-Manganese-Cobalt Hydroxide Precursor |
|---|---|
| Defined feed | washed hydroxide precursor cake |
| Material-specific focus | preserve precursor chemistry and particle morphology; washing salts are not removed by drying |
| Product quality checks | residual moisture, soluble salts, metal ratios and agglomerate size |
| Downstream handling | controlled transfer to the subsequent cathode synthesis step |
Loading and Material Movement
Set layer depth, loading distribution and tray position; inspect the slowest drying locations.
Include residual moisture, soluble salts, metal ratios and agglomerate size in the trial record. Define the sampling locations and analytical methods before the test; a result from a different grade, loading pattern or residual liquor cannot establish the operating endpoint for this feed.
Material-Specific Configuration
Vacuum Tray Dryer selection for this feed should be assessed alongside the industrial vacuum dryer process description. Evaluate low-temperature vacuum drying and heat-sensitive material drying with representative nickel-manganese-cobalt hydroxide precursor. This chemical powder drying application requires a material-specific sampling and acceptance plan.
After the batch meets the agreed specification, arrange controlled transfer to the subsequent cathode synthesis step. Examine the effect of discharge, temporary holding and packaging exposure on the measured product condition. Establish the usable batch and cycle for this material; the original model parameters below remain the equipment reference, not a throughput promise for every formulation.
View the FZG Vacuum Tray Dryer range and original equipment specifications
Technical References for This Application
Keep the powder-drying duty separate from cell electrochemistry and performance qualification. U.S. DOE battery-material context.
Specify the intended cathode chemistry and precursor or finished-powder stage. U.S. DOE cathode-material chemistry reference.
Review the supplier SDS for the actual grade and residual process liquor. HSE safety-data-sheet guidance.
Assess charging, sampling, cleaning and discharge around the selected material. HSE process exposure assessment.
Define the heat-transfer duty and utilities rather than assuming a universal drying cycle. U.S. DOE process-heat reference.
Equipment Reference Parameters
These are the FZG Vacuum Tray Dryer model specifications. The operating duty for nickel-manganese-cobalt hydroxide precursor must be established from the feed and the finished-product requirements above.
| Item | YZG-600 | YZG-1000 | YZG-1400 | FZG-8 | FZG-15 | FZG-20 | FZG-30 | FZG-45 |
|---|---|---|---|---|---|---|---|---|
| Internal Chamber Dimensions (mm) | Φ600×976 | Φ1000×1527 | Φ1400×2054 | 1140×890×1400 | 1500×1220×1400 | 1500×1800×1400 | 3200×1220×1400 | 3200×1220×1700 |
| Overall Dimensions (mm) | 1150×810×1020 | 1740×1226×1385 | 2386×1657×1800 | 1580×1203×1924 | 2060×1513×1924 | 2060×1883×1924 | 3760×1513×1924 | 3760×1513×2224 |
| Shelf Layers | 4 | 6 | 8 | 8 | 8 | 8 | 8 | 12 |
| Layer Spacing (mm) | 81 | 98 | 102 | 122 | 122 | 122 | 122 | 102 |
| Tray Dimensions (mm) | 310×600×45 | 640×460×45 | 640×460×45 | 640×460×45 | 640×460×45 | 640×460×45 | 640×460×45 | 640×460×45 |
| Number of Trays | 4 | 12 | 32 | 16 | 32 | 48 | 64 | 96 |
| Capacity (kg) | 5 | 30 | 60–80 | 30–40 | 60–80 | 100–120 | 130–150 | 200–240 |
| Allowable Heating-Pipe Pressure (MPa) | ≤0.784 | ≤0.784 | ≤0.784 | ≤0.784 | ≤0.784 | ≤0.784 | ≤0.784 | ≤0.784 |
| Operating Temperature (°C) | 35–150 | 35–150 | 35–150 | 35–150 | 35–150 | 35–150 | 35–150 | 35–150 |
| No-Load Chamber Vacuum (MPa) | −0.09 to −0.096 | −0.09 to −0.096 | −0.09 to −0.096 | −0.09 to −0.096 | −0.09 to −0.096 | −0.09 to −0.096 | −0.09 to −0.096 | −0.09 to −0.096 |
| Vacuum-Pump Model and Power | SK-1.5, 3 kW | SK-3, 5.5 kW | SK-6, 11 kW | SK-3, 5.5 kW | SK-6, 11 kW | SK-6, 11 kW | SK-12, 18.5 kW | SK-12, 18.5 kW |
| Weight (kg) | 400 | 900 | 1400 | 1400 | 2300 | 2800 | 3500 | 4800 |
| Selection Item | Information Required |
| Material | Composition, consistency and bulk density |
| Batch | Required loading quantity and production schedule |
| Moisture | Initial moisture and target final moisture |
| Temperature | Product temperature limit and heating utilities |
| Vacuum | Process pressure and expected vapor load |
| Construction | Contact materials, seals and cleaning requirements |
| Installation | Space, access and process connections |
Discuss Nickel-Manganese-Cobalt Hydroxide Precursor Drying
Send QUANPIN the incoming nickel-manganese-cobalt hydroxide precursor specification, sample information and the required final product condition for an equipment review.
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