Celanese Uhmw Pe 4212

Celanese UHMW-PE 4212

    • Product Name: Celanese UHMW-PE 4212
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 247615
    Material Type Ultra-high molecular weight polyethylene (UHMW-PE)
    Density 0.93 g/cm3
    Bulk Density 0.45 g/cm3
    Molecular Weight 4.0 x 10^6 g/mol
    Particle Size 120 µm typical
    Tensile Modulus 700 MPa
    Tensile Strength Yield 17 MPa
    Tensile Strength Break 40 MPa
    Elongation At Break >=300%
    Charpy Notched Impact >=100 kJ/m2
    Hardness Shore D 60-65
    Vicat Softening Temperature 80 °C
    Melting Point 130-135 °C
    Crystallinity 50-60%
    Thermal Conductivity 0.42 W/m·K
    Coefficient Linear Thermal Expansion 200 µm/m·°C
    Specific Heat 1.8 kJ/kg·K
    Water Absorption <0.01%
    Coefficient Of Friction 0.15
    Abrasion Resistance Excellent
    Chemical Resistance Good against most chemicals
    Dielectric Constant 2.3
    Volume Resistivity >10^15 ohm·cm
    Dielectric Strength 45 kV/mm

    As an accredited Celanese UHMW-PE 4212 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Celanese UHMW-PE 4212 is typically packaged in 25 kg multi-ply paper bags, palletized and shrink-wrapped for industrial shipping.
    Container Loading (20′ FCL) Celanese UHMW-PE 4212 is palletized and loaded into a 20′ FCL container, properly secured and braced for safe ocean transport.
    Shipping Celanese UHMW-PE 4212 is shipped as a non-hazardous, unregulated solid in moisture-resistant bags, fiber drums, or bulk bags. Keep containers closed, dry, and clean; avoid contamination and excessive heat. It is not assigned a UN number, hazard class, or packing group for transport.
    Storage Store Celanese UHMW-PE 4212 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and strong oxidizing agents. Keep containers tightly closed and protect from moisture, dust, and contamination. Maintain clean, segregated storage at ambient temperature. Avoid dust generation, use appropriate PPE, and follow the supplier’s safety data sheet and local regulations. Do not store near food, feed, or drinking water.
    Shelf Life Celanese UHMW-PE 4212 has an indefinite shelf life when stored sealed in original packaging, cool, dry, and protected from sunlight and contaminants.
    Application of Celanese UHMW-PE 4212

    In the wet-process route for lithium-ion battery separators, ultra-high molar mass polyethylene is compounded with a paraffinic process oil to form a metastable gel that can be extruded through a slit die and subsequently biaxially stretched. The role of UHMW-PE 4212 in this sequence is not that of a conventional melt-processable thermoplastic; it is a gel-former that must retain entanglement density during solvent extraction and heat setting. Industry compliance for separator-grade film includes UL 1642 for cell-level abuse tolerance and IEC 62660-3 for secondary lithium-ion cells used in electric vehicles, while mechanical property acceptance is typically carried out under ASTM D882 for thin-film tensile and ASTM D3763 for puncture resistance. The formulation window for wet-process separator masterbatch falls between 18 wt% and 32 wt% UHMW-PE in a paraffinic oil or decalin/naphthenic oil blend, with a typical operating point of 22 wt% to 25 wt%; antioxidant packages, usually hindered phenols or phosphite blends at 0.1 phr to 0.5 phr, are dispersed into the oil phase before powder introduction. Production-scale equipment uses a co-rotating twin-screw extruder with L/D ratios of 40:1 to 52:1, barrel temperatures between 160 °C and 230 °C, and a melt pump followed by a coat-hanger flat die with a die gap of 0.5 mm to 1.5 mm. After casting onto a chill roll at 20 °C to 40 °C, the gel film undergoes sequential or simultaneous biaxial stretching at draw ratios of 4:1 to 7:1 in the machine direction and 4:1 to 7:1 in the transverse direction. Extraction of the process oil uses methylene chloride or n-hexane in multi-stage countercurrent baths, followed by heat setting at 115 °C to 130 °C under controlled tension. Terminal products include single-layer and ceramic-coated separators for electric vehicle lithium-ion cells, consumer 18650 and 21700 cylindrical cells, and high-rate power cells where a shutdown temperature near 135 °C is required. Operational boundaries include the need to avoid water ingress into the gel compounding zone, because steam pockets in the extruder cause film thickness variation above ±2 µm at line speeds exceeding 30 m/min.

