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Beijing Evergrow Resources UHMWPE ER-24

    • Product Name: Beijing Evergrow Resources UHMWPE ER-24
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 641615
    Material Type Ultra-high molecular weight polyethylene (UHMWPE)
    Grade ER-24
    Appearance White powder
    Molecular Weight Approximately 2.4 million g/mol
    Density 0.93–0.94 g/cm³
    Bulk Density 0.40–0.45 g/cm³
    Particle Size Approximately 150–250 µm
    Melting Point 130–136 °C
    Crystallinity 40–50%
    Tensile Strength 20–25 MPa
    Elongation At Break 350–450%
    Notched Impact Strength ≥100 kJ/m²
    Water Absorption <0.01%
    Coefficient Of Friction 0.10–0.20
    Abrasion Resistance High
    Thermal Conductivity 0.42 W/(m·K)
    Dielectric Constant 2.3 at 1 MHz
    Volume Resistivity >10^15 Ω·cm
    Shore D Hardness 60–65
    Vicat Softening Point 80–90 °C

    As an accredited Beijing Evergrow Resources UHMWPE ER-24 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Beijing Evergrow Resources UHMWPE ER-24 is packaged in 25 kg net-weight bags, typically supplied in 1,000 kg pallet quantities.
    Container Loading (20′ FCL) Beijing Evergrow Resources UHMWPE ER-24 loaded in 20′ FCL: 25 kg bags, palletized, shrink-wrapped, stacked, and secured for ocean transport.
    Shipping Beijing Evergrow Resources UHMWPE ER-24 is typically shipped as a non-hazardous, free-flowing polyethylene powder in moisture-resistant bags or drums on pallets. Keep dry, away from UV, heat, and contamination. Transport in clean, covered vehicles; comply with local regulations and supplier SDS.
    Storage Store Beijing Evergrow Resources UHMWPE ER-24 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, sparks, and flames. Keep containers tightly closed to prevent moisture and dust contamination. Avoid strong oxidizing agents. Use grounding to control static. Keep in original packaging, avoid prolonged UV exposure, and follow the supplier’s SDS and local regulations.
    Shelf Life Typical shelf life is two years when stored cool, dry, in sealed packaging, protected from direct sunlight and moisture.
    Application of Beijing Evergrow Resources UHMWPE ER-24

    Gel-spinning ER-24 into High-Molecular-Weight Fibre at the 6–8 wt% Plasticiser Window

    For high-tenacity fibre lines, Beijing Evergrow Resources ER-24 powder is first pre-dried at 80–100 °C for 2 h under vacuum because moisture above 100 ppm in the slurry feed generates bubble-related capillary breakage during spinneret discharge. The powder is then suspended in a high-boiling paraffin oil at 6–8 wt% total solids; the oil phase typically has a kinematic viscosity of 40–70 mm²/s at 40 °C. A hindered-phenol antioxidant, added at 0.1–0.3 wt% of ER-24 mass, is pre-dissolved in the oil to suppress chain scission during twin-screw dissolution under vacuum of −0.08 MPa at 135–160 °C for 45–90 min. Because ER-24 is characterised by a viscosity-average molecular weight near 2.4 × 10⁶ g/mol on the supplier certificate of analysis, complete solvation requires an intermeshing co-rotating twin-screw extruder with an L/D ratio of 48, screw speed limited to 100–200 min⁻¹, and head pressure held at 3–8 MPa; pressure excursions beyond 8 MPa indicate gel flecks or incomplete solvation that will tear the spinneret capillary. The solution is filtered through a 20 µm sintered metal pack and metered by a 10 cm³/rev gear pump into a spinneret capillary of 0.8 mm diameter and L/D of 10. The air gap is controlled at 2–5 mm, and the gel filament is fixed in a water bath at 10–20 °C. Residual paraffin oil is removed in a countercurrent n-hexane or dichloromethane extraction train at 30–45 °C. Two-stage hot stretching at 120–145 °C operates at a total draw ratio of 20:1–40:1. Fibre tensile properties are measured per ASTM D885/D885M-10A; commercially reported gel-spun UHMWPE fibre reaches tenacity of 2.8–3.6 GPa and modulus of 90–120 GPa, with ER-24-specific values dependent on draw ratio, extraction efficiency, and molecular weight distribution. Terminal products include cut-resistant gloves, offshore mooring ropes, industrial slings, fishing nets, and ballistic prepreg laminates. EU textile intermediates require REACH compliance under Regulation (EC) No 1907/2006; assembled rope and sling products may be certified to ISO 2307:2019 for breaking strength and elongation.

