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Beijing Evergrow Resources UHMWPE UHF-W800

    • Product Name: Beijing Evergrow Resources UHMWPE UHF-W800
    • 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 595740
    Product Name Beijing Evergrow Resources UHMWPE UHF-W800
    Brand Beijing Evergrow Resources
    Model UHF-W800
    Material Ultra-high molecular weight polyethylene (UHMWPE)
    Type UHMWPE fiber
    Form Continuous filament yarn
    Denier 800D
    Color White
    Density 0.97 g/cm³
    Melting Point 144-152 °C
    Tensile Strength ≥30 cN/dtex
    Elastic Modulus ≥1000 cN/dtex
    Elongation At Break ≤3.5%
    Moisture Regain 0%
    Chemical Resistance Excellent
    Uv Resistance Good
    Abrasion Resistance Excellent

    As an accredited Beijing Evergrow Resources UHMWPE UHF-W800 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Typically supplied in 25 kg multi-wall paper bags or woven sacks, palletized, for Beijing Evergrow Resources UHMWPE UHF-W800.
    Container Loading (20′ FCL) Non-hazardous 20′ FCL loading of Beijing Evergrow Resources UHMWPE UHF-W800, palletized bags, shrink-wrapped and securely stowed for export.
    Shipping Beijing Evergrow Resources UHMWPE UHF-W800 is normally shipped as a non-hazardous polymer powder in sealed 25 kg bags or fiber drums, palletized and shrink-wrapped. Keep dry, cool, and away from UV, ignition sources, and strong oxidizers. Ensure local transport regulations are met.
    Storage Store Beijing Evergrow Resources UHMWPE UHF-W800 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and strong oxidizers. Keep original containers or bags tightly sealed and palletized off the floor. Prevent moisture, dust, oil, and chemical contamination. Maintain good housekeeping and avoid prolonged elevated temperatures. No special ventilation required under normal conditions.
    Shelf Life Shelf life: 2 years when stored cool, dry, well-ventilated, and protected from direct sunlight, moisture, and heat.
    Application of Beijing Evergrow Resources UHMWPE UHF-W800

    In wet-process lithium-ion battery separator lines, UHMWPE is not processed as a neat resin but is dispersed into an HDPE-rich matrix through a paraffinic oil gel route before biaxial drawing. UHF-W800 is introduced at 5 wt% to 15 wt% of the polymer fraction when cast film must survive sequential machine-direction and transverse-direction stretching below 25 μm final thickness. The extrusion unit is normally a co-rotating twin-screw machine with 35:1 L/D to 45:1 L/D and multiple injection ports for liquid paraffin; melting and mixing zones are held between 160 °C and 200 °C, because local shear heating above 220 °C produces oil exudation and destabilises the gel boundary at the T-die exit. The gel sheet is cast onto a chill drum at 20 °C to 40 °C with a die-to-roll draw-down of 10:1 to 30:1; machine-direction drawing is set from 3:1 to 7:1 and transverse-direction drawing from 6:1 to 10:1. Solvent extraction with n-heptane or methylene chloride must reduce residual oil below 100 ppm before heat-setting at 90 °C to 110 °C. The finished lithium-ion separator has porosity of 35% to 50%, a mean pore diameter between 40 nm and 100 nm, and is tested under ASTM D882-18 for thin-film tensile and a voltage-based pinhole inspection at 1.0 kV to 2.5 kV. Compliance is weighted to REACH SVHC concentration below 0.1 wt% and RoHS Directive 2011/65/EU restricted substances; cell assemblers may also require IEC 62281 transport test evidence. The process conflict is that weight fractions above 15% increase T-die backpressure and produce transverse thickness variation beyond ±2%, while fractions below 5% leave insufficient entanglement strength to resist pinhole formation during transverse draw. Published data for this specific grade in commercial separator formulations is limited; pilot-scale extrusion on a 45:1 L/D twin-screw line is required before continuous cast-film campaigns.

    What Controls Draw Ratio and Gel Homogeneity in Gel-Spun Fibre Production?