    What Criteria Govern the Gel Spinning of UHMW-PE 4212 into Ballistic-Grade Filaments?

    The selection of a high molar mass polyethylene for gel-spun filament manufacture is governed by the interaction among solution concentration, entanglement density, and spinline drawability. For UHMW-PE 4212, the practical solution concentration in decalin, paraffin oil, or a low-volatility aliphatic solvent ranges from 5 wt% to 12 wt%, with 7 wt% to 9 wt% preferred on continuous lines to balance spinline stability and final filament tenacity. Industry compliance for ballistic end use is normally assessed through NIJ 0101.06 or NIJ 0101.07 body armor test methods, while marine and industrial ropes are qualified under ISO 9554:2019 for fibre ropes and ISO 2307:2019 for breaking load determination. The production line typically consists of a co-rotating twin-screw extruder with L/D 40:1 to 48:1, a melt pump, and a spinneret with conical capillaries of 0.5 mm to 1.0 mm diameter; spinhead temperatures are maintained between 190 °C and 220 °C because the solution phase is shear-sensitive. After extrusion into a water or ethanol quench bath at 5 °C to 15 °C, the gel filaments undergo solvent extraction and hot drawing at draw ratios of 30:1 to 60:1, with intermediate draw stages at 110 °C to 150 °C. The resultant filaments have a denier per filament range of 2 dpf to 10 dpf and are processed into unidirectional ballistic panels, cut-resistant gloves meeting EN 388:2016, winch ropes, offshore mooring lines, and race yacht rigging. The main processing incompatibility is the use of low-boiling solvents such as petroleum ether, which creates filament voids when extraction occurs faster than 2 s per filament bundle; published data for this specific grade in high-speed spinning above 800 m/min is limited.

    Compression molding and ram extrusion impose markedly different pressure histories.

    For monolithic wear stock and machined components, UHMW-PE 4212 is processed without melt-flow methods because the melt viscosity prevents conventional screw injection or single-screw extrusion. Compression molding uses positive-pressure platens with a maximum specific pressure between 10 MPa and 20 MPa, a dwell temperature of 190 °C to 210 °C, and a cooling rate controlled between 5 K/min and 10 K/min to minimize internal voids. Ram extrusion, by contrast, heats a reciprocating piston chamber and a shaping die to separate zones of 180 °C to 200 °C and 140 °C to 160 °C, respectively, with alternating piston strokes of 0.2 m to 0.5 m and back-pressure above 10 MPa. Formulation for industrial wear stock is usually 100 wt% virgin powder, but glass bead or carbon black additions at 0.5 wt% to 2.0 wt% are used where conductive or reduced-creep variants are required; FDA-compliant food-contact components use only virgin olefin polymer under 21 CFR 177.1520 and must avoid recycled material. Industry compliance for stock shapes is covered by ISO 21304-1:2019 for designation and ASTM D4020-18 for specification, while fabricated parts are verified for abrasion resistance under ISO 15527:2022 or ASTM D4060-19. Terminal products include chain guides, star wheels, wear strips, scraper blades, guide rails, conveyor idler sleeves, and pump impellers where the polymer contacts metal surfaces at pressures below its compressive yield of approximately 20 MPa. The operational boundary is dimensional tolerance: ram-extruded round bar above 200 mm diameter often shows centerline porosity if cooling is not staged over at least 24 h, and compression-molded sheet above 60 mm thickness requires preheating at 90 °C to 100 °C before machining to avoid thermal stress cracking.

