| HS Code | 908874 |
| Productname | Beijing Evergrow Resources UHMWPE UHF-R3200 |
| Material | Ultra-high molecular weight polyethylene (UHMWPE) |
| Model | UHF-R3200 |
| Form | Filament fiber/yarn |
| Lineardensity | 3200 denier |
| Tenacity | 35 cN/dtex |
| Tensilemodulus | 1200 cN/dtex |
| Elongationatbreak | 3.5% |
| Density | 0.97 g/cm³ |
| Meltingpoint | 150 °C |
| Color | White |
| Moistureregain | 0% |
| Chemicalresistance | Good against acids, alkalis, and organic solvents |
| Uvresistance | Poor |
| Abrasionresistance | High |
| Electricalconductivity | Low/insulative |
As an accredited Beijing Evergrow Resources UHMWPE UHF-R3200 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 25 kg woven bags, palletized and stretch-wrapped, labeled Beijing Evergrow Resources UHMWPE UHF-R3200 for safe transport. |
| Container Loading (20′ FCL) | Beijing Evergrow Resources UHMWPE UHF-R3200 loaded in a 20′ FCL container, bags securely stowed and moisture-protected for ocean freight. |
| Shipping | UHMWPE UHF-R3200 from Beijing Evergrow Resources is a non-hazardous polyethylene polymer, not regulated for transport (no UN number). It ships in 25 kg bags or 500–1000 kg jumbo bags, palletized and shrink-wrapped. Keep packaging sealed; store cool, dry, well-ventilated, away from sunlight, moisture, and ignition sources. Handle with standard industrial care. |
| Storage | Store Beijing Evergrow Resources UHMWPE UHF-R3200 in a cool, dry, well-ventilated warehouse, preferably in original sealed packaging on pallets. Protect from direct sunlight, moisture, heat, and ignition sources. Keep away from strong oxidizing agents. Maintain clean, dust-free conditions. No special ventilation is required under normal storage; material is stable when properly stored. Avoid prolonged UV exposure. Use first-in, first-out stock rotation. |
| Shelf Life | Shelf life approximately 24 months when stored unopened in a cool, dry, ventilated area, away from direct sunlight and moisture. |
In wet-process lithium-ion battery separator manufacturing, Beijing Evergrow Resources UHMWPE UHF-R3200 is introduced as the high-viscosity polyolefin component in a paraffin-oil plasticized system. The exact lot-specific viscosity number, bulk density, and particle-size distribution must be confirmed against the certificate of analysis for UHF-R3200 before compounding. The polymer concentration is typically held between 10 wt% and 30 wt%, with the lower half of that window preferred when the lot viscosity number exceeds 2,000 mL/g under ISO 1628-3. Pre-drying of the powder is required when ambient relative humidity exceeds 60%; drying at 80–100°C for 2–4 h in a dehumidified hopper reduces surface moisture that otherwise produces micro-voids at the cast-film stage. The plasticized mixture is compounded in a segmented twin-screw extruder with an L/D ratio of 40:1 to 52:1, operating at die temperatures between 180°C and 230°C; excursions above 230°C accelerate thermo-oxidative chain scission and lower melt consistency, while temperatures below 180°C produce shark-skin melt fracture at the die lip. The extrudate is cast onto a chilled roller maintained at 10–40°C to promote gelation before biaxial stretching. Machine-direction stretching is performed at 110–125°C and transverse-direction stretching at 115–130°C, with draw ratios of 5× to 7× in each axis. Solvent extraction with n-hexane or dichloromethane at 25–40°C reduces residual paraffin oil to below 0.2 wt%; heat-setting at 120–135°C for 30–120 s then stabilises pore geometry. Final separator film is normally 9–20 µm thick with porosity between 35% and 50% and Gurley air resistance of 150–250 s/100 cm³ measured per JIS P8117. Tensile properties of the finished film are evaluated according to ASTM D882-18, and thickness uniformity according to ISO 4593. Compliance requirements for lithium-ion cells include abuse-tolerance screening under IEC 62660-1, plus REACH 1907/2006 and RoHS 2011/65/EU for market access. The terminal product is the polyolefin separator used in consumer and electric-vehicle lithium-ion cells.