    Gel spinning imposes a narrow window between solution intimacy and extrusion pressure because UHMWPE entanglements remain partially intact even at 5 wt% solids. UHF-W800 is dissolved in decalin or paraffin oil at 5 wt% to 15 wt%; the twin-screw dissolution zone is held below 200 °C and a gear pump delivers the solution through spinneret capillaries of 0.5 mm to 1.0 mm diameter at 3 MPa to 8 MPa. Gel filaments are quenched in water below 10 °C, drawn after extraction in multiple stages, and total draw ratios between 30:1 and 80:1 are common. The residual solvent must remain below 100 ppm because retained oil acts as an internal lubricant that suppresses creep resistance. Tenacity values for industrial high-modulus polyethylene yarns typically fall between 30 cN/dtex and 40 cN/dtex, with tensile modulus from 1,000 cN/dtex to 1,600 cN/dtex; testing is performed under ASTM D2256-22 and ISO 2062:2009. End products are cut-resistant gloves, ballistic panels, marine ropes, and industrial slings. The boundary condition is severe: raising solution concentration above 15 wt% raises gear-pump pressure beyond 10 MPa and can induce spinneret leakage; drawing before the gel filament reaches 120 °C to 140 °C causes axial fibrillation. This route requires a closed solvent recovery system and is not executable on conventional granular HDPE fibre equipment.

    Ram Extrusion Pressure Profiles in Guide Rail and Wear Strip Production

    Production-scale ram extruders making UHMWPE guide rails and wear strips do not melt-pump the resin; the feed zone compacts powder into a solid slug that is pushed through heated barrel sections by a hydraulic ram. For UHF-W800 the barrel is zoned from 180 °C at the feed throat to 220 °C at the die adapter, with the die body at 200 °C to 230 °C. Ram pressure is held between 15 MPa and 35 MPa, and stroke speed is 0.5 mm/s to 2.0 mm/s depending on cross-section. The powder bulk density should be measured under ASTM D1895-17 Method A; feed lots with bulk density below 0.40 g/cm³ stretch the compaction zone and create longitudinal seams. Heater bands must be separated because UHMWPE thermal conductivity is low; a calibration die length of 20:1 to 30:1 relative to die opening is used to stabilise dimensions. End products are bottle-conveyor guide rails, chain-guided packaging wear strips, and dry-running machine pads, machined to ±0.2 mm on wear faces. Mechanical verification rests on ASTM D4020-18, ISO 11542-1:2001, ASTM D638-14, ISO 178:2019, and ISO 868:2003. For food-contact service, the finished machined article must satisfy FDA 21 CFR 177.1520(c) and EU 10/2011 overall migration limits after surface machining. The dominant failure is internal axial porosity from insufficient die-adapter hold time; porosity above 2% by optical image analysis reduces service life and causes delamination under cyclic side loads.

    Application routeGoverning standard or regulationMaterial or finished-part propertyAcceptance threshold
    Food-contact conveyor guide railFDA 21 CFR 177.1520(c), EU 10/2011Overall migration on machined surface10 mg/dm² or actual simulant limit
    Orthopaedic bearing stockISO 5834-2:2019, ASTM F648-21, ISO 10993-1:2018Device-specific tests; no generic raw-powder pass/failAs set by device risk file
    Battery separator filmREACH (EC) No 1907/2006, RoHS Directive 2011/65/EUSVHC concentration; restricted substance level0.1 wt% per SVHC; Cd 0.01 wt%
    Potable-water sintered filterNSF/ANSI 61Leachate acceptance under potable-water protocolPass as certified article

    Because the melt viscosity of UHMWPE remains too high for screw plastication, orthopaedic bearing stock is converted by direct compression molding or ram extrusion followed by machining, and the process window is controlled by oxidation history rather than by flow. UHF-W800 is an industrial engineering resin and must be independently qualified against ISO 5834-2:2019 and ASTM F648-21 before any implantable use; the raw-powder certificate is not sufficient. In direct compression molding, powder is charged into a preheated mould at 200 °C to 240 °C, pressed at 15 MPa to 30 MPa, and held for 30 min to 60 min for a 50 mm slab because low thermal diffusivity delays centreline consolidation. Cooling under pressure is maintained at 5 °C/min to 15 °C/min; faster cooling reduces crystallinity and modulus, while slower cooling can enlarge spherulitic boundaries that act as crack-initiation sites. Machined acetabular liners or tibial inserts are tested per ASTM F2102-17 for oxidation index and per device-control tensile and impact methods. If radiation crosslinking is used, the absorbed dose is typically 25 kGy to 100 kGy, followed by remelting above 150 °C to quench residual free radicals. The processing boundary is narrow: mould temperatures below 200 °C leave translucent fusion defects at particle interfaces, while temperatures above 240 °C raise the FTIR ketone carbonyl peak. The powder is incompatible with amine-based additives that accelerate discolouration during long consolidation cycles, and pre-drying at 80 °C for 4 h is required after storage above 60% relative humidity.

