Celanese Uhmw Pe 4050

Celanese UHMW-PE 4050

    • Product Name: Celanese UHMW-PE 4050
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 947751
    Density 0.93 g/cm³
    Molecular Weight 4.0 × 10^6 g/mol
    Bulk Density 0.30 g/cm³
    Average Particle Size 50 µm
    Melting Point 130-135 °C
    Crystallization Temperature 118 °C
    Tensile Modulus 750 MPa
    Tensile Strength At Yield 17 MPa
    Elongation At Break >300%
    Charpy Notched Impact Strength No break
    Shore D Hardness 62
    Water Absorption <0.01%
    Thermal Conductivity 0.41 W/m·K
    Coefficient Of Linear Thermal Expansion 2.0 × 10^-4 /°C
    Dielectric Constant 2.3
    Volume Resistivity >10^14 Ω·cm
    Coefficient Of Friction 0.1-0.2

    As an accredited Celanese UHMW-PE 4050 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Celanese UHMW-PE 4050 is typically packaged in 25 kg multiwall paper bags or 500 kg bulk bags, palletized for shipment.
    Container Loading (20′ FCL) Celanese UHMW-PE 4050 is palletized in 25 kg bags and securely loaded into a 20-foot FCL container for ocean shipment.
    Shipping Celanese UHMW-PE 4050 is a non-hazardous polyethylene solid/powder. It is not regulated as dangerous goods for transport. Ship in clean, dry, sealed bags, drums, or bulk containers. Protect from moisture, contamination, and ignition sources. No UN number, hazard class, packing group, or placards required; follow the SDS and local rules.
    Storage Store Celanese UHMW-PE 4050 in a cool, dry, well-ventilated area away from direct sunlight, heat, flames, and ignition sources. Keep original packaging tightly closed to prevent moisture, dust, and contamination. Avoid contact with strong oxidizing agents. Protect from prolonged UV exposure. Do not stack excessively; rotate stock. Use clean handling equipment. No special temperature control is normally required.
    Shelf Life No specific shelf life; stable indefinitely when stored cool, dry, sealed, and away from direct sunlight.
    Application of Celanese UHMW-PE 4050

    Celanese UHMW-PE 4050 powder is introduced into closed porous-mold cavities without pre-compounding when the target component is a sintered vent plug, pneumatic silencer, or liquid filter plate. Dry powder with bulk density 0.40–0.52 g/cm³ is filled under vibration at 50–100 Hz to reduce void variation, then compacted at 1–3 MPa while the mold is heated to 170–195 °C. Hold time at peak temperature is normally 10–30 min per 10 mm of wall thickness. Cooling from the peak temperature is controlled at 2–5 K/min to prevent skin densification and to keep interconnected porosity uniform. Final sintered density for filtration grades commonly falls between 0.60 g/cm³ and 0.85 g/cm³, with mean pore diameter from 5 µm to 50 µm depending on particle-size distribution. Pore-size distribution is checked by mercury intrusion porosimetry per ISO 15901-1, and bulk part density is checked by ISO 1183-1. Dimensional tolerance after cooling is typically ±1.5 % to ±2.0 %; through-hole plugs and threaded adapters usually require a secondary machining step because sintered UHMW-PE cannot reliably form sharp threads in the mold. Published data for this specific 4050 sintered configuration is limited; process parameters are therefore confirmed by first-article part inspection rather than by standard mold-flow analysis. The finished sintered parts serve in pneumatic silencers on packaging-line valves, vent plugs for gearboxes, and filtration plates used in low-pressure liquid clarification. Because the material retains high impact resistance after sintering and does not hydrolyze in water, the components are substituted for bronze and sintered polypropylene in applications where metal noise or corrosion is unacceptable.

    What Limits Ram Extrusion Throughput When 4050 Is Selected for Bottling-Line Wear Guides?