    What Limits Gurley Values When ER-24 Is Used in Wet-Process Separator Film?

    Because a 100% ER-24 melt remains too viscoelastic for stable cast-film extrusion at commercial separator line speeds, lithium-ion battery separator production blends ER-24 with high-density polyethylene. The dry-blend formulation commonly consists of 20–30 wt% ER-24, 5–10 wt% HDPE, 65–75 wt% paraffin oil plasticiser, and 0.05–0.1 wt% antioxidant. The mixture is plastified in a twin-screw extruder at 180–220 °C and cast through a 1.0–2.0 mm slot die onto a chilled roll at 30–60 °C. The gel film is then stretched in a simultaneous biaxial tenter at 90–120 °C with draw ratios of 5×–7× in machine direction and 5×–7× in transverse direction. Paraffin oil is extracted in a methylene chloride or n-hexane countercurrent bath at 25–40 °C, followed by heat setting at 120–135 °C under controlled tension. Finished separator targets include thickness of 7–12 µm, porosity of 40–55 % measured by mercury intrusion per ISO 15901-1:2016, and Gurley permeability of 150–400 s/100 cm³ using a densometer method aligned to ISO 5636-5. Pinhole formation is the dominant failure mode; if the ER-24/HDPE phase separates or undissolved gel particles remain in the cast film, pores above 1 µm appear and are detected by bubble point testing per ASTM F316-03. Residual plasticiser content must remain below 500 mg/m² before cell assembly because carbonate electrolytes dissolve low-molecular-weight oil fractions and shift the separator’s shutdown response. Shutdown temperature is established by differential scanning calorimetry at 130–140 °C, while the ER-24 fraction preserves membrane integrity above 150 °C. Terminal products are separators for lithium-ion secondary cells used in electric vehicle and energy storage systems. Finished cell qualification typically references IEC 62660-2:2021 or UL 1642, and separator scrap is managed under Directive 2006/66/EC and national battery waste equivalents.

    Size-classified ER-24 powder in the 100–250 µm sieve cut is used directly in sintered porous filter manufacture without binder, plasticiser, or solvent. The powder is charged into a matched-metal mould, levelled to uniform fill depth, and compacted at 3–10 MPa to produce a green preform with sufficient mechanical integrity for demoulding. Sintering is performed in a forced-air oven with a heating rate of 1–3 °C/min to 180–210 °C, held for 30–90 min, and cooled at 0.5–1 °C/min to room temperature. The resultant porous body exhibits average pore diameter of 15–60 µm and open porosity of 35–45 % measured by mercury intrusion per ISO 15901-1:2016. Fine particles below 75 µm reduce pore throat diameter, while compaction above 10 MPa densifies the preform and blocks permeability. Overheating above 210 °C or heating faster than 3 °C/min causes non-uniform densification and fine-wall cracking that is difficult to detect without bubble point testing per ASTM F316-03. Terminal products include aeration diffuser discs, vacuum filter plates, silencer elements, and porous filter tubes. For aqueous food-contact filtration service, the sintered article must meet extractables and migration limits under 21 CFR 177.1520 and Regulation (EU) No 10/2011.

