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Low-Cake-Moisture Pusher Centrifuge for Soda Ash Dewatering

Low-Cake-Moisture Pusher Centrifuge for Soda Ash Dewatering

Brand Name: Peony
Model Number: HR
MOQ: 1set
Price: 35800
Packaging Details: Wooden packing
Payment Terms: T/T D/A D/P L/C
Detail Information
Place of Origin:
China
Certification:
CE
Temperature Allowed:
Below 105℃
Control System:
PLC
Operation:
Continuous Automatic
Product Name:
Basket Centrifuge
Size:
Customerized
Material:
SS304,SS316,DUPLEX SS As Option
Warranty:
1 Year
Application:
Soda Ash Dewatering
Supply Ability:
5 sets/month
Highlight:

Mechanical Pusher Centrifuge Machine

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Hr 800 Pusher Centrifuge Machine

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Plc Control Basket Centrifuge

Product Description
Low-Cake-Moisture Pusher Centrifuge for Soda Ash Dewatering
Low-Cake-Moisture Pusher Centrifuge for Soda Ash Dewatering 0
Description

Low-Cake-Moisture Pusher Centrifuge for Soda Ash Dewatering is designed for continuous dewatering and mother liquor separation of soda ash crystals, sodium carbonate crystals, and soda ash-related crystalline slurry in chemical production lines.

In soda ash production or sodium carbonate crystallization processes, the crystal slurry usually contains soda ash solids, alkaline mother liquor, dissolved salts, fine particles, and residual process liquid.

A pusher centrifuge removes free liquid through centrifugal filtration and continuously discharges a lower-moisture crystal cake before drying, cooling, screening, or packaging.


Typical Applications
  • Soda ash crystal dewatering
  • Sodium carbonate crystal dewatering
  • Sodium carbonate slurry solid-liquid separation
  • Mother liquor separation after crystallization
  • Soda ash wet cake discharge before drying
  • Sodium carbonate cake washing and dewatering
  • Alkali chemical crystal dewatering
  • Evaporation crystallization product dewatering
  • Continuous soda ash production line integration
  • Pre-drying dewatering before fluidized bed dryer or rotary dryer

What It Separates in Soda Ash Dewatering
Output Phase Typical Composition Main Purpose
Soda Ash Crystal Cake Sodium carbonate crystals, soda ash solids, alkali chemical crystals Recover lower-moisture crystal product before drying
Mother Liquor Alkaline process liquor, dissolved sodium salts, residual solution Separate liquid from crystals for reuse, recovery, or treatment
Wash Liquor Washing liquid after cake washing, if used Reduce residual mother liquor or soluble impurities

The actual separation result depends on crystal size, slurry concentration, alkaline liquor viscosity, screen opening, washing requirement, and operating parameters.


Why Low Cake Moisture Matters in Soda Ash Dewatering

Soda ash production usually requires stable moisture control before drying. If the wet cake contains too much mother liquor, the plant may face:

  • Higher dryer energy consumption
  • Unstable dryer feeding
  • Soda ash caking before or after drying
  • More residual alkaline liquor in the product
  • Lower product consistency
  • Higher load on cooling and screening equipment
  • More dust or agglomeration problems after drying
  • Higher operating cost in continuous production

A low-cake-moisture pusher centrifuge helps remove free mother liquor from soda ash crystals before drying. This makes downstream drying more stable and helps improve overall process continuity.


How the Pusher Centrifuge Works in Soda Ash Dewatering

Soda ash crystal slurry enters the centrifuge through the feed pipe and is evenly distributed onto the rotating screen basket.

Under centrifugal force, alkaline mother liquor passes through the screen openings and is collected as filtrate. Soda ash crystals are retained on the screen surface and form a filter cake.

The pusher mechanism moves the crystal cake forward step by step. During this movement, the cake continues to lose liquid. If product washing is required, wash liquid can be sprayed onto the cake to reduce residual mother liquor or soluble impurities.

Finally, the dewatered soda ash crystal cake is discharged continuously from the basket end and sent to the dryer, cooler, screening machine, packaging section, or next process stage.