    Ram extrusion is selected for 4050 because the high molecular weight prevents stable screw plasticization without severe melt fracture and die swell. The process is discontinuous: powder is fed into a heated die cavity, compressed by a hydraulically driven ram, and held under pressure until the compacted material fuses into a void-free profile. Throughput is limited by heat conduction through the polymer rather than by screw speed, so die-land length must be matched to cross-section. A land ratio of 8:1 to 12:1 is typical for rectangular wear guides, with barrel wall temperature set between 180 °C and 220 °C and die temperature 200–230 °C. Ram pressure is held at 10–25 MPa depending on profile thickness; thicker sections require longer hold times of 2–5 min per 10 mm. If the die wall temperature drops below 175 °C, inter-particle fusion becomes incomplete and the extruded profile can delaminate under abrasive service. If the die wall exceeds 240 °C, surface oxidation can generate yellow-brown degradation bands and reduce weld-line strength. The extruded profiles are used as bottle-track wear strips, chain guides, and star-wheel friction parts in beverage and pharmaceutical packaging lines. Finished parts are machined from the ram-extruded stock and are covered by FDA 21 CFR 177.1520 when incidental food contact is part of the line specification. Tensile yield stress on machined test bars is typically above 17 MPa according to ISO 527-2, while elongation at break exceeds 300 %. Wear performance is commonly evaluated with a thrust-washer apparatus per ASTM D3702, but production acceptance is usually based on dimensional stability and surface roughness rather than published wear factors for this specific 4050 profile configuration.

    If Paraffin Oil Is Used as a Liquid Porogen in 4050 Separator Film, Extraction Control Determines Gurley Values

    In gel-processed microporous film, the 4050 resin is dispersed in paraffin oil at a mass ratio of 1:4 to 1:6 in a high-shear mixer heated to 180–250 °C. The gel is extruded through a slit die, cooled below the gelation temperature, and biaxially stretched at draw ratios from 5×5 to 7×7. The paraffin oil is then extracted from the oriented film with n-hexane or a chlorinated solvent, leaving a sub-micrometer pore network. Extraction control is the main process gate: residual oil above 1.5 wt% blocks ionic transport and reduces electrolyte uptake, while over-extraction can collapse the oriented tie fibrils and raise the Gurley value beyond acceptable limits. Pore-size distribution is measured by mercury porosimetry per ISO 15901-1, thin-film tensile by ASTM D882, and gas permeability by a Gurley densometer according to TAPPI T460. Terminal use is as a base film for lithium-ion battery separators after optional ceramic coating. Published data for this specific 4050 grade in a 12 µm separator configuration is limited; available industry data for UHMW-PE separator films indicates that porosity below 50 % and Gurley values above 200 s/100 mL are generally unsuitable for high-rate cells. The process is incompatible with screw extrusion without a solvent because the neat polymer cannot be plasticated homogeneously. Separator manufacturers therefore use dedicated gel-extrusion lines with explosion-rated extraction and solvent-recovery systems.

    When 4050 is compression molded into food processing components, the grade must be evaluated for olefin polymer food-contact compliance under FDA 21 CFR 177.1520 and the relevant migration limits of EU Regulation 10/2011. Sheet and block stock is molded at 190–210 °C under 5–10 MPa; pressure is held until the core reaches at least 190 °C, then the platen is cooled at 3–5 K/min to reduce warpage and residual stress. Molded blanks are planed into cutting boards, dough scraper bars, hopper liners, and chain guide rails for bakery and meat processing. Because UHMW-PE absorbs less than 0.01 % water by ISO 62 after 24 h, the components resist swelling during washdown. However, the material should not be exposed to continuous steam above 121 °C because dimensional growth and softening occur even though short-term FDA compliance may extend to hot-fill conditions. The following table summarizes the principal compliance and physical-property checks for food-contact stock.

    CheckStandard or regulationRequirement
    Olefin polymer food-contact statusFDA 21 CFR 177.1520Conforms for use with aqueous and low-alcohol foods up to 121 °C
    Overall migrationEU 10/2011, EN 1186-3<10 mg/dm²
    DensityISO 1183-10.930–0.945 g/cm³
    Water absorptionISO 62<0.01 % after 24 h
    Tensile yield stressISO 527-2>17 MPa on machined test bars

    Suction Box Cover Stock and Dewatering Foil Machining Parameters

    Wet-end dewatering elements machined from 4050 stock require controlled stress-relief annealing because compression-molded sheet retains residual stress near the core. Rough machining is followed by annealing at 100–120 °C for 4–6 h per 25 mm of thickness, then final grinding to flatness within 0.05 mm/m. Carbide-tipped tooling with cutting speeds of 200–500 m/min and light feed rates is used to prevent burr formation and melt smearing on seal surfaces. The material is selected for suction box covers, forming-board blades, deflector strips, and knock-down bars in paper and board machines because it shows low water absorption, good chemical resistance to alum and alkaline cleaning solutions, and a low sliding coefficient against forming fabric. Wear factor is evaluated by thrust-washer method per ASTM D3702; published comparative data for 4050 in paper machine slat configuration is limited, so mill trials usually rank the material against existing high-density polyethylene and ceramic cover stock. Water absorption is checked by ISO 62, tensile modulus by ISO 527-2, and density by ISO 1183-1. The operational boundary for this application is delamination caused by overheated machining: if surface temperature during grinding exceeds 135 °C, localized reflow can seal surface pores and create tensile stress at the machined edge, reducing service life under wet-end vacuum pulses.