    When ER-24 Powder Is Ram-Extruded Through a Cylindrical Compaction Die

    Ram extrusion of ER-24 is a solid-state compaction process distinct from screw extrusion. The powder is pre-dried at 80 °C for 2–3 h if ambient relative humidity exceeds 60 % and is fed into a hydraulically driven ram extruder with a barrel L/D of 20:1. The barrel is set in a reverse-temperature profile from 180 °C at the feed zone to 220 °C at the die entry, while the die block is controlled at 190–210 °C with maximum block-to-block variation of ±5 °C. Ram pressure is maintained at 15–40 MPa and ram speed is limited to 0.3–1.5 m/min to avoid centreline voids caused by incomplete heat penetration. Production-scale machine operators reject output when die pressure fluctuates by more than 10 % within a single stroke, because pressure variation indicates inconsistent bulk density or residual moisture. Extruded profiles are cooled under tension in a 10–20 m water bath and cut into chain guides, conveyor wear strips, star wheels, and chute liners. Dimensional classification follows ISO 11542-1 and ASTM D4020. Tensile properties are determined on machined specimens per ASTM D638-14; typical values include tensile yield strength of 21–28 MPa and elongation at break above 300 %. Coefficients of friction against polished steel are evaluated by ASTM D1894-14 and generally remain below 0.25. These profiles are specified in packaging and beverage conveyor applications where the component must resist continuous chain movement and where incidental food contact requires clearance under 21 CFR 177.1520.

    Before ER-24 is considered for orthopaedic implant semi-finished stock, the supplier documentation must demonstrate conformance to ASTM F648-21 and ISO 5834-2 for both powder and fabricated form. Compression moulding is preferred over ram extrusion because the moulded artefact must be free of fusion defects, voids, and high-shear thermal history. The powder is pressed in a vacuum-capable compression press at 200–220 °C and 5–15 MPa for 30–60 min, then cooled at 0.5 °C/min or slower to reduce residual stress before machining into tibial inserts, acetabular liners, and patellar components. The implant-grade fabricated form must show density of 0.930–0.945 g/cm³ per ISO 1183-1, tensile yield strength of 21–28 MPa per ASTM D638-14, elongation at break above 300 %, and Izod impact resistance reported as no-break per ASTM D256-10. Sterilisation is typically performed by gamma irradiation at 25–40 kGy in inert gas, and the oxidation index must remain below 1.0 when verified by ASTM F2102-17 after accelerated ageing. ER-24 should not be combined with calcium stearate, processing waxes, or unknown reclaim because such additives violate implant-grade resin cleanliness and alter wear performance. Published long-term wear data for this specific Beijing Evergrow Resources grade is limited; implant engineers therefore require lot-specific thermal history, oxidation index, and mechanical test results before design freeze.

    Compression-Moulded ER-24 Liners in Slurry Handling and Chute Applications

    In mining and mineral processing, ER-24 sheet is produced by hot-compression moulding rather than screw extrusion because the grade does not form a stable melt at conventional melt index test conditions. The powder is filled into a stainless-steel picture-frame mould at a controlled bulk density of 0.42–0.50 g/cm³, compacted cold at 5–10 MPa to expel entrapped air, and then heated to 200–220 °C under 10–15 MPa. Soak time is 20–40 min for 10–20 mm sheet, followed by cooling under pressure at 0.5–1.0 °C/min. The resulting liner is machined into slurry pipe spools, hopper liners, pump volute liners, and drag-chain paddles. Sliding friction against moving bulk solids is evaluated by ASTM D1894-14. Sections above 30 mm require extended heating time, and the heating rate through the preform must not exceed 2 °C/min; otherwise the centreline remains below the crystalline transition temperature and delamination occurs during machining. ER-24 liners are frequently specified for dilute and moderate slurry services where pH is between 2 and 12 and where pipe temperatures do not exceed 80 °C; concentrated oxidising acids and continuous chlorine dosing degrade the exposed surface and reduce wear life. Published abrasion data for ER-24 in specific slurry chemistries is limited, so field trials against the incumbent steel or rubber liner are required. EU sales of mining liners require REACH compliance under Regulation (EC) No 1907/2006.