    Under sintering conditions where inter-particle necking is the primary consolidation mechanism, UHMW-PE 4212 powder is charged into a closed mold without external compaction pressure, heated to 160 °C to 200 °C, and held until adjacent particles form a mechanically coherent porous network. The porosity of the sintered body is controlled by powder particle size distribution and mold fill density rather than by the addition of a blowing agent, although water-soluble salts such as sodium chloride at 30 wt% to 50 wt% can be incorporated as a pore former when larger interconnected channels are required. Compliance for filter elements is traced to ISO 16889:2022 for hydraulic fluid power filter elements, ISO 2941:2009 for collapse and burst resistance, and EC Regulation 1935/2004 for food contact materials when municipal water contact is specified. Production-scale sintering uses forced-convection ovens or oil-jacketed molds with temperature uniformity of ±3 °C across the mold face; cycle times for 25 mm thick plates typically require 3 h to 6 h at dwell plus 2 h to 4 h cooling. Terminal products include porous filter tubes for aggressive chemical filtration, pneumatic silencer elements, air sparging diffusers for wastewater treatment, battery vent membranes, and self-lubricating porous bearings that are later filled with lubricating oil. The main limitation is capillary flow: pore sizes below 10 µm are not reliably produced from standard grade powder without secondary surface treatment, and published data for this specific grade in FDA-regulated potable water components is limited.

    Internal Lubrication and Impact Modification in POM and PA Compounds

    The use of ultra-high molar mass polyethylene as a dispersed minor phase in polyoxymethylene and polyamide compounds alters tribological and impact behavior only when the particle size is reduced below 10 µm and the interface is adequately wetted by the host matrix. For engineering thermoplastic modification, 5 wt% to 15 wt% UHMW-PE 4212 is introduced through twin-screw compounding at barrel temperatures of 180 °C to 220 °C for POM and 240 °C to 270 °C for PA66; the screw configuration must include a high-shear kneading section after the powder feed to avoid agglomerates larger than 50 µm. Industry compliance for automotive and general engineering compounds includes RoHS Directive 2011/65/EU for restricted substances, while mechanical validation uses ISO 527-2:2012 for tensile and ISO 179-1:2010 for notched Charpy impact. Terminal products include interior sliding clips, conveyor chain bushings, gears for office automation, cable drag chain links, and automotive window regulator guides where the addition reduces stick-slip events without the use of migrating external lubricants. The operational boundary is strict: above 15 wt% in POM, molded parts exhibit visible delamination and reduced weld line integrity in ISO 527-2:2012 tensile specimens, and PA66 compounds require predrying at 80 °C for 4 h when stored above 60% RH. This combination is incompatible with high-fluoropolymer processing aids above 0.5 wt%, which can encapsulate the UHMW-PE domains and eliminate the intended wear reduction.

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    Certification & Compliance
    More Introduction

    Celanese UHMW-PE 4212 is an ultra-high-molecular-weight polyethylene homopolymer powder in the GUR resin range. The grade is designed for consolidation by compression moulding, ram extrusion, and sintering, not for conventional melt extrusion or injection moulding. Its viscosity-average molecular weight is approximately 4.4 × 10⁶ g·mol⁻¹ under ASTM D4020 dilute-solution conditions. Moulded density is 0.930 g·cm⁻³ measured according to ISO 1183-1, and as-supplied bulk density is typically 0.42–0.48 g·cm⁻³ under ISO 60. The powder is specified for wear strips, chute liners, porous filter plates, battery separator gel stock, and ram-extruded profiles where low friction and high abrasion resistance are required.

    Because UHMW-PE 4212 does not exhibit measurable melt flow under ISO 1133-1:2022 condition 190 °C/21.6 kg, melt-flow index is not a relevant specification. Processability is instead governed by powder particle size distribution, bulk density, compaction pressure, and dwell time. Lot-level certificates report a median particle diameter in the 120–160 µm range for many industrial applications, although the exact particle-size specification depends on the conversion route and the supplier’s certificate for the purchased lot. Pre-drying is applied when ambient relative humidity exceeds 60 %; residual moisture at 0.05 wt% or higher can generate microvoids in sintered or compression-moulded parts.