    When Sintered Porous Elements Require Controlled Interstitial Pore Diameters

    Sintered porous media made from UHMWPE powder rely on particle necking at contact points rather than full densification, and pore-size distribution is governed by the feed particle-size distribution. For UHF-W800, narrow sieve fractions with D50 from 100 μm to 250 μm are levelled in a mould cavity by vibration before entering a convection oven at 180 °C to 200 °C with temperature uniformity of ±2 °C. Sintering time is 30 min to 90 min for tube walls between 5 mm and 30 mm; heating rates above 10 °C/min can form a surface skin that closes surface pores. The resulting void volume is 20% to 40%, with bubble-point pore diameters from 10 μm to 80 μm controlled by blending coarse and fine fractions or by using a single classified fraction. Pore-size verification is performed by bubble-point or mean-flow pore methods under ASTM F316-03. End products include gas-diffusion plates for water treatment, pneumatic silencers, air-venting membranes, and fluidising plates for powder conveying. For potable-water contact, the sintered article is assessed under NSF/ANSI 61, and no plasticising additives may be introduced during the sintering step. Continuous service above 80 °C can relax the sintered necks and reduce crush strength; therefore the filter housing must prevent steam breakthrough in air-venting service.

    When UHMWPE powder is added to HDPE or polypropylene compounds for abrasion resistance, the target is a dispersed wear phase rather than a fused continuous network, and the extruder must avoid building a gel network that chokes the die. UHF-W800 is compounded at 5 wt% to 15 wt% into a high-flow HDPE carrier with an MFI of 5 g/10 min to 20 g/10 min at 190 °C/2.16 kg under ISO 1133-1:2022; for polypropylene matrices the carrier MFI is generally 10 g/10 min to 30 g/10 min at 230 °C/2.16 kg. The UHMWPE powder is side-fed after the melt zone of a co-rotating twin-screw extruder with 36:1 L/D to 48:1 L/D, screw speed 300 rpm to 600 rpm, and melt temperature capped at 220 °C. The resulting compound is used in industrial pallet feet, cable guides, and low-speed gear wheels where the dispersed UHMWPE phase lowers coefficient of friction and improves abrasion resistance measured under ISO 9352:2012. Dispersion quality is checked by polished-plate microscopy and Charpy impact testing under ISO 179-1:2010; a poorly dispersed compound shows delamination and reduced impact energy. The rheological boundary is firm: exceeding 15 wt% UHMWPE in a low-MFI matrix can produce die-plate pressure spikes above 100 bar and strand instability that cannot be corrected by screw-speed adjustment. Food-contact or implantable status should not be assumed from this compounding route; the finished article must be separately tested under the applicable finished-product standard.

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    Certification & Compliance
    More Introduction

    Beijing Evergrow Resources UHMWPE UHF-W800 is a virgin ultra-high-molecular-weight polyethylene powder supplied primarily for solid-state conversion processes. The product model UHF-W800 carries a nominal viscosity-average molecular weight of 8.0 × 10⁶ g/mol in distributor documentation, placing it in the upper molecular-weight segment of ISO 11542-2:1998. The material is differentiated from standard high-density polyethylene by the absence of a measurable melt flow rate under ISO 1133-1:2022 or ASTM D1238-20; typical HDPE grades flow at 0.3–20 g/10 min, whereas UHF-W800 is reported as non-flowing. Product-specific certificates are limited, so the values discussed below are representative of the high-molecular-weight UHMWPE class and must be confirmed against lot-specific data before production qualification.

