| Brand Name: | Peony |
| Model Number: | PP |
| MOQ: | 1 |
| Packaging Details: | Standard export packings |
| Payment Terms: | T/T,L/C |
A fertilizer crystal dewatering pusher centrifuge is designed for continuous solid-liquid separation of fertilizer-grade crystalline materials after crystallization, reaction, or concentration processes. It is commonly used for ammonium sulfate, potassium chloride, nitrate crystals, ammonium chloride, potassium sulfate, and other fertilizer-related crystalline products.
In fertilizer production, wet crystals usually contain mother liquor, soluble impurities, process liquid, and fine particles. If the wet cake contains too much free liquid, the downstream dryer may face higher energy consumption, unstable feeding, product caking, and inconsistent final moisture.
A pusher centrifuge removes mother liquor through centrifugal filtration. The screen basket retains the fertilizer crystals, while the liquid phase passes through the screen and is collected as filtrate. The pusher mechanism moves the crystal cake forward continuously and discharges it from the basket end.
Compared with batch filtration or manual discharge equipment, a pusher centrifuge is more suitable for fertilizer plants that require large capacity, continuous operation, stable cake discharge, lower dryer load, and reduced manual handling.
| Fertilizer Material | Process Source | Dewatering Purpose |
|---|---|---|
| Ammonium sulfate crystals | Neutralization, crystallization, or recovery process | Remove mother liquor before drying and packaging |
| Potassium chloride crystals | Potash processing, brine concentration, or fertilizer production | Dewater fertilizer-grade KCl crystals before drying |
| Potassium sulfate crystals | SOP fertilizer crystallization process | Reduce free liquid and improve dryer feed stability |
| Nitrate fertilizer crystals | Nitrate crystallization or fertilizer intermediate process | Continuous wet crystal dewatering before drying |
| Ammonium chloride crystals | Fertilizer intermediate or chemical fertilizer process | Separate crystals from mother liquor and reduce moisture |
| Compound fertilizer intermediate crystals | Reaction or crystallization slurry | Reduce liquid carryover before downstream processing |
| Fertilizer-grade salt crystals | Fertilizer raw material or nutrient salt production | Provide stable wet cake for dryer, cooler, and screening |
A pusher centrifuge is usually installed after crystallization or slurry thickening and before the dryer.
Typical process route:
Reaction / concentration → Crystallization → Pusher centrifuge → Wet fertilizer crystal cake → Dryer → Cooler → Screening → Packaging
For fertilizer products requiring washing:
Crystallizer slurry → Pusher centrifuge → Cake washing zone → Mother liquor removal → Wet cake discharge → Dryer
In a complete fertilizer production line, the centrifuge works together with crystallizers, reactors, evaporators, dryers, coolers, screening machines, and packaging systems. Its performance is closely related to crystal size, slurry concentration, mother liquor composition, washing requirement, and dryer capacity.
The fertilizer crystal slurry enters the rotating screen basket through the feed pipe. Under centrifugal force, mother liquor passes through the screen openings and is discharged as filtrate. Fertilizer crystals remain 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 fertilizer crystal cake is discharged continuously from the basket end and sent to drying, cooling, screening, packaging, or further processing.
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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 |
Fertilizer crystals must be able to form a stable filter cake on the screen basket.
Coarse and uniform crystals are usually easier to dewater. Fine crystals may pass through the screen, block the screen openings, reduce filtrate clarity, or increase product loss.
For ammonium sulfate, potassium chloride, nitrate, or ammonium chloride crystals, the actual crystal size distribution should be checked before equipment selection.
Feed solids content affects throughput, cake thickness, pushing resistance, and screen filtration performance.
If the feed slurry is too dilute, cake formation may be unstable. If the solids content is too high, the pusher load and discharge resistance may increase. The suitable feed concentration depends on the material, crystal size, liquid viscosity, and production capacity.
Fertilizer mother liquor may contain salts, ammonium compounds, chloride, nitrate, sulfate, or other dissolved components. These substances affect corrosion resistance, screen selection, filtrate collection, and maintenance frequency.
Material selection should be based on pH value, chloride content, temperature, salt concentration, and corrosion behavior.
Lower wet cake moisture can reduce downstream dryer load and improve drying stability. However, final moisture depends on crystal size, cake permeability, screen opening, centrifugal force, residence time, and washing condition.
For fertilizer production, the practical goal is usually to provide a stable wet cake suitable for continuous drying, rather than pursuing unrealistic moisture reduction only by mechanical dewatering.
Some fertilizer crystals require washing to reduce residual mother liquor, soluble impurities, or surface contamination. In this case, the washing zone, wash liquid distribution, cake thickness, and residence time should be considered.
A pusher centrifuge is suitable for continuous washing because the cake moves through the screen basket in a controlled and stable manner.
Fertilizer crystals can be abrasive, and mother liquor can be corrosive. The screen basket, pusher plate, discharge area, and wetted parts should be selected according to actual working conditions.
Common configuration options include:
The pusher centrifuge supports continuous feeding, filtration, washing, dewatering, and discharge for fertilizer production lines.
By removing free mother liquor before drying, the centrifuge helps reduce thermal load and supports more stable dryer operation.
The pusher mechanism moves the crystal cake forward continuously, helping maintain stable discharge during high-capacity production.
The equipment is suitable for continuous fertilizer production where high throughput, long operating hours, and low manual handling are required.
A washing zone can be configured to reduce residual mother liquor or soluble impurities on fertilizer crystals.
Screen basket, pusher components, process housing, and wetted parts can be selected according to fertilizer crystal abrasiveness and mother liquor corrosion.
For correct model selection, please provide:
It can be used for filterable fertilizer crystals such as ammonium sulfate, potassium chloride, nitrate crystals, potassium sulfate, ammonium chloride, and other fertilizer-grade crystalline products.
Yes. A pusher centrifuge is commonly used for ammonium sulfate crystal dewatering when the crystals have suitable particle size and filterability.
Yes. A washing zone can be configured to reduce residual mother liquor or soluble impurities on the fertilizer crystal cake.
Final cake moisture depends on crystal size, feed solids content, mother liquor viscosity, screen opening, centrifugal force, cake thickness, washing condition, and residence time.
By removing free liquid before drying, the centrifuge can reduce dryer load, improve feeding stability, and support more consistent final product moisture.
If you have local customer channels or project resources involving ammonium sulfate, potassium chloride, nitrate crystals, potassium sulfate, ammonium chloride, fertilizer-grade salt crystals, or continuous fertilizer crystal dewatering lines, Peony welcomes cooperation.
Peony can support local agents, distributors, and project partners with technical model selection, material evaluation, screen basket selection, washing design, corrosion-resistant configuration, process proposal, manufacturing, installation guidance, commissioning support, spare parts, and after-sales service.
Please send us your target market, customer type, material name, project background, and cooperation proposal. Our team will evaluate the opportunity and provide technical and commercial support for suitable fertilizer crystal dewatering projects.