    On a production-scale compression moulding line for chute liners, the powder is charged into a hydraulic press with platen force calculated to deliver 20–40 MPa on the projected area. The tool is heated to 200–230 °C and held until the core of the part reaches the fusion temperature. If the core remains below 180 °C for an insufficient dwell period, the centre stays granular and interlaminar shear failures appear during machining. Ejection above 60 °C produces warpage and sink marks on thick sections. These process limits are observed directly on compression presses and are not cosmetic fluctuations; they define the practical lower boundary for full particle fusion.

    How is the powder consolidated without a measurable melt flow index?

    In compression moulding, the powder is charged into a negative-clearance tool and compacted at 20–40 MPa before heating to 200–230 °C. Hold time is typically 10–15 min per 10 mm of final thickness, after which the part is cooled to below 60 °C under pressure. Reducing the pressure too early creates internal voids; holding the part too long at the high-temperature plateau can produce a yellowish edge band from thermo-oxidative degradation. On production-scale ram extruders, barrel temperatures are maintained at 180–210 °C and die temperatures at 190–220 °C. Ram-face pressure, rather than melt pressure, is the controlling variable because no continuous melt is formed. Conventional single-screw extrusion and injection moulding are not suitable for this grade because the high molecular weight prevents melt flow under standard pressures.

    Ram extrusion of UHMW-PE 4212 is carried out on specialized machines with a heated barrel, a high-pressure plunger, and a cooled die. Ram pressure is typically 20–40 MPa, and ram speed is limited to 0.5–2.0 m/h to permit heat transfer into the compacted plug. Increasing ram speed above this range without lengthening the barrel can produce a cold core and poor interparticle fusion. The extrudate is pulled through a calibration sleeve, and surface roughness may track batch-to-batch changes in particle size distribution. These pressure fluctuations at the ram face are a known production fault, not a routine adjustment.

    Porous filtration plates made from 4212 are formed by charging the powder into a shallow mould and applying only enough pressure to establish particle contact, typically 10–20 MPa, before sintering at 180–200 °C. At the lower end of the sintering range, particle necks form while pores remain open; above 200 °C, localised melting collapses the pores and reduces permeability. Temperature uniformity across the platen must therefore be maintained within ±5 °C to prevent low-permeability cold zones and high-shrinkage hot zones. This threshold is critical because only a few degrees separate an open-pore filtration medium from a dense, impermeable sheet.

    Property profile and standard methods

    Table 1 lists typical physical and mechanical values for compression-moulded UHMW-PE 4212. The values are not direct powder specifications; they are measured on fully fused plaques produced under controlled consolidation conditions.

    PropertyMethodTypical value
    Viscosity-average molecular weightASTM D40204.4 × 10⁶ g·mol⁻¹
    Density, moldedISO 1183-10.930 g·cm⁻³
    Bulk densityISO 600.42–0.48 g·cm⁻³
    Tensile yield stressISO 527-222 MPa
    Elongation at breakISO 527-2≥300 %
    Charpy notched impactISO 179-1/1eAno break
    Shore D hardnessISO 86862–64
    Vicat softening point A50ISO 30680 °C
    Melting peakISO 11357-3133 °C
    Water absorption at saturationISO 62<0.01 %
    Volume resistivityIEC 62631-3-1>1 × 10¹⁴ Ω·cm

    Mechanical properties are strongly dependent on consolidation quality. The Charpy no-break result is obtained only on fully fused plaques; incomplete sintering causes shear along particle boundaries and can reduce impact response to a brittle break at ambient temperature. The Vicat softening point of 80 °C and melting peak at 133 °C define the upper short-term thermal envelope. Load-bearing service above this range requires creep testing under ISO 899.

    On a polyolefin separator line, UHMW-PE 4212 is processed by oil plasticization and twin-screw extrusion before extraction. Typical dry-blend formulations contain 60–75 wt% mineral oil and 20–30 wt% fumed silica, and the mixture is extruded at 180–230 °C. After extraction with methylene chloride or n-hexane, the gel film is stretched to create microporosity. The resin particle size distribution and molecular weight influence pore-size uniformity and tortuosity. For sintered filtration discs, the powder is compacted at 20–40 MPa and heated to 180–200 °C to fuse particles without sealing pores. The resulting interconnected pore-size range typically falls between 5 µm and 40 µm depending on powder cut and sintering cycle. Published product-specific permeability data for this exact grade are limited; filtration-grade lots are therefore qualified on a lot-by-lot basis using bubble-point and air-permeability methods.

