Crystalline salts
High-concentration salt crystals and comparable free-filtering inorganic products.
Screw-feed horizontal filtration
Continuous screen filtration with scroll discharge. The screw-feed arrangement is a requested configuration to be confirmed; no variant-specific capacity or power is stated.
Product Essentials
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Screw-Feed Horizontal Filtration Centrifuge Technical Data
Reference performance values for the four screw-feed horizontal filtration centrifuge configurations. Confirm material conditions and final configuration before selection.
| Model | Bowl diameter (mm) | Bowl speed (r/min) | Separation factor | Production capacity (N/min) | Main motor power (kW) | Machine weight (kg) | Overall dimensions (mm) |
|---|---|---|---|---|---|---|---|
| Model 1 | 350 | 2500 | 1765 | 1–5 | 11 | 1400 | 2300 × 1180 × 1000 |
| Model 2 | 450 | 2500 | 1575 | 2–8 | 22 | 2000 | 2360 × 1210 × 1040 |
| Model 3 | 530 | 2000 | 1190 | 3–10 | 30 | 2800 | 2650 × 1350 × 1230 |
| Model 4 | 630 | 1800 | 1140 | 5–15 | 37 | 4200 | 3050 × 1580 × 1400 |
Source reference values. Production-capacity ranges indicate the supplied configurations; final dimensions, materials and performance are confirmed during engineering.
Applications
Applications include crystalline salts and chemical products. Confirm material properties and process conditions before selecting the equipment configuration.
High-concentration salt crystals and comparable free-filtering inorganic products.
Crystalline and granular chemicals with good filtration behavior and no strict particle-breakage limit.
Fibers, crop hulls and related coarse solids after process review.
Plastic granules and similar particulate materials suitable for continuous screen filtration.
Chemical, food, salt, mining, pharmaceutical and high-salinity wastewater processing.
Working Principle
The process route is selected around the material and product targets.
Confirm the drive, feed arrangement and control functions for the selected filtration duty.
Liquid passes through the filter screen and basket openings, while solids are retained on the screen surface.
The retained solids form a cake and remain under centrifugal force for continued liquid removal.
Relative speed between the basket and scroll transports the cake continuously toward the solids-discharge end.
Dewatered solids leave automatically while filtrate exits through the separate liquid route.
Performance Highlights
Final performance remains dependent on feed properties and engineering confirmation.
Liquid passes through the screen while retained solids are conveyed to discharge.
Drive type, feed equipment, scroll speed and protection functions must be specified for the selected material.
System Configuration
Core equipment and auxiliary systems are selected around the process duty.
Confirm the drive, feed arrangement and control functions for the selected filtration duty.
Steady feed reduces loading fluctuations and promotes more uniform entry into the filtration zone.
Screen opening and basket geometry are selected for particle retention, filtrate capacity and cake dewatering.
Controlled relative basket-to-scroll speed conveys the retained cake continuously to discharge.
Feed, basket and discharge functions can be coordinated for stable automatic operation.
A straightforward machine arrangement supports routine inspection, cleaning and maintenance.
Selection Support
Share the following process information for an efficient preliminary review.