Celanese Uhmw Pe 4056 3

Celanese UHMW-PE 4056-3

    • Product Name: Celanese UHMW-PE 4056-3
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    VTB
    Specifications
    HS Code 335827
    Density 0.95 g/cm³
    Molecularweight 5.6 million g/mol
    Bulkdensity 0.45 g/cm³
    Particlesize 120 µm
    Meltingpoint 135 °C
    Crystallinity 45 %
    Thermalconductivity 0.41 W/m·K
    Tensilemodulus 700 MPa
    Tensilestrengthatyield 17 MPa
    Elongationatbreak 300 %
    Charpynotchedimpactstrength 100 kJ/m²
    Shoredhardness 62
    Waterabsorption <0.01 %
    Coefficientoffriction 0.15
    Abrasionresistance 100
    Dielectricconstant 2.3
    Volumeresistivity >10^15 Ω·cm
    Dielectricstrength 45 kV/mm
    Flammability HB (UL 94)
    Carbonblackcontent 3 %
    Color Black

    As an accredited Celanese UHMW-PE 4056-3 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Celanese UHMW-PE 4056-3 is supplied in 25 kg moisture-resistant paper bags, palletized and shrink-wrapped for industrial handling.
    Container Loading (20′ FCL) Container Loading (20′ FCL): Celanese UHMW-PE 4056-3 packed in 25 kg bags on pallets, loaded, secured for safe ocean transport.
    Shipping Celanese UHMW-PE 4056-3 is a non-hazardous solid polymer. It is not classified as dangerous goods for transport by DOT, IMDG, IATA, or ADR; no UN number is assigned. Ship in sealed original bags, drums, or boxes. Keep dry, avoid dust, and protect from ignition sources. No special placards required.
    Storage Store Celanese UHMW-PE 4056-3 in a cool, dry, well-ventilated area, away from direct sunlight, heat, flames, and strong oxidizers. Keep original containers tightly closed to prevent moisture, dust, and contamination. Protect from UV exposure. Maintain clean, segregated storage, off floors and away from drains. Follow the SDS and local regulations. No special ventilation is normally required.
    Shelf Life Typically 2 years (24 months) if stored unopened in a cool, dry place, away from direct sunlight and moisture.
    Application of Celanese UHMW-PE 4056-3

    Wet-process lithium-ion battery separator manufacturing represents the most temperature- and shear-sensitive downstream use of Celanese UHMW-PE 4056-3 because the polymer is not pelletised and must be dispersed directly into a low-volatility paraffinic process oil under controlled shear. In this sector the formulation addition ratio is expressed as polymer weight fraction in the process-oil slurry or gel dope, typically 8–18 wt% UHMW-PE 4056-3 with 82–92 wt% paraffinic process oil; a starting evaluation point of 12 wt% polymer to 88 wt% oil is common, with subsequent adjustment until the extracted, biaxially stretched membrane reaches a Gurley air-permeability value of 200–400 s/100 cm³ at 0.02 MPa test pressure. Published data for this specific configuration with 4056-3 is limited, so pilot-scale validation on the intended twin-screw rig is required before setting injection depth and screw-speed ramp profiles. Downstream production equipment for this grade is typically a co-rotating twin-screw extruder with L/D of ≥ 52, liquid injection at barrel zone 4 or 5, melt temperature maintained at 160–230 °C, gear-pump-assisted die pressure of 35–80 bar, cast roll temperature of 20–50 °C, sequential machine-direction and transverse-direction stretching at draw ratios of 6×–10×, solvent extraction with methylene chloride or hexane, heat-setting at 110–135 °C, and slitting to roll widths of 300–1200 mm. Terminal product types include single-layer PE separator membranes, ceramic-coated microporous membranes, and PP/PE/PP trilayer laminates used in prismatic, cylindrical, and pouch lithium-ion cells. Industry compliance standards applicable to these films include tensile property measurement per ASTM D882-18 and ISO 527-3:2018, puncture resistance per ASTM F1306-21, thickness determination per ISO 4593:2019, cell-level performance validation per IEC 62660-1:2018, and transport validation under UN Manual of Tests and Criteria, Part III, subsection 38.3 when finished cells enter distribution.

    What Controls Gel-Fibre Draw Ratios in High-Modulus Polyethylene Yarn Production?