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    Certification & Compliance
    More Introduction

    Beijing Evergrow Resources supplies UHMWPE ER-24 as an ultra-high-molecular-weight polyethylene resin intended for compression molding, ram extrusion, and subsequent machining into wear components. The ER-24 grade belongs to the PE-UHMW classification under ISO 11542-1; its solution viscosity number exceeds 2000 cm³/g when determined by ISO 1628-3 in decalin at 135 °C. Unlike HDPE, the material does not produce a conventional melt flow rate under ISO 1133-1:2022, because the molar mass is sufficiently high to prevent meaningful flow in a standard melt indexer. Supplier documentation for ER-24 should be used for particle size distribution, bulk density, and gel count. Published open-literature data for this specific configuration is limited; the technical envelope below therefore relies on the ISO 11542-1 class definition and standard conversion practices for PE-UHMW rather than a certified lot datasheet.

    For unfilled PE-UHMW stock shapes, density is normally 0.930–0.945 g/cm³ when tested to ISO 1183-1, tensile yield stress is 20–25 MPa under ISO 527-2, and elongation at break is above 300%. Notched Charpy impact strength at 23 °C exceeds 100 kJ/m² under ISO 179-1/1eA and typically remains high at subambient temperatures. Shore D hardness is in the 60–72 range per ISO 868. Vicat softening temperature for PE-UHMW is near 80 °C under ASTM D1525, but this is a short-term thermal test; load-bearing service is limited to lower temperatures. These values describe the unfilled PE-UHMW material class and should be verified against the ER-24 certificate of analysis before die design, regulatory submission, or wear-rate testing.

    How Does ER-24 Differ From High-Density Polyethylene and PTFE in Sliding Wear?

    UHMWPE ER-24 differs from HDPE primarily in molar mass and entanglement density. HDPE grades typically show solution viscosity numbers below 500 cm³/g, whereas PE-UHMW exceeds 2000 cm³/g; this shifts conversion from injection molding and film extrusion toward sintering, ram extrusion, and compression molding. Under dry sliding against ground 316L stainless steel, PE-UHMW exhibits a dynamic coefficient of friction of approximately 0.10–0.22 by ASTM D1894 or pin-on-disk testing per ASTM G99. HDPE is slightly higher at 0.15–0.25, virgin PTFE is lower at 0.04–0.10, and dry PA66 is higher at 0.20–0.30. In block-on-ring wear testing per ASTM G77, unfilled PE-UHMW class materials typically show specific wear rates below 1 × 10⁻⁶ mm³/N·m at moderate pressure-velocity products, while unfilled HDPE can wear at rates an order of magnitude higher. PTFE remains lower in friction but suffers higher creep and can be displaced under concentrated loads; PE-UHMW is therefore selected when abrasive contamination, impact loading, and sliding motion occur together.

    Comparative property envelopes for unfilled PE-UHMW, HDPE/HMW-PE, virgin PTFE, and dry PA66
    PropertyTest methodPE-UHMW (ER-24 class)HDPE/HMW-PEVirgin PTFEPA66 dry
    Solution viscosity numberISO 1628-3> 2000 cm³/g< 500 cm³/gNot applicableNot applicable
    DensityISO 1183-10.930–0.945 g/cm³0.940–0.965 g/cm³2.13–2.20 g/cm³1.13–1.15 g/cm³
    Yield stressISO 527-220–25 MPa22–30 MPa10–15 MPa60–85 MPa
    Elongation at breakISO 527-2> 300%100–600%200–400%20–80%
    Notched Charpy, 23 °CISO 179-1/1eA> 100 kJ/m²10–30 kJ/m²13–16 kJ/m²5–15 kJ/m²
    Shore D hardnessISO 86860–7262–7050–6575–85
    Dry dynamic coefficient of friction vs polished steelASTM D18940.10–0.220.15–0.250.04–0.100.20–0.30