    For orthotic and prosthetic socket check devices, 4050 is supplied as compression-molded slab and then CNC-machined because the polymer cannot be injection molded or thermoformed. Molding uses a press temperature of 190–210 °C and pressure of 10–15 MPa, with cooling under load at 3–5 K/min to prevent centerline voids. Rough-machined socket blanks are annealed at 100–120 °C for 4 h before final contouring to stabilize dimensions. The terminal parts are provisional diagnostic sockets, orthotic articulation blocks, and custom adapters used during gait analysis or rehabilitation. Patient-contact evaluation is governed by ISO 10993-5 for cytotoxicity and ISO 10993-10 for sensitization; the 4050 grade should be verified against these standards for each lot if the component will contact skin for more than 30 days. Not all UHMW-PE powder grades carry medical packaging certification or the same residual catalyst profile, so material substitution without requalification is not recommended. The material demonstrates good machining behavior but has a high coefficient of thermal expansion relative to metal inserts; press-fit metal bushings can loosen under temperature cycling from −20 °C to 50 °C if the wall section is below 6 mm. Published data for 4050 in diagnostic socket applications is limited, and design allowables are typically established from molded-slab tensile tests according to ISO 527-2 rather than from injection-molding datasheets.

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    Certification & Compliance
    More Introduction

    Celanese UHMW-PE 4050 is a virgin ultra-high-molecular-weight polyethylene powder grade controlled by viscosity-number methods rather than melt flow. The material is assigned to ISO 11542-1 as an ultra-high-molecular-weight polyethylene moulding and extrusion material. Reported average molecular weight is approximately 5.0 × 10⁶ g/mol when determined by ASTM D4020. The consolidated density is 0.93 g/cm³ under ISO 1183-1, and the as-supplied powder bulk density falls in the range 0.42–0.47 g/cm³ under ASTM D1895. Melt mass-flow rate per ASTM D1238 is not applicable at 190 °C and 21.6 kg because the ultra-high molecular weight suppresses conventional melt flow. Grade control therefore relies on viscosity number, bulk density, particle size distribution, and residual moisture.

    Processing routes for Celanese UHMW-PE 4050 are limited to compression moulding, ram extrusion, and sintering because conventional screw extrusion and thin-wall injection moulding cannot generate the required melt conveying. Production-scale compression presses are used to heat precompacted powder under pressure and then cool the material while constrained to avoid internal void formation. Machined stock shapes produced from this grade are used in wear strips, chain guides, chute liners, conveyor screws, bearing blocks, and guide rails. The 4050 design therefore occupies a middle processing window within the ultra-high-molecular-weight polyethylene family, balancing abrasion resistance and impact toughness against consolidation time.

    Indicative specification values for Celanese UHMW-PE 4050 powder and consolidated stock
    PropertyTest methodIndicative value
    Average molecular weightASTM D40205.0 × 10⁶ g/mol
    DensityISO 1183-10.93 g/cm³
    Bulk densityASTM D18950.42–0.47 g/cm³
    Tensile yield stressISO 527-221 MPa
    Tensile elongation at breakISO 527-2>300 %
    Shore D hardnessISO 86862–64
    Double-notched impact strength at 23 °CISO 11542-1>150 kJ/m²
    Vicat softening temperature A50ISO 30679 °C
    Melting peak temperatureISO 11357-3133 °C
    Water absorption after 24 hISO 62<0.01 %
    Dynamic coefficient of friction against polished steelASTM D18940.10–0.15

    What Distinguishes 4050 from Lower-Molecular-Weight UHMW-PE and HDPE?