    Potential conversion routes for UHF-W800 include compression molding of sheet and block, ram extrusion of rod and profile, gel spinning of high-tenacity fiber, and wet-process film or separator manufacturing. In solid-state applications, the powder is used for wear strips, guide rails, hopper liners, star wheels, and similar components where abrasion resistance and dimensional stability are required. In solution-based processes, the same molecular weight class is evaluated where narrow particle size distribution, low residual catalyst, and low gel defect counts matter. No single grade is universally suited to every conversion line; pilot trials are necessary for solution processes. For food-contact use, compliance may be evaluated under FDA 21 CFR 177.1520, but specific regulatory confirmation is end-use dependent.

    What Constitutes the Relevant Specification Set for Incoming Quality Control?

    Incoming QC for UHMWPE powder of this molecular weight generally includes viscosity-average molecular weight, apparent bulk density, particle size distribution determined by laser diffraction under ISO 13320:2020, ash content under ISO 3451-1:2019, and molded-plaque tensile behavior. The table below summarizes typical ranges for UHMWPE resins near 8 × 10⁶ g/mol. It is not a substitute for the supplier certificate of analysis for UHF-W800.

    ParameterTypical range or valueTest designation
    Viscosity-average molecular weight8.0 × 10⁶ g/mol nominalASTM D4020-18 / ISO 1628-3:2010
    Bulk density0.40–0.50 g/cm³ISO 60:1977 / ASTM D1895-96
    Density of molded plaque0.930–0.940 g/cm³ISO 1183-1:2019
    Tensile yield stress17–25 MPaISO 527-2:2012
    Elongation at break>300 %ISO 527-2:2012
    Notched Izod impact, 23 °Cno breakISO 180:2000
    Shore D hardness60–70ISO 868:2003
    Melt flow rate, 190 °C/21.6 kgnon-measurable / no flowISO 1133-1:2022

    Particle size distribution is a relevant additional specification because it controls powder flow into ram extruders and solvent wetting in gel processes. For comparable high-molecular-weight powders, the median particle size is commonly between 100 μm and 250 μm by laser diffraction, with low fines and controlled top size. UHF-W800 release limits may differ; this point should be clarified with the supplier, especially when the powder is intended for filtration-limited solvent lines.

    The absence of a measurable melt flow rate is not an instrument artifact. At 8.0 × 10⁶ g/mol, the entangled network does not reach terminal flow at 190 °C under 21.6 kg load; the sample remains a compacted solid in the melt indexer reservoir. The practical consequence is that ordinary single-screw extruders with L/D ratios of 24:1 or 30:1 are unsuitable for unmodified UHF-W800 powder because there is no molten phase to pump along the barrel. Attempts to force the material through heated screw extruders generate high motor loads, poor heat transfer, and oxidative discoloration before the core reaches fusion temperature. Injection molding is likewise excluded because mold filling depends on melt flow, and no practical injection pressure can fill thin-wall cavities without degrading the molecular weight that defines the material. These restrictions are fundamental boundaries of UHMWPE rheology, not defects of a specific production lot.

    Ram Extrusion and Compression Molding Conditions for Stock Shapes

    Ram extrusion is the primary stock-shape conversion route for UHF-W800 rod and profile. In intermittent ram extrusion, powder is compacted by a hydraulic ram and sintered in a heated die. Industrial ram extruders for UHMWPE operate at die temperatures from 180 °C to 240 °C and compaction pressures from 15 MPa to 60 MPa, depending on die diameter and cross-section. The lower temperature limit is set by incomplete powder fusion, while the upper limit is set by thermo-oxidative chain scission and discoloration. Heat transfer from the die wall to the powder plug is slow, so throughput scales with die surface area rather than cross-sectional volume; thick profiles require lower ram speeds and longer residence time to allow the core to reach fusion temperature.

    Experience from production-scale lines shows that batch-to-batch shifts in bulk density, even from 0.42 g/cm³ to 0.48 g/cm³, alter feed compaction and require adjustment of ram stroke or heating zone setpoints. Powders with high top sizes above 350 μm may bridge in feed hoppers, while excessive fines can reduce bulk density and cause dust accumulation in the press area. These effects are mechanical rather than chemical but have a direct influence on product consistency.