    For conversion of ER-24 powder into sheet, production-scale compression molding presses with clamp forces from 1000 kN to 3000 kN are used. The powder is consolidated at platen temperatures of 190–210 °C and pressures of 5–15 MPa; hold time is typically 20–60 min depending on sheet thickness. Controlled cooling at 5–15 °C/h through the crystallization range reduces warp and internal voids. Ram extrusion of rod and profile uses barrel temperatures from 190–230 °C and back pressure of 5–20 MPa; die-land length-to-diameter ratios above 6:1 improve particle fusion. On production lines, the dominant defects are internal weld lines from insufficient compaction, oxidative yellowing from excessive residence time, and centerline porosity from trapped air. These failures are controlled by vacuum deaeration, by matching charge weight to cavity volume, and by avoiding temperature increases above the recommended band. Because PE-UHMW does not form a stable melt pool in the conventional thermoplastic sense, process optimization targets particle interfacial diffusion rather than melt-flow filling.

    The sintering kinetics of PE-UHMW are controlled by diffusion of chain ends across particle boundaries above the crystalline melting temperature. The melting point of unfilled UHMWPE is typically 130–136 °C by ISO 11357-3 differential scanning calorimetry, with a degree of crystallinity between 40% and 60%. During compression molding, the first stage heats the powder to a homogeneous 200 °C; the second stage applies pressure to remove voids; the third stage crystallizes the sheet under controlled cooling. Because molecular weight is extremely high, the rate of interparticle fusion is slow compared with HDPE. Hold times must therefore be extended, and local temperature overshoot above 230 °C can cause oxidative degradation without improving flow. Gel particles and unmelted powder cores can act as stress raisers in finished parts; class-defined PE-UHMW resins are inspected for gel count and foreign-particle contamination using optical methods specified by the supplier.

    Because PE-UHMW ER-24 is converted to final parts by machining, the material’s high coefficient of linear thermal expansion—typically 1.5 × 10⁻⁴ K⁻¹ to 2.0 × 10⁻⁴ K⁻¹ by ASTM D696—must be accommodated in mounting holes and wear clearances. This expansion value is roughly an order of magnitude higher than steel; a part machined at 20 °C and later warmed to 40 °C grows by approximately 3–4 mm per meter. In production settings, this mismatched expansion causes buckling of wear strips that are rigidly bolted without slotted holes. The recommended compensation is to use oversized mounting holes, slotted bolt patterns, and expansion gaps of 2–3 mm per meter of length for indoor temperature swings. Tight machining tolerances above ±0.05 mm are possible, but they require temperature-controlled inspection and stress-relieved stock shapes to prevent post-machining movement.

    Pressure-Velocity Limits and Filled UHMWPE Trade-Offs

    The permissible pressure-velocity product for unfilled PE-UHMW in continuous dry service is generally below 0.1 MPa·m/s for low wear and below 0.2 MPa·m/s for intermittent duty. Above this threshold, frictional surface heating accelerates wear and can soften the polymer. This ceiling is a critical difference from filled UHMWPE grades containing molybdenum disulfide, glass fiber, or crosslinked polymer networks. Filled grades may increase compressive strength and reduce wear under dry sliding but usually sacrifice notched impact toughness and elongation at break. ER-24 should not be assumed to be internally lubricated or crosslinked; its selection is based on retained ductility, impact resistance, and machinability. If a specification demands surface resistivity below 10⁹ Ω per IEC 62631-3-2, an antistatic grade—not ER-24—must be used unless supplier documentation confirms otherwise. In abrasive slurry tests such as ASTM G75, PE-UHMW class materials often show lower relative abrasion than HDPE but may rank below rigid ceramic-filled polymers; the decision therefore balances particle size, impingement angle, and impact energy rather than coefficient of friction alone.

    Crosslinked UHMWPE differs from ER-24 class material in network structure, elongation, and oxidative wear resistance. Radiation crosslinking at 50–100 kGy reduces elongation at break to 200–300% or lower and improves wear resistance in reciprocating bearing studies, but it also reduces toughness and cannot be reprocessed by melting. Non-crosslinked PE-UHMW retains its higher elongation and is preferred for impact-dominant wear strips, conveyor guides, and marine structural surfaces. If ER-24 is supplied as a non-crosslinked compression-molding resin, substitution of a crosslinked grade without redesign can lead to premature cracking at bolt holes and reduced resistance to high-rate impact; if a crosslinked grade is substituted into a sliding wear-only application, wear rate may improve but the impact safety margin decreases. The component specification must therefore state whether network density, gel fraction per ASTM D2765, or elongation at break is the controlling parameter.

