SS316 Peeler Basket Centrifuge
,Bottom Discharge Peeler Basket Centrifuge
,SS316 Horizontal Basket Centrifuge

The Scraper Bottom Discharge Centrifuge is designed for dense, high-solids crystalline slurry that requires controlled feeding, stable cake formation, centrifugal dewatering, and automatic bottom discharge.
It is particularly suitable when the crystal-to-liquor ratio is high, slurry concentration fluctuates between batches, or upstream crystallization produces intermittent peak loads that require controlled basket filling and reliable cake discharge.
For high-solids slurry, the main challenge is not only liquid removal. The equipment must also handle dense feeding, maintain an even cake layer, avoid basket overload, control cake thickness, and discharge the dewatered crystals reliably. The scraper bottom discharge design is well suited for these requirements.
- Concentrated crystal slurry discharged from evaporative crystallizers
- High crystal-to-liquor ratio slurry after upstream concentration
- Dense slurry transferred from crystallizer buffer tanks
- Crystal slurry with significant solids concentration fluctuation
- High-load batches requiring controlled basket filling
- Slurry requiring uniform cake thickness before spin drying
- Mother liquor recycle systems with elevated crystal loading
- Peak-load crystal slurry during crystallizer discharge
- Dense slurry generated during campaign changeover or crystallizer cleanout
- High-solids wet crystal transfer before downstream drying, screening, or storage
Peony provides separation support for the process section between crystallization and downstream drying, screening, packaging, or mother liquor recycle.
A typical system arrangement is:
Crystallizer / Evaporator → High-Solids Slurry Buffer Tank → Controlled Feed System → Scraper Bottom Discharge Centrifuge → Filtrate Collection or Recycle → Optional Cake Washing → Bottom Crystal Discharge → Dryer / Screen / Packaging
For high-solids slurry, a buffer tank and controlled feed arrangement are important. They help stabilize slurry concentration, prevent sudden overload, and maintain a more uniform cake layer inside the basket.
The separated mother liquor can be routed to an evaporator, crystallizer circulation loop, brine tank, solvent recovery section, or other designated recycle point.
Process Evaluation
Our engineers evaluate:
- Crystal type and crystal morphology
- Crystal size distribution and fines content
- Slurry solids concentration
- Slurry density and viscosity
- Cake permeability and filtration behavior
- Feed consistency and solids fluctuation
- Required batch capacity
- Target cake moisture
- Cake washing requirement
- Mother liquor recycle route
- Corrosion condition and material compatibility
Equipment Selection
We help customers determine:
- Basket diameter and working volume
- Maximum suitable batch loading quantity
- Feed rate and feed sequence
- Filter medium and support screen configuration
- Cake thickness control
- Washing system and wash-liquid distribution
- Spin-drying speed and cycle time
- Scraper structure and bottom discharge arrangement
- Filtrate collection and recycle connection
- Product-contact material and corrosion-resistant configuration
- PLC automation and overload protection logic
The high-solids crystalline slurry enters the rotating basket lined with filter media.
- Controlled Slurry Feeding
High-solids slurry is introduced into the rotating basket at a controlled rate to avoid uneven loading and excessive cake thickness. - Mother Liquor Filtration
Mother liquor passes through the filter medium and is collected through the filtrate outlet. - Crystal Cake Formation
Crystals are retained inside the basket and gradually form a dense filter cake on the basket wall. - Optional Cake Washing
Compatible wash liquid can be introduced to reduce residual mother liquor, soluble salts, or other impurities retained within the cake. - Spin Drying
The basket continues rotating at high speed to remove residual liquid from the crystalline cake. - Automatic Scraping
After the programmed cycle, the scraper removes the dewatered cake from the basket wall. - Bottom Discharge
The crystals are discharged through the bottom outlet for drying, screening, packaging, recycle, or further processing.
The complete cycle is controlled through PLC operation to maintain stable loading, repeatable dewatering, and automatic cake discharge.

Material Selection and Configuration Options
Material selection should be based on crystal composition, mother liquor chemistry, chloride concentration, pH, temperature, solvent content, and corrosion conditions.