    Compression molding of thick sheet and block uses similar sintering behavior. A heated press with flat platens is loaded with powder and heated at 200–220 °C. The press then applies 5–10 MPa and holds the part until the core is consolidated. Cooling under pressure at rates below 10 K/min through the crystallization range, near 120–130 °C, is used to reduce void coalescence and residual stress. Rapid cooling can produce stresses that appear as dimensional movement after machining. Mold insulation and platen temperature uniformity are critical because UHMWPE has low thermal conductivity; thick sections can retain heat for hours and must not be removed from the press before the core has crystallized.

    When UHF-W800 Powder Is Evaluated for Gel Spinning and Separator Film Lines

    In gel spinning, UHMWPE powder is dissolved in a high-boiling solvent such as paraffin oil or decalin at 120–160 °C under inert atmosphere. The solution is then extruded through spinnerets, cooled, and drawn after solvent removal. UHF-W800 may be considered for this route when the producer’s release data demonstrate low residual catalyst, low gel-level contamination, and controlled particle size. Undissolved fine particles or catalyst residues can block filtration packs and create filament defects. For comparable grades, acceptance limits are often set at ash below 300 ppm and a maximum particle size below 200 μm; actual UHF-W800 release limits must be obtained from the manufacturer.

    Wet-process separator film lines similarly require consistent dissolution and extrusion without gel particles. The resin is compounded with solvent and plasticizer, extruded into sheet, and stretched to create porosity. UHF-W800 should not be blended with flow-modified UHMWPE grades containing external lubricants or lower molecular weight fractions unless the resulting blend has been validated for pore structure and thermal shutdown behavior. Published comparative data for this specific configuration is limited; converter trials on the actual line are necessary before specification.

    Against 2–3 × 10⁶ g/mol UHMWPE, UHF-W800 presents increased entanglement density and a measurable reduction in low-stress abrasive wear. Comparative screening under ISO 15527:2018 sliding abrasion or ASTM G75 slurry abrasion generally shows lower volume loss for the higher-molecular-weight material class, but the magnitude depends on counterface roughness, abrasive particle sharpness, and test duration. The trade-off appears in processing: the higher molecular weight reduces particle mobility during sintering, requiring longer preheating time or slightly higher compaction force than lower-molecular-weight UHMWPE. In applications with moderate wear and sufficient toughness, a 3 × 10⁶ g/mol grade may be easier to consolidate and less sensitive to temperature gradients in thick sections.

    Compared with HDPE, the selection boundary is more fundamental. HDPE melts and can be injection molded, blown-film processed, and extruded on conventional screw lines. UHF-W800 cannot be melt-processed without chain degradation. The use of UHF-W800 is therefore justified only where solid-state abrasion resistance, low friction, and high impact strength are decisive; it is not a drop-in replacement for HDPE in thin-wall injection molding or high-speed extrusion.

    Oxidative Degradation, Storage, and Additive Compatibility Boundaries

    The high-molecular-weight UHMWPE class is sensitive to oxidation during high-temperature consolidation. At processing temperatures above 250 °C, hydroperoxide formation can initiate chain scission at the part surface, generating lower-molecular-weight fractions and brittle zones. The actual onset temperature shifts with stabilizer package, residual catalyst, and oxygen concentration; it should be assessed by oxidation induction time under ISO 11357-6. If custom stabilizers or colorants are required, their thermal stability should be verified under the same method before use on a production press.

    In storage, UHF-W800 absorbs negligible moisture, but condensation on cold powder exposed to high-humidity air can produce surface defects in extruded profiles. Drums stored outdoors should be conditioned in the press room before opening; if the ambient relative humidity exceeds 60 %, condensation risk should be evaluated. The powder should not be dry-blended with copper-based pigments or transition-metal salts known to accelerate polyolefin oxidation. Strong oxidizing acids and chlorinated solvents can attack UHMWPE under stress, so chemical resistance claims require actual medium testing rather than inference from the polymer family. Regulatory documentation under REACH and RoHS Directive 2011/65/EU is typically maintained for neat UHMWPE, but final compliance depends on the supplier’s substance declaration for the specific grade and any additives present.

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