| Parameter | Operating range | Failure signature outside range | Reference method |
|---|---|---|---|
| Polymer concentration in paraffin oil | 10–30 wt% | Below 10 wt% gives low melt strength; above 30 wt% raises die pressure beyond 250 bar and forms undispersed gel specks | ISO 1628-3 for viscosity control |
| Die temperature | 180–230°C | Below 180°C causes shark-skin melt fracture; above 230°C causes yellowing and chain scission | Melt thermocouple calibration record |
| MD/TD stretch ratio | 5×–7× each axis | Below 5× yields porosity under 35%; above 7× increases pinhole tear propagation | ASTM D882-18 |
| Heat-setting | 120–135°C for 30–120 s | Below 120°C leaves longitudinal shrinkage above 5%; above 135°C collapses pores | JIS P8117 |
Gel spinning of ultra-high-molecular-weight polyethylene fibre starts with dissolution of UHF-R3200 in decahydronaphthalene or high-purity mineral oil at polymer concentrations of 5–10 wt%, corresponding to solvent-to-polymer ratios from 9:1 to 19:1. The dissolution stage is run in a twin-screw extruder with L/D 40:1 or higher and precise temperature zoning between 120°C and 220°C depending on solvent selection; oxygen exclusion through nitrogen blanketing is mandatory because local oxidation reduces maximum draw ratio. The spin solution is metered through a multi-hole spinneret with capillary diameters of 0.5–1.0 mm, and a jet stretch of 1× to 3× is imposed before the gel filament enters a water quench bath at 5–15°C. The gel fibre is then passed through an extraction train using n-hexane or dichloromethane at 25–40°C to remove solvent, followed by multi-stage hot drawing at 120–150°C. Total draw ratios for commercial gel-spun UHMWPE fibres typically lie between 30× and 80×, producing tenacities of 30–45 cN/dtex and initial moduli of 1,000–1,500 cN/dtex when tested according to ASTM D885-16. The upper draw limit is set by a conflict between chain orientation and chain scission: excessive draw initiates surface fibrillation and broken filaments, whereas insufficient draw leaves low modulus and elevated creep. Lot-to-lot variation in UHF-R3200 solution viscosity requires adjustment of polymer concentration rather than temperature; published data for UHF-R3200-specific draw-ratio maxima is limited, so laboratory spin trials with ISO 1628-3 viscosity verification are recommended before production transfer. Fibre-grade compliance for industrial applications includes ASTM D885-16 for tensile metrics and EN 388:2016 for cut-resistant glove yarns, with REACH 1907/2006 documentation required for import. Terminal products are high-tenacity yarns for marine ropes, industrial slings, cut-protection textiles, and unidirectional ballistic prepreg input.
Sintered porous parts are produced from UHMWPE powder by filling a compression mould with a controlled particle-size distribution; for UHF-R3200, the practical d50 window is 100–300 µm, with a fill-to-final-thickness ratio between 1.5:1 and 2:1 to allow densification without eliminating interconnected porosity. The mould is heated to 180–200°C and held under 5–15 MPa for 2–20 min depending on part thickness. The processing window is critical: sustained temperature above 200°C collapses pores and produces a dense polyethylene slab, while temperatures below 175°C leave only weakly fused particles with poor flexural integrity. A ±5°C variation across the platen can produce measurable differences in center-core porosity and surface skin density. After cooling under pressure at 5–10°C/min to below 60°C, the resulting porous body has interconnected porosity typically in the 30–50% range and mean flow-pore diameters between 10 µm and 100 µm. Flexural modulus is evaluated by ASTM D790-17, density by ISO 1183-1, and pore-size distribution by mercury intrusion per ISO 15901-1. Food-contact porous components must be qualified under FDA 21 CFR 177.1520 for olefin polymers, including extraction-cell limits on total extractables. Terminal products include venting membranes, silencer discs, suction filter elements, fluidizing plates in powder-handling equipment, and low-load bearing porous supports.
Direct compression molding of medical-grade UHMWPE is not a generic powder-to-part route; UHF-R3200 is only suitable for implant applications if the lot certificate of analysis demonstrates conformance to ASTM F648-21 and ISO 5834-2, including limits on trace catalyst residues, oxidation index, and tensile properties. The unfilled powder is conditioned to a moisture level below 0.05 wt% before mould charging. The compression mould is evacuated or purged with nitrogen while the powder is heated to 190–220°C and pressed at 7–15 MPa for 20–60 min; the fill ratio is typically 2:1 to 3:1 by bulk volume to final implant volume to account for powder density. Cooling is conducted under pressure at 5–15°C/min to below 60°C to minimise warpage and residual stress. When post-consolidation crosslinking is required for wear reduction, the consolidated implant is gamma-irradiated at 50–75 kGy in an inert atmosphere and then remelted at 150°C to quench residual free radicals. Mechanical acceptance testing follows ISO 527-3 or ASTM D638-14 for tensile yield and elongation, with oxidation index measured by ISO 5834-4. Calcium stearate or amine-based processing aids are not introduced unless specifically allowed by the implant specification, because such additives can alter wear-particle morphology and oxidative stability. Published data for UHF-R3200 implantation-grade qualification is limited; resin batches not explicitly certified for medical use cannot be assumed to meet ISO 5834-2 without full characterisation. Terminal products are orthopaedic tibial inserts, acetabular cups, and other total joint replacement components.