    Gel-spun high-tenacity yarn manufacturing with Celanese UHMW-PE 4056-3 is constrained by dope viscosity and disentanglement kinetics rather than by conventional melt fracture, because the polymer remains below its fully molten state in the solvent-rich gel phase. The addition ratio for the spinning dope is 2–8 parts by weight of 4056-3 per 100 parts by weight of decalin or white mineral oil; below 2 wt% polymer, solvent recovery costs become disproportionate and gel filaments lose dimensional stability, while above 8 wt% the elongational viscosity rises sufficiently to create drawing discontinuities and filament diameter coefficient of variation above 5%. In a typical line the powder is slurried in cold solvent, then fed into a co-rotating twin-screw dissolver with L/D ≥ 48, jacket temperature 180–250 °C, and residence time 8–20 min; the solution is metered through a gear pump and a spinneret with capillary diameters 0.5–1.5 mm at 35–80 bar pressure, quenched in an air gap and then in a water bath at 5–25 °C. Gel filaments are extracted with n-hexane or dichloromethane to reduce residual oil below 0.1 wt%, then hot-drawn in stages to total draw ratios of 30:1–60:1 to achieve tenacities above 2.0 GPa. Terminal product types include high-tenacity filament yarns, cut-resistant glove liners, ballistic helmet shells, composite armour backings, lifting slings, marine ropes, synthetic winch lines, and fishing netting. Compliance standards include yarn breaking force per ISO 2062:2009, linear density per ISO 2060:1994, cut resistance per EN 388:2016+A1:2018, ballistic resistance per NIJ 0101.06, and chemical management under EU REACH 1907/2006. Process limitations are explicit: decalin is a combustible solvent requiring explosion-proof enclosures and nitrogen inerting below 8% oxygen, and antioxidant addition at 0.1–0.2 phr based on polymer mass is typical to suppress thermo-oxidative gelation during dissolution.

    Ram Extrusion Profiles for Conveyor Guide Rails and Chain Guides

    Ram extrusion of Celanese UHMW-PE 4056-3 differs fundamentally from screw plastication because the powder is pressure-compacted through a heated die without fully melting and without imparting screw shear. The material is charged at a feed temperature of 20–40 °C, densified in a reciprocating ram cylinder, and advanced through a die with land temperature 180–220 °C and exit cooling to below 90 °C before cut-off. In unfilled profiles, the formulation addition ratio is 100 parts by weight 4056-3 powder with no solvent and no internal lubricant; where enhanced lubricity or electrostatic dissipation is required, processors often shift to pre-compounded grades because direct addition of graphite above 5 wt% or carbon black above 3 wt% to this high-molecular-weight powder can destabilise the ram compaction front and create weld-line porosity. Downstream production uses an alternating twin-ram extruder or single-ram extruder with die swell compensation, followed by water or air cooling, puller alignment, and CNC machining of rod, sheet, or profile to final tolerances of ±0.05 mm for guide rail dimensions. Terminal product types include bottling-line chain guides, profile wear strips, scraper blades, pump wear plates, star wheels, curved guide rails, and food-processing conveyor components. Industry compliance standards include material specification per ASTM D4020-18, tensile properties per ISO 527-1:2019, density by ISO 1183-1:2019, Shore D hardness by ISO 868:2003, and, for food-contact applications, extraction testing under FDA 21 CFR 177.1520 and EU 10/2011 when migration limits are met.

    Historically, compression molding of 4056-3 into solid liners and chute plates uses closed steel tools heated to 200–220 °C under platen pressure 3–10 MPa, with cooling under pressure to below 60 °C to minimise warpage; the addition ratio is 100 parts virgin powder without solvent, and terminal product types include hopper liners, seal plates, pump volute liners, and wear pads. Compliance for these parts is typically verified against ASTM D4020-18 for incoming powder quality and ISO 9001:2015 for batch traceability.

    When Porous Sintered Media Require Interparticle Void Retention

    Porous sintered components produced from Celanese UHMW-PE 4056-3 depend on partial consolidation of powder particles at the die wall and interparticle boundaries without eliminating the void network. The formulation addition ratio is 100 parts by weight 4056-3 powder; if controlled pore diameters above 20 µm are required, processors use removable pore-forming fillers such as sodium chloride or low-molecular-weight polyethylene wax at 10–30 parts per hundred powder, but direct filler use with this grade requires pre-screening to avoid filler segregation because the high molecular weight limits reflow during sintering. Downstream production uses vibratory or gravity filling of near-net-shape steel moulds, sintering at 160–200 °C under sufficient pressure to form particle necks, and slow cooling before ejection; porous sheets, tubes, and cylinders are then machined or die-cut. Terminal product types include pneumatic exhaust mufflers, silencer elements, filter sheets, vent plugs, porous wick components, and air-permeable vent membranes. Compliance standards applicable to porous forms include pore-size characterisation by ASTM F316-03(2019), porosity calculated from bulk density by ISO 1183-1:2019, and material quality under ASTM D4020-18; published data for this specific configuration with 4056-3 is limited, so pilot sintering trials are recommended before production release.

