
The Scraper Bottom Discharge Centrifuge is designed for dewatering crystallized salt slurry discharged from MVR evaporation and crystallization systems.
In an MVR salt recovery process, water is removed through mechanical vapor recompression until the dissolved salt reaches supersaturation and crystals form. The resulting crystal slurry contains salt crystals, concentrated mother liquor, dissolved impurities, and residual process liquid. The centrifuge separates the crystals from the mother liquor, supports optional cake washing, reduces residual moisture, and automatically discharges the dewatered salt cake through the bottom outlet.
This equipment is particularly suitable for MVR systems where the upstream evaporation and crystallization section operates steadily while the downstream solid-liquid separation section works in automatic batches. An agitated slurry buffer tank is normally used between the MVR crystallizer and centrifuge to stabilize feed concentration and match crystallizer output with centrifuge cycle time.
Peony provides the solid-liquid separation section between MVR crystallization and downstream salt handling.
MVR Crystallizer → Agitated Slurry Buffer Tank → Scraper Bottom Discharge Centrifuge → Mother Liquor Recycle / Purge → Salt Drying / Screening / Packaging
The MVR crystallizer operates continuously, while the centrifuge works in automatic batches. An agitated slurry buffer tank connects the two sections, stabilizes crystal concentration, prevents settling, and supplies slurry to the centrifuge at a controlled rate.
Inside the centrifuge, mother liquor is separated from the crystal cake and collected for recycle, evaporation, or controlled purge. Optional cake washing can reduce residual mother liquor before drying. The scraper then removes the dewatered salt cake automatically through the bottom outlet.
The final configuration is selected based on crystal size, slurry solids concentration, mother liquor viscosity, recycle route, salt washing requirement, target moisture, and corrosion conditions.
The crystallized salt slurry is withdrawn from the MVR crystallizer or slurry buffer tank and fed into the rotating basket lined with filter media.
The complete cycle is automatically controlled through PLC operation to maintain stable batch dewatering and consistent coordination with the upstream MVR crystallization process.

Material selection should be based on actual mother liquor chemistry, chloride concentration, sulfate content, pH, temperature, dissolved oxygen, cleaning chemicals, and corrosion history.
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Component
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Typical Material Options
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|---|---|
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Basket and casing
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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 support structure
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SS316L or Duplex Stainless Steel
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Filtrate 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, or chemical-resistant customized materials
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High-corrosion service
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Titanium, nickel alloy, or other special materials when required
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Model
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Diameter
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Volume
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Capacity
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Speed
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G-force
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Power
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Weight
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Dimension
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|---|---|---|---|---|---|---|---|---|
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PPSBD-140
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800 mm
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100 L
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140 kg
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1500 rpm
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1008
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11 kW
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3000 kg
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1800 × 1200 × 1670 mm
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PPSBD-200
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1000 mm
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150 L
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200 kg
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1200 rpm
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806
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15 kW
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4000 kg
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2050 × 1500 × 2000 mm
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PPSBD-200
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1000 mm
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150 L
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200 kg
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1200 rpm
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567
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15 kW
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4000 kg
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2050 × 1500 × 2000 mm
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|
PPSBD-400
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1250 mm
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280 L
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400 kg
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900 rpm
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567
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18.5 kW
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5000 kg
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2350 × 1650 × 2450 mm
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PPSBD-540
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1250 mm
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400 L
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540 kg
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1000 rpm
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700
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22 kW
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5000 kg
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2350 × 1650 × 2920 mm
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PPSBD-540
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1250 mm
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400 L
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540 kg
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1000 rpm
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700
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22 kW
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5500 kg
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2400 × 1700 × 2920 mm
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PPSBD-1200
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1600 mm
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900 L
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1200 kg
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850 rpm
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647
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37 kW
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8500 kg
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3000 × 2200 × 3300 mm
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Efficient removal of mother liquor from sodium sulfate crystals.
Scraper mechanism automatically removes crystal cake after dewatering.
Handles high crystal concentration feed without clogging.
Achieves low final moisture content for downstream drying.
Ideal for medium and large-scale sodium sulfate production plants.
Available in SS304, SS316L, Duplex Stainless Steel, Titanium, and other special materials.
To recommend a suitable centrifuge configuration for an MVR crystallized salt system, please provide:
Yes. A slurry buffer tank is normally installed between the MVR crystallizer and centrifuge. It stabilizes the feed and allows the centrifuge to operate in repeatable automatic batches.
Yes. The filtrate can be returned to the MVR crystallizer, evaporator circulation loop, mother liquor tank, or another designated recycle point. A purge stream may be required where impurities accumulate in the recycle loop.
It depends on the salt solubility and product specification. For highly soluble salts, unrestricted condensate washing may cause dissolution loss or disturb water balance. Saturated brine or another compatible wash liquid may be more suitable.
Yes, provided the slurry remains pumpable and the crystals form a stable, permeable cake. Feed control and appropriate basket loading are important for reliable operation.
The scraper automatically removes and discharges the dewatered salt cake through the bottom outlet, reducing manual handling and supporting stable transfer to downstream drying or salt handling equipment.
Peony welcomes distributor and agent cooperation with MVR system suppliers, evaporation and crystallization contractors, ZLD project companies, salt recovery specialists, industrial wastewater treatment contractors, and salt production partners.
We support partners with centrifuge selection, MVR process integration, slurry buffer design, mother liquor recycle arrangement, cake washing configuration, corrosion-resistant material selection, automation support, spare parts, and after-sales service.
Send us your MVR crystallized salt slurry data, process flow, mother liquor composition, crystal size, required capacity, target moisture, recycle route, and corrosion conditions. Our engineering team will recommend a suitable Scraper Bottom Discharge Centrifuge solution.