| Segment | Principal standard or regulation | Measured property or requirement |
|---|---|---|
| Lithium-ion battery separator | IEC 62660-1, REACH 1907/2006, RoHS 2011/65/EU | Cell abuse tolerance, film thickness by ISO 4593, tensile by ASTM D882-18, Gurley by JIS P8117 |
| Gel-spun industrial fibre | ASTM D885-16, EN 388:2016 | Yarn tenacity, modulus, elongation at break, cut resistance index |
| Sintered porous food-contact | FDA 21 CFR 177.1520 | Total extractables, density by ISO 1183-1, pore size by ISO 15901-1 |
| Medical implant | ASTM F648-21, ISO 5834-2, ISO 5834-4 | Oxidation index, tensile yield, elongation, trace impurity limits |
| Ram-extruded wear parts | ASTM D4020, ISO 11542-2, ISO 60 | Molecular identity, viscosity number, bulk density |
| Ballistic panel | NIJ Standard-0101.06, ASTM D885-16 | Backface deformation, ballistic resistance, incoming yarn tensile properties |
Ram extrusion is selected for UHMWPE because the melt viscosity is too high for conventional screw extrusion. UHF-R3200 is compacted in the feed zone at 20–30°C under 10–25 MPa before entering the heated die barrel where zone temperatures are held between 190°C and 220°C. The feed zone must remain below 50°C; if the powder compacts prematurely, bridging and irregular billet density cause pressure fluctuations above ±0.5 MPa and visible surface pitting on the extruded profile. Pre-drying at 80–100°C for 2–3 h is required when relative humidity exceeds 60%. Output is determined by ram stroke and billet throughput rather than screw rpm; very slow ram speeds below 2 m/h reduce melt fracture but limit productivity, while higher-speed cycles require longer heated die zones. The extruded profile is cooled under restraint to below 60°C before cutting to length. Material compliance for industrial wear parts includes ASTM D4020 for molecular identity and average molecular weight, ISO 11542-2 for viscosity-number determination, and ISO 60 for bulk density. Terminal products are chain guide rails, conveyor wear strips, idler rollers, chute liners, and guide profiles for bottling lines; each is used where dry sliding wear and impact are more decisive than continuous service above 80°C.
The ballistic product chain requires UHF-R3200 to be converted first into high-modulus fibre by gel spinning; the powder is not pressed directly into armour. The resulting yarn is laid into 0°/90° unidirectional plies and bonded with an elastomeric matrix at 10–20 wt% resin content, commonly a styrenic block copolymer or polyurethane. Plies are stacked from 4 to 20 layers depending on threat level and panel geometry. Consolidation is performed in a heated platen press at 120–130°C under 10–20 MPa for 20–60 min, followed by cooling under pressure to below 50°C. Press temperatures above 130°C initiate relaxation and measurable tensile-strength loss in the oriented fibre when incoming yarn is re-tested under ASTM D885-16, while temperatures below 115°C yield incomplete matrix adhesion and poor delamination resistance. The consolidated panel is evaluated for ballistic resistance under NIJ Standard-0101.06 and for backface deformation according to the same document; incoming UD prepreg tensile properties are validated according to ASTM D885-16. Published data for UHF-R3200-specific fibre-to-panel conversion is limited, requiring a full small-lot press trial before production transfer. Terminal products are hard armour plates, helmet shells, and spall liners for vehicle platforms.