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    Certification & Compliance
    More Introduction
    Celanese UHMW-PE 4056-3 is a high-molar-mass ultra-high-molecular-weight polyethylene (PE-UHMW) grade within the GUR portfolio. The numerical designation identifies a nominal average molecular weight of approximately 5.6 × 10⁶ g/mol, although the current Celanese technical datasheet remains the governing source for lot-specific values. The product is supplied as powder or consolidated stock for compression moulding, ram extrusion, and machining. In common with PE-UHMW grades classified under ASTM D4020 and ISO 21304-1, the material does not produce a meaningful melt mass-flow rate under ISO 1133-1:2022 because the high molar mass and chain entanglement prevent standard piston flow. Typical PE-UHMW homopolymer performance includes a density between 0.930 g/cm³ and 0.945 g/cm³ measured by ISO 1183-1. The crystalline melting peak is observed between 130 °C and 136 °C by differential scanning calorimetry per ISO 11357-3. Because the grade is intentionally high-molecular-weight, conventional melt flow data are replaced by solution viscosity number according to ISO 1628-3 as a release parameter. Batch-to-batch variation in powder bulk density and viscosity number can influence consolidation behaviour; production lots with lower bulk density often require tighter feed control on ram extrusion lines to prevent bridging. Published data for this specific grade configuration is more limited than for commodity HDPE. The values cited in this document are representative PE-UHMW ranges and must be verified against the current Celanese certificate of analysis before design.

    Which physical property thresholds define the 4056-3 grade?

    For most wear and structural applications, the material is specified against the property set below. The table presents representative ranges for PE-UHMW 4056-3 under standard specimen preparation. These values are not absolute design allowables because machined-part performance depends on stock shape, fusion quality, and machining-induced surface damage.
    PropertyTest methodRepresentative range
    DensityISO 1183-1 / ASTM D7920.930–0.945 g/cm³
    Tensile yield stressISO 527-2 / ASTM D638-1421–28 MPa
    Tensile elongation at breakISO 527-2 / ASTM D638-14>300 %
    Notched Izod impactASTM D256no break
    Shore D hardnessISO 868 / ASTM D224060–70
    Vicat softening temperature A50ISO 306 / ASTM D152580–85 °C
    Water absorption 24 hASTM D570<0.01 %
    Creep and wear performance are not captured by short-term tensile data. For continuous load-bearing applications above 60 °C, creep modulus can decline rapidly; design calculations should use creep-rupture data generated on the fabricated form rather than room-temperature tensile properties. Processing the high-viscosity powder requires positive pressure and sufficient time at temperature to achieve chain interdiffusion across particle boundaries. Compression moulding is typically performed at 10–20 MPa and 190–220 °C, with hold times extended to 30–60 min for thick sections to avoid incomplete fusion. Cooling under pressure to below 60 °C before demoulding reduces warpage and residual stress. Insufficient pressure or a heating ramp below 180 °C produces powder-grain boundary defects that appear as chalky, low-impact fracture surfaces. Ram extrusion of rod and sheet uses barrel temperatures between 180 °C and 220 °C; the die temperature is often maintained slightly above the crystalline melting point to control melt fracture. Production ram extruders for high-molar-mass grades frequently operate below 0.1 m/min; higher pull rates increase axial residual stress and centreline porosity. Pre-drying at 80 °C for 2–4 h is applied when ambient relative humidity exceeds 60 % because adsorbed moisture can form microvoids during consolidation. Conventional single-screw extrusion is generally avoided for 4056-3; published data for continuous screw plastication of this exact grade is limited. Cold pre-compaction at 5–10 MPa prior to heating improves powder contact and reduces trapped air in thick sections. For compression moulding presses, platen temperature uniformity should be maintained within ±3 °C across the part; larger platens with uneven heating can produce differential crystallinity and warpage. Production-scale empirical checks include visual inspection of machined surfaces for chalky zones and notched impact testing of coupons cut from the centre of thick sections. Machining of 4056-3 stock produces discontinuous chips; tool geometry should use high positive rake and generous clearance to reduce melt smearing. Dimensional control is complicated by a coefficient of linear thermal expansion near 1.5 × 10⁻⁴ K⁻¹; parts machined at elevated temperature can shift in size after cooling.