Technical Parameter
Model PP-25 PP-40 PP-50 PP-60 PP-85
Diameter (mm) 200/251 290/360 438/500 560/630 738/820
Rotate speed (Max)(rpm) 3000 2500 2000 1360 1040
Stroke of Pusher Mechanism (times/min) 33-52 40-80 40-80 70-80 70-80
Main motor power (kw) 7.5 11-15 352-1140 286-1145 236-875
Main motor Protection class IP54/F1 IP54/F1 IP54/F1 IP54/F1 IP54/F1
Main motor Power supply 3 phase AC Customized 3 phase AC Customized 3 phase AC Customized 3 phase AC Customized 3 phase 380V/50HZ
Oil pump motor spec/Power(Kw) 4 NB4C100F SNE/A280 NB5D140F NBX6-F160F
Oil pump outflow(ml/turn) 100 100 480 140 180
Oil pump max pressure(Mpa) 2.5 2.5 2 8 8
Export Dimension(mm) 2155x1320x990 2346x1090x1006 3660x1420x2078 3127x1700x1955 3990x2000×1939
820x500x1650
Weight(kg) 1275 2600 4400 4860 6250

Main Advantages in Soda Ash Dewatering
Lower Soda Ash Cake Moisture

Centrifugal filtration removes free mother liquor from the soda ash cake, helping reduce moisture before drying.

Reduced Dryer Load

Lower moisture feed can reduce drying pressure and improve dryer operating stability.

Stable Crystal Cake Discharge

The pusher mechanism moves soda ash cake forward step by step, supporting continuous discharge and stable dryer feeding.

Product Washing Available

Cake washing nozzles can be added when residual mother liquor or soluble impurities need to be reduced.

Lower Product Loss

Proper screen opening helps retain soda ash crystals while allowing mother liquor to pass through.

Suitable for Alkali Chemical Production

Contact material and sealing options can be selected according to alkaline liquor composition and process conditions.

Easy Integration with Soda Ash Lines

The centrifuge can be connected with crystallizers, washing systems, dryers, coolers, screening machines, packaging systems, and mother liquor recovery systems.


Expected Results

Under suitable feed and operating conditions, the system can typically help achieve:

  • 4–12% wet cake moisture for many well-formed soda ash or sodium carbonate crystals
  • 50–85% reduction in free mother liquor carryover before drying compared with untreated wet slurry.
  • 95–99.5% soda ash crystal recovery when the screen opening is properly matched with particle size distribution.
  • 30–70% reduction of residual alkaline mother liquor in the cake when cake washing is applied.
  • 15–40% reduction in downstream dryer load
  • More stable wet cake feeding to dryer, cooler, screening machine, or packaging section.
  • Reduced risk of uneven drying, caking, and moisture fluctuation before final product handling.
  • 8–24 hours/day continuous operation

Final performance depends on soda ash crystal size, particle shape, slurry concentration, alkaline mother liquor composition, viscosity, screen opening, centrifugal force, washing condition, and operating parameters.


What Data Is Needed for Selection?

To recommend a suitable pusher centrifuge for soda ash dewatering, please provide:

  • Processing capacity
  • Feed material name: soda ash, sodium carbonate, or related crystal slurry
  • Feed slurry concentration
  • Solids content
  • Crystal size distribution
  • Crystal shape
  • Mother liquor composition
  • Mother liquor viscosity
  • Feed temperature
  • pH or alkalinity condition
  • Target wet cake moisture
  • Product washing requirement
  • Required product purity
  • Filtrate reuse or treatment requirement
  • Existing upstream crystallizer or washing system
  • Downstream dryer, cooler, screening machine, or packaging system
  • Required operating hours per day
  • Site voltage and control preference
  • Preferred material of construction
  • Required screen slot size, if known

FAQ
What is this pusher centrifuge used for?

It is used for continuous dewatering, mother liquor separation, and optional washing of soda ash or sodium carbonate crystals.

Why focus on low cake moisture?

Lower cake moisture reduces dryer load, improves dryer feeding stability, and helps control final product consistency.

Can it reduce dryer energy consumption?

Yes. By removing free mother liquor before drying, the centrifuge can reduce the amount of liquid that must be evaporated in the dryer.

Can the soda ash cake be washed inside the centrifuge?

Yes. Cake washing nozzles can be added to reduce residual mother liquor or soluble impurities.

What affects final soda ash cake moisture?

Final moisture depends on crystal size, cake permeability, slurry concentration, alkaline liquor viscosity, screen opening, centrifugal force, washing condition, and operating settings.


Contact Peony for Partnership

If you have customer resources or project opportunities in soda ash production, sodium carbonate crystallization, alkali chemical processing, or solid-liquid separation systems, Peony welcomes cooperation.

We support distributors, agents, and project partners with model selection, process advice, customized configuration, equipment manufacturing, installation guidance, spare parts, screen segment customization, and after-sales service.

Send us your material name, capacity, crystal size, solids content, mother liquor composition, and target cake moisture. Our team will help evaluate the suitable soda ash dewatering solution.