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Beijing Evergrow Resources supplies UHF-R3200 as an ultra-high-molecular-weight polyethylene (UHMWPE) grade for compression-moulded semifinished stock, ram-extruded profiles, and machined wear components. The grade designation is associated with a nominal viscosity-average molecular mass of 3.2×10⁶ g/mol; the polymer is an unfilled linear homopolymer and is typically handled as a free-flowing powder with an apparent density of 0.45–0.55 g/cm³ when tested according to ISO 60. Moulded stock made from UHF-R3200 exhibits a density of 0.930–0.945 g/cm³ under ISO 1183-1 and falls within the ultra-high-molecular-weight classification of ASTM D4020-18. Because the extensive chain-entanglement network suppresses melt flow, the material is not considered injection-mouldable; it is converted by powder compaction, compression moulding, or ram extrusion. Typical finished components include chain guides for conveyor systems, bottling-line wear strips, star wheels, scraper blades, guide rails, chute liners, and bearing pads in bulk solids handling and food-processing equipment. Table 1 lists representative property values derived from certificates of analysis and supplier technical documentation. These values are not design substitutes for lot-specific data because small variations in molecular mass and bulk density alter consolidation behaviour and abrasion resistance.
| Property | Test method | Unit | Representative value |
|---|---|---|---|
| Viscosity-average molecular mass | ISO 1628-3 / ASTM D4020-18 | g/mol | 3.2×10⁶ |
| Density | ISO 1183-1 | g/cm³ | 0.930–0.945 |
| Tensile yield stress | ISO 527-2 Type 1B, 50 mm/min | MPa | 20–25 |
| Tensile elongation at break | ISO 527-2 | % | 300–500 |
| Notched Izod impact strength, 23°C | ISO 180/A | kJ/m² | no break |
| Shore D hardness | ISO 868, 15 s | — | 60–70 |
| Water absorption, 23°C, 24 h | ISO 62 | % | ≤0.01 |
| Vicat softening temperature A120 | ISO 306/A120 | °C | 78–84 |
When UHF-R3200 is substituted for a standard high-density polyethylene homopolymer, the functional difference is not chemical identity but the density of load-bearing entanglement junctions. The nominal molecular mass of 3.2×10⁶ g/mol is 30–60 times greater than that of ordinary HDPE extrusion grades, which generally lie between 50,000 g/mol and 200,000 g/mol. Under dry-sand rubber-wheel abrasion in ASTM G65 Procedure A, unfilled UHMWPE of this class typically loses mass at a rate 5–10 times slower than HDPE; however, published data for this specific product configuration is limited, and design-level wear rates require lot-specific testing. Under low-speed pin-on-disc sliding against 316 stainless steel, the dynamic coefficient of friction for UHMWPE is commonly measured in the range 0.10–0.20, whereas HDPE often increases above 0.30 once the transfer film is removed or the surface temperature exceeds 60°C.
In chain guides and wear strips, the switch from HDPE to UHF-R3200 changes the dominant failure mode from abrasive loss and edge fracture to long-term creep. The notched Izod impact resistance of UHF-R3200 is generally reported as no break under ISO 180/A at 23°C, while unfilled HDPE may yield 10–25 kJ/m². Edge chipping during jam events and low-temperature cracking in cold stores are therefore reduced. The reduced stiffness, however, is a measurable limitation: tensile modulus of UHMWPE is typically 800–1000 MPa under ISO 527-2, whereas high-molecular-weight HDPE can exceed 1200 MPa. A load-bearing component with the same cross-section will deflect more; designers usually increase thickness or use a steel-backed liner instead of assuming direct shape replacement.
Friction performance is also more sensitive to break-in than HDPE. During the first 50–100 h of dry sliding, a transfer film of UHMWPE must build on the metallic counterface to stabilize the coefficient of friction. Abrasion or chemical cleaning of the metal surface destroys this film and temporarily raises friction and wear until the film reforms. This behaviour is observed on bottling-line guide rails and should be included in startup procedures rather than evaluated only from steady-state wear rates.
For ram extrusion of UHF-R3200 on production machines with die diameters from 50 mm to 120 mm, the powder is compacted in the cold zone and then sintered through the die at 200–240°C. Compaction pressure is normally held between 25 MPa and 40 MPa. A pressure below 20 MPa commonly produces incomplete powder consolidation and visible axial porosity in the extruded rod. Because heat transfer through the compacted powder controls line speed, a 50 mm diameter profile may require 15–40 min residence time in the heated die, depending on die length and wall temperature uniformity. Die temperature excursions above 250°C initiate thermo-oxidative chain scission; the surface becomes yellow to brown, and the notched impact strength falls before the dimensional change becomes apparent.
Compression moulding of thick sections follows a similar thermal path. Pre-compacted powder is heated to 200–220°C under platen pressure of 10–20 MPa, held for 30–60 min per 25 mm of finished thickness, and then cooled under pressure at 2–5°C/min. Faster cooling from 220°C to 80°C reduces crystallinity and hardness, but increases residual stress and post-machining warpage. The cooling stage must therefore be treated as part of the dimensional-control strategy for close-tolerance parts.
