Aplicación
Post-Consumer r-HDPE Bottle & Drum Recycling and Pelletizing Line
Post-consumer recycled H…
Solution
Integrated post-pelletizing dewatering, vertical spiral cooling, and multi-deck dedusting classification system to eliminate surface moisture, hot clumping, and off-spec fines.
This solution provides an integrated post-pelletizing dewatering, active continuous cooling, and precision classification system engineered specifically for strand pelletizing, water-ring pelletizing, and underwater pelletizing lines. Installed directly downstream of the extruder pelletizer cutter, it rapidly captures water-slurry pellet streams, removes over 99.8% of surface moisture through high-g centrifugal acceleration, gently elevates and cools pellets to safe packaging temperatures (≤ 40°C) via a vibrating spiral tower, and classifies the stream through a double-deck linear vibrating screen to completely separate oversize agglomerates and micro-fines.
In modern high-capacity compounding and recycling operations, high extruder throughput often overwhelms traditional horizontal cooling troughs or passive fluid beds, resulting in hot, moist pellets entering packaging silos. When packed hot (> 50°C), residual latent heat causes thermal sticking, clump formation inside 25 kg bags or bulk containers, and condensation-induced mold or hydrolysis during maritime export. Furthermore, uncut pellet stringers and knife dust contaminate the product stream. This engineered system delivers bone-dry, cool, and perfectly calibrated pellets ready for immediate automated bagging or bulk container loading.
The problem
Removes > 99.8% surface moisture and cools pellets to ≤ 40°C while eliminating agglomerates and knife dust prior to packaging.
Compounding and recycling lines rely on basic water troughs and rudimentary gravity mesh chutes or undersized standalone spin dryers. Hot, wet pellets exit the dryer at 65°C–80°C with 0.3%–1.0% residual surface moisture and are blown directly into packaging silos via pneumatic blowers.
Inside sealed packaging bags or Gaylord boxes, moisture cannot escape, resulting in clumped, caked pellets, hydrolysis degradation (especially in PET/PA), and frequent nozzle blockages on customer injection molding machines. Furthermore, un-scalped pellet stringers, tails, and knife cut fines lead to customer rejections.
Water-ring and underwater pelletizing systems rely on turbulent water flumes to instantly solidify hot polymer melts extruded through die holes. While water rapidly freezes the pellet outer shell, substantial latent heat remains trapped within the pellet core. If water removal is sluggish, residual surface water remains on the pellet.
Conversely, if pellets are dried centrifugally without active post-cooling, internal heat migrates to the surface, causing pellets to soften and fuse into large agglomerated clumps in the storage bin. Simultaneously, cutter blade wear produces micro-fines and stringers that create nozzle clogs during injection molding.
A continuous stream of cool (≤ 40°C), bone-dry (surface moisture ≤ 0.05%), and precisely sized pellets free from oversize agglomerates, long stringers, and knife dust, feeding directly into automatic bagging or bulk silo storage.
Process
The equipment named here is maintained on the step it belongs to, so the list and the quotation cannot disagree.
Post-Pellet Treatment
High-g centrifugal separation of transport water from pellet slurry, casting water outward through a cylindrical screen while driving dry pellets upward.
Rotor paddles rotating at 900–1200 RPM accelerate the pellet slurry. Centrifugal force drives 99.8% of surface water through the 1.5–2.0 mm screen holes into the lower sump, discharging dried pellets from the top outlet.
Equipos Vertical Centrifugal Dryer Underwater Pelletizing Dehydrator
Cooling
Vertical conveyance while continuously tumbling and actively chilling ascending pellets with high-velocity filtered air knives.
Dual synchronized vibration motors induce non-shearing micro-hops along a continuous upward spiral flight path (60–120 s retention time). Low-noise centrifugal blowers force ambient or chilled air through the fluidizing pellet bed, dropping core temperature from 75°C to ≤ 40°C.
Equipos Vibrating Spiral Elevator
Post-Pellet Treatment
Multi-deck linear vibration classification to scalp off oversize agglomerates and separate fine knife dust.
Linear dual-motor exciter drives pellets along a double-deck screen. Top deck rejects long stringers and agglomerates (> 4.5 mm); bottom deck discards fine shavings and dust (< 1.5 mm); qualified pellets discharge from center outlet.
Equipos Linear Vibrating Screen
Pelletizing
Continuously captures separated cooling water, removes stray fines via wedge-wire filter, and pumps water back to pelletizer cutting chamber.
Stainless steel balance tank with inline basket filter and booster pump maintains closed-loop water circulation, minimizing plant water consumption and thermal energy loss.
Material
Continuous pellet-water slurry discharged directly from strand pelletizing troughs, water-ring pelletizers, or underwater cutting chambers. Water flow rate up to 40 m³/h; pellet slurry temperature typically 45°C to 75°C. Polymer pellets: PP, HDPE, LDPE, PET, ABS, HIPS, PC, PA, filled compounds.
Bone-dry, dust-free, and uniformly cooled thermoplastic pellets. Residual surface moisture ≤ 0.05% (500 ppm), pellet discharge temperature ≤ 40°C, zero oversized agglomerates/twins, and fines (< 1.5 mm) content ≤ 0.05% by mass. Ready for immediate automated bagging or bulk container loading.
300–2500 kg/h
Based on continuous inline operation matched to a single or twin screw extruder pelletizing line with throughput ratings from 300 kg/h up to 2,500 kg/h, handling pellet bulk densities of 0.45–0.75 kg/L.
Fit
The boundaries are part of the solution: they keep a machine from being quoted into a case it cannot serve.
Essential for high-output compounding lines (500–2,500 kg/h) operating water-ring pelletizers or underwater pelletizers where traditional horizontal vibration tables lack sufficient retention time to cool pellets.
Crucial for polymers intended for maritime container export, where hot-caked pellets or residual moisture trigger catastrophic condensation, clump solidification, or hydrolytic degradation inside bulk liners.
Not suitable for un-pelletized plastic scrap, un-granulated film bales, or dense plastic purging blocks. Size reduction equipment (shredders/crushers) must precede this process.
Not suitable for high-melt-strength polymers processed via dry-face strand lines where no water slurry is utilized (e.g., hot air-blown strand lines).
Calculations assume standard rigid polyolefin or engineering thermoplastic pellets (PP, HDPE, ABS, PET, PC) with initial pellet slurry water-to-granule ratios between 10:1 and 25:1. Pellets must have attained sufficient core solidification prior to centrifugal dryer entry to prevent blade distortion.
For low-melting or sticky thermoplastic elastomers (TPU, TPE, EVA > 20% VA), a water-cooled hollow flight vibrating spiral elevator and anti-stick fluoropolymer screen coatings are required.
Site and connections
Total connected electrical power: 15 kW to 37 kW depending on line output capacity.
Vibration isolation rubber dampers and heavy helical springs isolate > 95% of dynamic vibratory force from building floor.
Targets
The numbers are targets agreed per project, not a general promise.
Tested continuously over a 4-hour full-load production run on the customer’s compounding line at the agreed nominal output rate. Surface moisture of discharged pellets sampled directly at the screen discharge chute is verified via halogen moisture analyzer (105°C / 10 min) to be ≤ 0.05% (500 ppm).
Pellet surface temperature measured via infrared pyrometer must register ≤ 40°C under ambient plant conditions (≤ 28°C ambient). Sieve analysis of the finished product bin must confirm 0.00% oversized stringers (> 5 mm) and fines content (< 1.5 mm) below 0.05% by mass.
Scope of supply
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Details
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