    Melt viscosity and grade-to-grade variation within the GUR portfolio

    Relative to lower-molecular-weight PE-UHMW grades such as GUR 4120 and GUR 4022, the 4056-3 grade has a longer reptation time for chain interdiffusion, which scales approximately with molar mass to the 3.4 power. This molecular-weight difference is the principal source of processing conflict: higher hardness and abrasion resistance require higher molar mass, but higher molar mass reduces molecular mobility and increases required moulding hold time. The numeric designation of GUR 4120 corresponds to approximately 1.2 × 10⁶ g/mol, GUR 4022 to approximately 2.2 × 10⁶ g/mol, and 4056-3 to approximately 5.6 × 10⁶ g/mol. These are grade-class identifiers rather than measured molecular weights. In the sand-slurry abrasion test of ISO 15527, higher-molar-mass PE-UHMW grades typically show lower volume loss than lower-MW grades; actual values depend on slurry velocity, particle angularity, and test temperature. Published data for this specific configuration is limited, so comparative wear screening should be performed against the candidate replacement grade in the same fixture. The solution viscosity number measured by ISO 1628-3 is the most reliable release parameter for differentiating grades. When raw powder changes from lower-MW to higher-MW material, ram extrusion lines often require a reduction in pull rate and an increase in heating zone residence time. Batch-to-batch variance in solution viscosity number and powder bulk density can shift the processing window by several degrees; production personnel typically monitor motor load and dimensional swell to adjust the feed rate. Sliding-wear and impact applications make use of the combination of low dry-sliding friction and high notched impact strength. Pin-on-disc testing per ASTM G99 against polished steel commonly places the dynamic coefficient of friction between 0.10 and 0.25, depending on surface finish, sliding velocity, and contact pressure. The static coefficient can be higher, particularly at low speeds. The grade is therefore specified for chain guides, wear strips, star wheels, conveyor idlers, buffer pads, and hopper liners where impact loads accompany abrasive sliding. The high molar mass of 4056-3 shifts the ductile-to-brittle transition toward lower temperatures; notched Izod specimens prepared per ASTM D256 often report no break at -196 °C. This characteristic differentiates the material from HDPE, which can exhibit brittle fracture under the same conditions. HDPE notched Izod impact per ASTM D256 typically falls between 100 J/m and 200 J/m; the same test on well-fused PE-UHMW 4056-3 usually records no break. The impact result is strongly dependent on fusion quality and notching practice; machined corners and sharp chamfers act as stress concentrators and may reduce component-level impact performance below the datasheet value. Surface finish of fabricated stock is controlled to Ra 0.8 µm or lower for dynamic seal rails and wear guides. Rougher surfaces increase initial wear debris generation and can elevate steady-state wear rate during the bedding-in period. Oxidative degradation is monitored by oxidation induction time per ISO 11357-6; a reduction from the virgin-powder value indicates stabilizer depletion in reclaimed material.

    When 4056-3 replaces HDPE or PTFE in sliding-wear service

    When 4056-3 replaces HDPE in chilled or abrasive service, the primary benefit is a reduction in abrasive wear rate and improved low-temperature impact resistance. The trade-off is a longer consolidation cycle and reduced melt processability. When the replacement targets PTFE, the coefficient of friction is higher than PTFE; however, PE-UHMW often exhibits higher wear resistance under high-load or particle-contaminated conditions. Direct one-to-one substitution without clearance modification can fail because PE-UHMW has a higher thermal expansion coefficient than steel, near 1.5 × 10⁻⁴ K⁻¹ per ASTM D696; running clearances must be adjusted to avoid seizure at elevated temperature. The maximum continuous service temperature under load is lower than PTFE. Creep resistance above 90 °C is limited; PTFE remains more suitable for non-lubricated sliding at elevated temperature unless a filled PE-UHMW is qualified. In addition, 4056-3 is not intended for continuous exposure to strong oxidizing acids, chlorine gas, or aromatic hydrocarbons at elevated temperatures, which can cause environmental stress cracking or oxidative embrittlement. Regulatory compliance for 4056-3 depends on the specific lot, the conversion process, and any added stabilizers or processing aids. PE-UHMW homopolymers in this family may be formulated to meet FDA 21 CFR 177.1520 for food-contact olefin polymers, provided that end-use extraction testing is completed on the finished article. The material is subject to REACH Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU; absence of halogenated flame retardants and heavy metals must be confirmed against the safety data sheet. For medical device use, ASTM F648 applies only to implant-grade PE-UHMW powder and fabricated forms; the 4056-3 grade should not be assumed to meet implant specifications without a dedicated qualification under ISO 10993-1. Biocompatibility assessment under ISO 10993-1 includes cytotoxicity per ISO 10993-5, sensitization per ISO 10993-10, and irritation per ISO 10993-23 where applicable. These tests are performed on the final device, not on raw resin.
    ScopeStandard/regulationApplicability
    Food contactFDA 21 CFR 177.1520Lot-specific; extraction testing required
    EU chemical registrationREACH (EC) No 1907/2006Substance/import compliance
    RoHSDirective 2011/65/EUCertified absence of restricted substances
    General classificationASTM D4020 / ISO 21304-1PE-UHMW material specification
    Surgical implantASTM F648 / ISO 10993-1Only if dedicated grade; not assumed
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