    Where UHMW-PE 4212 diverges from GUR 4120 and GUR 4150 in wear-sensitive parts

    In portfolio comparisons, the lower viscosity-average molecular weight of UHMW-PE 4212 reduces the interparticle diffusion path and permits lower compaction pressure or shorter hold time than grades specified at 5.0 × 10⁶ g·mol⁻¹ or 9.2 × 10⁶ g·mol⁻¹. In abrasive sand-slurry service, higher-molecular-weight grades such as GUR 4150 generally retain more material under ISO 15527 conditions. The 4.4 × 10⁶ g·mol⁻¹ product provides lower but still substantial abrasion resistance for components with complex porous geometry. Where impact and wear are the only requirements, substitution of 4212 for GUR 4150 should be based on a full-scale wear test because laboratory abrasion data may not capture the effect of consolidated-powder porosity. For surgical implants, the exact grade must be ordered and validated against ASTM F648 or ISO 5834-1; standard industrial lots are not automatically suitable for implantable devices.

    The lower molar mass also shifts the compression-moulding window 5–10 °C lower than GUR 4150 in many production tools, but this does not eliminate long hold times because diffusion coefficients in ultra-high-molecular-weight polyethylene are extremely low. In erosive wear, higher-molecular-weight grades outperform 4212 when hard particles strike the surface at high angle; in three-body abrasion where debris embeds into a porous surface, the ranking may be less consistent. Published product-specific wear factors for 4212 are limited; direct replacement should be validated with the actual slurry composition and service temperature.

    Preventing oxidative degradation and additive incompatibility in continuous processing

    At processing temperatures above 180 °C, thermo-oxidative chain scission becomes kinetically relevant. The as-supplied 4212 powder contains a phenolic stabilizer package; the grade should be protected from oxygen during consolidation at the upper end of the processing window. Production-scale ram extruders are operated with nitrogen purge on the feed hopper when part quality demands low yellowness index, because oxidation at the barrel wall can generate discoloured specks. If the powder is blended with carbon black, graphite, or metallic fillers, the stabilizer demand changes because high-surface-area fillers can adsorb antioxidant. Copper and copper-based fillers are not recommended in humid processing environments unless the compound has been tested by ISO 11357-6 for oxidation induction time at 200 °C. Amine-based stabilizers should be avoided unless compatibility with the base package is confirmed by migration testing; uncontrolled amine additions can cause surface blooming and interfere with particle sintering.

    For porous sintered sheets, part thickness tolerance is directly controlled by the bulk density of the incoming powder. Because bulk density varies between 0.42 and 0.48 g·cm⁻³, a fill height calculated for one lot may produce a different final thickness if the next lot is denser. Manufacturers compensate by weighing the charge rather than filling by volume. Shrinkage during sintering is anisotropic and can be 2–5 % in the compaction direction and 1–2 % perpendicular to it; published shrinkage data for 4212 in porous parts is limited, so tool dimensions must be confirmed on a pilot lot before full production.

    Chemical resistance of UHMW-PE 4212 generally follows that of high-density polyethylene. At 23 °C, retention of tensile properties is high in dilute mineral acids, alkalis, saline solutions, and many polar solvents. Aromatic hydrocarbons, chlorinated solvents, and certain oils cause swelling and may reduce mechanical strength by 10–30 % depending on exposure time and temperature. The grade is not compatible with strong oxidizing acids at elevated temperature. For chemical service, testing under ISO 175 is recommended when the fluid is not represented in standard resistance tables. Continuous service for unfilled 4212 parts should be limited to 80 °C under significant load; concentrated nitric acid, fuming sulfuric acid, and halogens at elevated temperature cause chain degradation. For food-contact and potable-water applications, the exact grade and lot must be confirmed against the relevant regulatory clearance, and for implantable components, ASTM F648 or ISO 5834-1 compliance must be specified at the purchase order stage.

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