    General-purpose HDPE has a molecular weight between 50,000 g/mol and 500,000 g/mol, while Celanese UHMW-PE 4050 contains chains approximately ten to one hundred times longer. This molecular architecture raises the zero-shear viscosity at 190 °C to the order of 10⁸ Pa·s and eliminates measurable melt flow under ASTM D1238. The practical result is a tensile yield stress near 21 MPa and elongation at break above 300 % under ISO 527-2, combined with impact toughness that standard HDPE cannot match. In sliding service, the 4050 grade retains a low coefficient of friction of 0.10–0.15 against polished steel, and its gouging resistance under impact is superior to HDPE liners of equal thickness.

    Compared with lower-molecular-weight injection-moulding UHMW-PE grades in the Celanese portfolio, 4050 is less suited to thin-wall injection moulding but offers higher resistance to flow-induced chain orientation and improved long-term creep resistance. Those lower-molecular-weight products consolidate more easily and may be processed at lower melt pressures, but they typically display lower sand-slurry abrasion resistance. Higher-molecular-weight UHMW-PE grades in the 7.5 × 10⁶–10.5 × 10⁶ g/mol range provide greater abrasion resistance and impact capacity, yet they require longer heating cycles and higher ram pressures and are generally restricted to compression moulding and ram extrusion. Celanese UHMW-PE 4050 therefore occupies the intermediate space where machinable block stock, high abrasion resistance, and acceptable consolidation time must be balanced.

    Comparative positioning of Celanese UHMW-PE 4050 against adjacent polyethylene types
    Material classApproximate molecular weightProcessing routeTypical trade-off
    Celanese UHMW-PE 40505.0 × 10⁶ g/molCompression moulding, ram extrusion, sinteringBalanced toughness, wear resistance, and consolidation time
    Lower-molecular-weight UHMW-PE2.5 × 10⁶–3.5 × 10⁶ g/molInjection moulding, compression mouldingEasier consolidation, lower abrasion resistance
    Higher-molecular-weight UHMW-PE7.5 × 10⁶–10.5 × 10⁶ g/molCompression moulding, ram extrusionMaximum abrasion and impact, longest cycles
    HDPE5 × 10⁴–5 × 10⁵ g/molInjection moulding, extrusion, blow mouldingMelt processability, lower wear and impact toughness

    Compression Moulding, Ram Extrusion and Sintering Process Boundaries

    Compression moulding of Celanese UHMW-PE 4050 is generally conducted at 190–210 °C under 4–10 MPa hydraulic pressure. The heating cycle must allow thermal penetration through the precompacted powder bed. Industrial practice often applies a soak period of 10–15 min/mm of final section thickness, after which cooling under pressure to below 50 °C is used to prevent centreline porosity and dimensional drift. Published grade-specific data for very thick sections is limited, but processing records from production compression presses show that precompaction at 20–30 MPa reduces trapped air and improves fusion-line strength in consolidated billet cores. Oxygen exposure above 220 °C must be avoided because oxidative chain scission produces yellow discoloration and reduced impact strength.

    Ram extrusion is required because the high melt viscosity of 5.0 × 10⁶ g/mol material prevents stable screw conveying. In ram extrusion, powder enters a heated die where a reciprocating piston consolidates and fuses successive charges. Die temperature setpoints typically fall within 180–220 °C, and the part is cooled while constrained to maintain section density. Processing personnel monitor back-pressure, ram speed, and die temperature. A low bulk-density lot can cause charge-weight fluctuation and intermittent fusion lines. Batch-to-batch variation is therefore controlled by incoming powder characterization using ASTM D1895 for bulk density and ASTM D1921 for particle size distribution. In automatic ram extrusion lines, hopper bridging has been observed when the fines fraction below 100 µm exceeds 10 %; pre-screening and dedusting reduce feed interruptions.

    Sintering of porous UHMW-PE components uses controlled heating near the crystalline melting peak of 133 °C measured by ISO 11357-3. The powder is placed in a mould and heated without full consolidation pressure, leaving interconnected porosity for filtration, venting, or wicking. Sintering time depends on the particle size distribution and the desired pore fraction. Overheating beyond 220 °C must be avoided because the melt structure degrades and the finished part loses impact strength. Density checks on sintered blanks are used to confirm the pore fraction because the base polymer density of 0.93 g/cm³ remains unchanged while the apparent part density varies with porosity.