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Component
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Typical Options
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Basket and casing
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SS304, SS316L, Duplex Stainless Steel, Super Duplex, or customized alloy
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Scraper assembly
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SS316L, Duplex Stainless Steel, or customized material
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Filter medium
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Perforated basket, metal screen, filter cloth, or customized filter media
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Feed piping
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SS316L, Duplex, PTFE-lined steel, or customized material
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Seals and gaskets
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PTFE, EPDM, FKM, silicone, or chemical-resistant materials
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Electrical configuration
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Standard or explosion-proof configuration
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Optional protection
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Nitrogen protection, vibration monitoring, load monitoring, or customized PLC logic
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Technical Parameter
| Model | Diameter | Volume | Capacity | Speed | G-force | Power | Weight | Dimension |
|---|---|---|---|---|---|---|---|---|
| PPSBD-140 | 800 mm | 100 L | 140 kg | 1500 rpm | 1008 | 11 kW | 3000 kg | 1800 × 1200 × 1670 mm |
| PPSBD-200 | 1000 mm | 150 L | 200 kg | 1200 rpm | 806 | 15 kW | 4000 kg | 2050 × 1500 × 2000 mm |
| PPSBD-200 | 1000 mm | 150 L | 200 kg | 1200 rpm | 567 | 15 kW | 4000 kg | 2050 × 1500 × 2000 mm |
| PPSBD-400 | 1250 mm | 280 L | 400 kg | 900 rpm | 567 | 18.5 kW | 5000 kg | 2350 × 1650 × 2450 mm |
| PPSBD-540 | 1250 mm | 400 L | 540 kg | 1000 rpm | 700 | 22 kW | 5000 kg | 2350 × 1650 × 2920 mm |
| PPSBD-540 | 1250 mm | 400 L | 540 kg | 1000 rpm | 700 | 22 kW | 5500 kg | 2400 × 1700 × 2920 mm |
| PPSBD-1200 | 1600 mm | 900 L | 1200 kg | 850 rpm | 647 | 37 kW | 8500 kg | 3000 × 2200 × 3300 mm |
Suitable for Dense Crystal Slurry
The centrifuge is designed for slurry with moderate to high crystal concentration. It can handle dense, filterable crystal feed while maintaining a controlled separation cycle.
Controlled Cake Thickness
Feed rate, batch loading quantity, and basket filling level can be controlled to avoid excessive cake thickness. This helps maintain better filtrate flow and more stable dewatering performance.
Reduced Mother Liquor Carryover
Centrifugal filtration and spin drying remove mother liquor from the crystal cake before downstream drying. This helps reduce liquid carryover and lowers the drying load.
Automatic Scraping for Dense Cake Discharge
High-solids slurry can form a thick cake inside the basket. The scraper mechanism removes the dewatered cake automatically and discharges it through the bottom outlet, reducing manual cleaning and handling.
Flexible Integration With Crystallization Lines
The centrifuge can be integrated with evaporators, crystallizers, MVR systems, slurry tanks, mother liquor recycle loops, dryers, and packaging systems to form a complete high-solids crystal handling section.
To recommend a suitable Scraper Bottom Discharge Centrifuge, please provide:
- Material name and crystal composition
- Crystal size distribution
- Slurry solids concentration
- Maximum and minimum solids fluctuation
- Mother liquor composition and viscosity
- Feed temperature
- Required capacity or batch volume
- Target cake moisture
- Cake washing requirement
- Mother liquor recycle requirement
- Corrosion condition
- Required material of construction
- Installation area and power supply
- Explosion-proof requirement, if applicable
Can the centrifuge handle high-solids crystal slurry directly?
Yes, provided the slurry is pumpable and the crystals can form a stable, permeable filter cake. A buffer tank and controlled feeding system are recommended where solids concentration changes significantly.
Why is feed control important for high-solids slurry?
High-solids slurry can form a thick cake quickly. Excessive or uneven feeding may reduce filtrate flow, create an uneven cake layer, and affect final moisture. Controlled batch loading helps maintain stable operation.
Can the centrifuge remove mother liquor from dense salt slurry?
Yes. Mother liquor passes through the filter medium while crystals remain inside the basket. High-speed spin drying further reduces liquid retained in the cake.
Can the cake be washed before scraping?
Yes. An optional wash system can be used to reduce residual mother liquor, soluble impurities, and surface contamination before final spin drying and discharge.
Is this machine continuous?
No. It is an automatic batch filtration centrifuge. However, it can work with continuous upstream crystallization or evaporation systems through a slurry buffer tank and programmed batch cycles.
Peony welcomes distributor and agent cooperation with salt producers, chemical manufacturers, evaporation and crystallization contractors, MVR system suppliers, wastewater salt recovery projects, and industrial separation partners.
We provide centrifuge selection, feed control guidance, filter medium matching, cake washing design, corrosion-resistant material selection, mother liquor recycle integration, installation guidance, commissioning support, spare parts, and after-sales service.
Send us your crystalline slurry data, solids concentration, particle size, mother liquor composition, target moisture, required capacity, and process layout. Our engineering team will help recommend a suitable high-solids slurry dewatering solution.
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