Powder feed consistency is the main batch-to-batch variable on ram extruders. Apparent density outside the 0.45–0.55 g/cm³ range shifts the compaction ratio and alters back-pressure. UHMWPE powder absorbs less than 0.03% moisture by mass at 50% relative humidity, so pre-drying is generally not required. However, condensation on cold powder stored in humid warehouses above 80% relative humidity can introduce enough surface moisture to cause steam porosity during sintering. A fluidized-bed dryer at 80°C for 30 min is used before extrusion when storage conditions are uncontrolled.
Screw plastication is not a viable conversion route for UHF-R3200. On a co-rotating twin-screw extruder with an L/D ratio of 40:1, the powder compacts into an unmelted plug and the drive torque can exceed the machine limit before the first kneading block. The same limitation applies to injection moulding: without a fluid melt phase, the material cannot fill a closed mould at pressures available on conventional injection presses. This is why the product is supplied as powder, ram-extruded stock, or machined shapes rather than as pelletized feedstock for high-speed screw plastication.
Compliance under FDA 21 CFR 177.1520 and EU Regulation 10/2011 is documented for unfilled polyethylene homopolymers used in food-contact parts, provided the finished component meets overall migration limits and end-use testing. Supplier statements for UHF-R3200 may reference these regulations when the fabricating plant controls source monomers and additives under the applicable positive list. The grade is outside current RoHS restrictions under 2011/65/EU because it does not require brominated flame retardants or heavy-metal stabilizers, and it can be reported under REACH 1907/2006 as an exempt polymer if the monomer content complies with Article 2(9). For chemical resistance, UHF-R3200 withstands dilute acids, alkalis, and aqueous salt solutions at ambient temperature. Concentrated oxidizing acids such as 98% sulfuric acid and 65% nitric acid embrittle the surface, and aliphatic or aromatic hydrocarbons swell the polymer at elevated temperature. Seal and coupling designs must allow for this dimensional change.
In wet or particulate-laden bearing seats, UHF-R3200 replaces polyamide 6 when moisture-induced dimensional growth and acid effluent contact are the controlling failure modes. Polyamide 6 absorbs 2.5–3.0% water at saturation under ISO 62, causing swelling and loss of bolt preload in bearing housings; UHF-R3200 absorbs ≤0.01% after 24 h and remains dimensionally stable in humid bottling lines and washdown areas. Against filled PTFE, UHF-R3200 has higher dry-sand abrasion resistance and lower creep sensitivity under ambient loads, but unfilled or filled PTFE retains a lower initial coefficient of friction and a far higher continuous service temperature of 260°C. The practical limit for unlubricated UHMWPE sliding against steel is often cited as a PV range of 0.2–0.3 MPa·m/s; above this threshold, frictional heating at the wear surface accelerates creep and eventual melting. In dirty environments containing sand, the softer UHMWPE surface can embed particles rather than scoring the metal shaft, which may reduce shaft damage but increases the composite wear rate if the particles are not flushed from the contact zone.
The substitution decision between UHF-R3200 and polyamide 6 depends on temperature and load. At 23°C and continuous compressive stress below 5 MPa, UHMWPE is usually selected for impact resistance and low water uptake. Above 60°C, glass-fibre-reinforced polyamide 6 may retain higher stiffness, but unfilled polyamide 6 loses toughness when dry and may hydrolyse in hot water above 70°C over long service. UHMWPE avoids hydrolysis but begins to creep rapidly near its Vicat softening point of 78–84°C; therefore both materials require support at elevated temperature.
Continuous service above 85°C is not recommended for load-bearing UHF-R3200 components because the Vicat softening point is 78–84°C under ISO 306/A120 and creep rate rises steeply across a narrow interval. In hoppers and chutes handling hot bulk solids above 80°C, the liner should be continuously supported by a metal backing to prevent sag and extrusion from fastener holes. Strong oxidizing solutions, chlorinated solvents, and prolonged ozone exposure embrittle the surface through free-radical chain degradation. If the application requires continuous exposure to >50% nitric acid or 90% sulfuric acid at temperatures above 40°C, UHF-R3200 is not appropriate. The thermal conductivity of UHMWPE is approximately 0.40–0.50 W/m·K, so frictional heating remains localized at the contact face. Dry sliding designs must therefore limit contact pressure and speed before increasing section thickness, because additional thickness does not remove heat from the interface.