    Powder handling in automatic ram extrusion lines is influenced by bulk density and particle size distribution. When bulk density drops below 0.40 g/cm³, powder feed screws may deliver inconsistent charge weights, and the back-pressure profile in the heated die can shift enough to create visible fusion rings. The recommended receiving procedure includes sieve analysis and bulk density on every lot. Processing logs from compression moulding operations show that a pressing temperature of 200 °C with a hold time of 15 min/25 mm is a common starting point for stock shapes, but thicker sections require a plateau correction to avoid thermal overshoot at the core.

    Post-machining of compression-moulded 4050 stock can be performed on standard metalworking lathes, mills, and routers using sharp carbide inserts, but the material’s high elongation makes chip control difficult. Positive rake angles and adequate chip clearance prevent chip winding. Fabricators often set cutting speeds from 200–500 m/min and feed rates from 0.1–0.3 mm/rev for turning, while allowing for thermal expansion. Tolerances should not be copied unchanged from aluminium or acetal designs because the low moisture absorption is offset by high thermal movement and creep under load.

    Thermal expansion of consolidated UHMW-PE 4050 is approximately 1.5 × 10⁻⁴ K⁻¹ by ISO 11359-2, and thermal conductivity is near 0.4 W/m·K by ASTM C177. These values require clearances in dry bearing service to be larger than metal-to-metal designs. A shaft running in a UHMW-PE bushing can expand the bore enough to close clearance if the assembly approaches 80 °C. Because the material does not dissipate frictional heat quickly, sliding speed and bearing pressure should be evaluated together rather than as independent maxima. Published data for this specific grade under high-speed dry sliding is limited, so trial validation is required beyond generic UHMW-PE design guides.

    In tribological liners, the low sliding friction of UHMW-PE 4050 is typically reported as a dynamic coefficient of friction of 0.10–0.15 against polished steel under ASTM D1894. Abrasive wear under particulate slurry is more sensitive to molecular weight and processing history. Field service in bulk solids handling equipment shows that chute and hopper liners fabricated from this grade resist gouging and cold flow under impact, but the material is not suitable for contact with sharp metallic edges that generate localized surface cutting. Moisture absorption is below 0.01 % by ISO 62 after 24 h immersion at 23 °C, so drying is not mandatory for conventional processing. If condensation has collected on the powder surface, a low-temperature drying step at 80 °C is applied to restore free-flowing behaviour.

    When 4050 Powder Is Selected for Food-Contact or High-Purity Environments

    Compliance must be verified against the specific lot certificate and regulatory declarations. The base ultra-high-molecular-weight polyethylene chemistry is normally covered by FDA 21 CFR 177.1520 for olefin polymers and may meet relevant migration limits under EU Regulation 10/2011, but the presence of additives, processing aids, or surface contaminants requires grade-specific confirmation. The 4050 grade is not automatically a medical-grade or implantable powder; no claim of ISO 5834-1 compliance should be inferred unless explicitly stated in the manufacturer’s certificate. In high-purity chemical service, resistance to aqueous acids, alkalis, and salt solutions is generally retained at ambient temperature, but strong oxidizing acids such as concentrated nitric acid and halogens can cause degradation, especially above 60 °C. Solvent exposure to aromatic hydrocarbons or chlorinated solvents at elevated temperature can plasticize or swell the surface, and continuous load at temperatures approaching 100 °C produces creep that is not acceptable for precision-clearance parts.

    Datasheet Values Are Not Independent of Processing History

    The numerical values listed for Celanese UHMW-PE 4050 are indicative of properly consolidated and machined test specimens. Tensile yield stress measured per ISO 527-2 typically falls near 21 MPa, but insufficient heating or premature pressure release can leave fusion defects that reduce apparent strength without changing the base resin specification. Hardness values of 62–64 Shore D under ISO 868 are used as a quick shop-floor check of consolidation, yet they cannot detect internal voids. Impact testing according to ISO 11542-1 yields double-notched values above 150 kJ/m² for well-fused mouldings; a drop to less than 50 kJ/m² is indicative of incomplete powder fusion or overheating degradation. The melting peak near 133 °C to ISO 11357-3 does not define the upper service temperature; loaded dimensional stability is governed by creep and by the Vicat softening temperature near 79 °C under ISO 306/A50. Incoming powder certification should therefore cover particle size distribution, bulk density, viscosity number, and residual moisture, while finished-part quality control should include fusion testing, density, and tensile or impact specimens from the same consolidation batch.

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