    In chemical service, UHMWPE ER-24 resists dilute acids, alkalis, and many polar solvents at ambient temperature, but it is not suitable for strong oxidizing acids, halogens, or high-temperature aromatic and chlorinated solvents. Swelling in aliphatic hydrocarbons is low at room temperature but increases with chain relaxation; continuous service above 60 °C under load produces creep rates that can exceed dimensional tolerances in close-clearance wear guides. The upper short-term service temperature is commonly stated near 90 °C, but the load-bearing ceiling is lower. Ultraviolet exposure causes chain scission and surface embrittlement; outdoor components require carbon black or hindered amine stabilizers unless the part is shielded from sunlight. Because UHMWPE is difficult to bond, assembly designs use mechanical fasteners, dovetail slots, or thermal welding; adhesive bonding is not reliable unless a validated surface treatment such as plasma or flame treatment is applied and tested to an appropriate shear-strength standard.

    When the Grade Is Evaluated for Food-Contact and Pharmaceutical Sliding Surfaces

    For food-contact and pharmaceutical sliding surfaces, UHMWPE ER-24 may be evaluated under FDA 21 CFR 177.1520 for olefin polymers intended for food-contact use; the finished article must meet the end-use limitations and extractive specifications applicable to the polymer and its additives. In the European Union, compliance is typically assessed under Regulation (EU) No 10/2011 and its amendments, with an overall migration limit of 10 mg/dm² for food simulants. REACH registration under Regulation (EC) No 1907/2006 must be confirmed from the supplier safety data sheet; substances of very high concern are restricted to below 0.1 wt% per article. RoHS Directive 2011/65/EU Annex II restrictions on lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE are normally met by unfilled polyethylene resin, but finished-component compliance depends on pigments and processing aids. USP <88> Class VI testing is not an automatic property of every PE-UHMW stock; if pharmaceutical contact or bioprocessing use is intended, a lot-specific certificate is necessary. The grade should not be assumed suitable for implantable medical use unless authorized through an appropriate regulatory pathway.

    Compliance checklist for PE-UHMW ER-24 end-use qualification
    Standard or regulationTest or clauseTypical basis for PE-UHMW ER-24
    FDA 21 CFR 177.1520Olefin polymers for food contactFinished-article extractive testing; end-use limitations apply
    Regulation (EU) No 10/2011Overall migration limit 10 mg/dm²Supplier documentation for food-contact grade
    Regulation (EC) No 1907/2006 REACHSVHC content < 0.1 wt% per articleSupplier safety data sheet
    Directive 2011/65/EU RoHSAnnex II restricted substancesXRF screening and chemical digestion of finished component
    ISO 11542-1PE-UHMW classificationViscosity number > 2000 cm³/g

    In dry bulk handling, UHMWPE ER-24 liners are used to reduce wall friction and promote mass flow; the mating steel surface should be finished to 0.4–0.8 µm Ra to avoid abrasive wear of the polymer. In conveyor chain guides, the material is machined into wear strips and slide rails; bolt-hole edges should be countersunk to prevent stress concentrations. For outrigger pads and marine fender facings, the grade’s low water absorption and high impact strength provide dimensional stability under intermittent compression. Field results on production-scale equipment show that edge loading, shaft misalignment above 1°, and obstructed expansion gaps are common causes of early wear; these failure modes are often misattributed to resin quality when they are actually traceable to machining or assembly conditions. ER-24 therefore requires the same lot-specific verification of density, tensile yield, and impact strength as any engineering polymer, particularly when the finished part is subjected to high-cycle sliding or food-contact extraction testing.

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