| Brand Name: | Peony |
| Model Number: | PP |
| MOQ: | 1 set |
| Price: | USD25000~120000/SET FOB SHANGHAI |
| Packaging Details: | Standard export packings |
| Payment Terms: | T/T,L/C,Western Union |
A crystal washing and mother liquor removal pusher centrifuge is designed for continuous filtration, washing, dewatering, and discharge of crystalline products after crystallization. It is mainly used when the crystal cake contains residual mother liquor, soluble impurities, by-products, or process liquid that must be reduced before drying or further processing.
In many chemical, salt, and fertilizer crystallization processes, separation is not only about removing free liquid. The remaining mother liquor on the crystal surface may affect product purity, color, impurity level, downstream drying stability, and final product quality. A pusher centrifuge allows the crystal cake to move through filtration and washing zones continuously, helping remove mother liquor while maintaining stable solids discharge.
This type of centrifuge is suitable for filterable crystals with good cake-forming behavior, especially where continuous operation, controlled washing, low liquid carryover, and stable wet cake discharge are required.
| Material Type | Process Source | Main Purpose |
|---|---|---|
| Salt crystals | Evaporation or cooling crystallization | Remove brine and reduce residual mother liquor |
| Fertilizer crystals | Crystallization or reaction slurry | Improve wet cake quality before drying |
| Chemical crystals | Fine chemical or intermediate production | Reduce soluble impurities and process liquid carryover |
| Inorganic salt crystals | Salt chemical crystallization | Separate crystals and recover mother liquor |
| Nitrate crystals | Chemical or fertilizer process | Wash crystal cake and reduce impurity residue |
| Ammonium sulfate crystals | Fertilizer crystallization | Remove mother liquor before dryer feeding |
| Potassium chloride crystals | Potash or brine process | Reduce brine carryover and improve product handling |
| Soda ash crystals | Alkaline crystallization process | Remove alkaline mother liquor from crystal cake |
The pusher centrifuge is usually installed after the crystallizer, thickener, or slurry feed tank.
Typical process route:
Crystallization → Slurry feeding → Centrifugal filtration → Cake washing → Mother liquor removal → Wet cake discharge → Drying / Cooling / Screening / Packaging
For processes requiring filtrate separation:
Crystallizer slurry → First filtrate collection → Washing zone → Wash filtrate collection → Crystal cake discharge
In some projects, mother liquor and wash filtrate may need to be collected separately. This depends on whether the liquid will be reused, returned to the crystallizer, sent to recovery, or discharged for further treatment.
The crystal slurry enters the rotating screen basket through the feed pipe. Under centrifugal force, the mother liquor passes through the screen openings and is collected as filtrate. The crystals remain on the screen surface and form a filter cake.
As the pusher mechanism moves the cake forward, the cake continues to dewater. If washing is required, wash liquid is sprayed evenly onto the moving cake layer. This helps dilute and remove residual mother liquor from the crystal surface.
After washing and further dewatering, the wet crystal cake is discharged continuously from the basket end. The filtrate and wash liquid are collected through the process housing and sent for reuse, recovery, or further treatment.
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| 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 |
Crystal size directly affects washing and dewatering performance.
Coarse and uniform crystals usually allow wash liquid to pass through the cake more evenly. Fine or irregular crystals may cause poor permeability, screen blockage, higher filtrate turbidity, and lower washing efficiency.
Mother liquor may contain salts, organic impurities, soluble by-products, acids, alkalis, or corrosive components. Its composition affects material selection, filtrate collection design, corrosion resistance, and washing strategy.
Before selection, the mother liquor concentration, pH, chloride content, temperature, and viscosity should be confirmed.
Not every crystal requires washing. For some products, simple mother liquor removal is enough. For higher-purity products, the washing zone becomes important.
The wash liquid type, spray amount, distribution method, cake thickness, and residence time should be designed according to product purity requirements.
Some processes require mother liquor and wash filtrate to be collected separately. This is common when mother liquor needs to be returned to the crystallizer or when wash filtrate has a different concentration.
In this case, the process housing and filtrate collection structure should be designed accordingly.
Lower cake moisture can reduce dryer load, but final moisture depends on crystal size, cake thickness, screen opening, centrifugal force, washing amount, and residence time.
The practical goal is to achieve a stable wet cake suitable for downstream drying, not to pursue unrealistic moisture reduction only by centrifugation.
Crystal slurry may be abrasive, while mother liquor may be corrosive. Wetted parts, screen basket, pusher components, and discharge areas should be selected based on actual working conditions.
Common options include stainless steel, duplex stainless steel, corrosion-resistant alloys, reinforced screen baskets, and wear-protected discharge parts.
The pusher centrifuge supports continuous slurry feeding, cake formation, washing, dewatering, and discharge.
The moving cake layer allows residual mother liquor to be reduced before drying or packaging.
Crystal washing can help reduce soluble impurities, surface contamination, and mother liquor carryover.
The pusher mechanism moves the cake forward step by step, supporting stable discharge in continuous production lines.
Mother liquor and wash filtrate can be collected according to process requirements.
The equipment is suitable for chemical crystals, inorganic salts, fertilizer crystals, salt chemicals, and other filterable crystalline products.
For correct model selection, please provide:
Crystal washing removes residual mother liquor, soluble impurities, or process liquid from the crystal cake before drying or further processing.
Yes. The filtrate collection structure can be designed to separate mother liquor and wash filtrate when the process requires recovery or reuse.
It depends on the particle size distribution. Very fine crystals may reduce cake permeability, increase solids loss, or block the screen.
Crystal size, cake thickness, wash liquid distribution, residence time, screen design, and mother liquor viscosity all affect washing efficiency.
Yes. By removing free liquid and reducing liquid carryover, the centrifuge can help provide a more stable wet cake for downstream drying.
If you have local customer channels or project resources involving crystal washing, mother liquor removal, salt crystal dewatering, fertilizer crystal washing, chemical crystal purification, or crystallization line separation projects, Peony welcomes cooperation.
Peony can support local agents, distributors, and project partners with material evaluation, screen basket selection, washing zone design, filtrate collection configuration, corrosion-resistant material recommendation, process proposal, manufacturing, installation guidance, commissioning support, spare parts, and after-sales service.
Please send us your target market, customer type, material name, process background, washing requirement, and cooperation proposal. Our team will evaluate the opportunity and provide technical and commercial support for suitable crystal washing and mother liquor removal projects.