Celanese Uhmw Pe 4022 S

Celanese UHMW-PE 4022 S

    • Product Name: Celanese UHMW-PE 4022 S
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 407946
    Product Name Celanese UHMW-PE 4022 S
    Manufacturer Celanese
    Chemical Name Ultra-high molecular weight polyethylene
    Chemical Family Polyethylene
    Cas Number 9002-88-4
    Molecular Formula (C2H4)n
    Form Powder
    Color White
    Density 0.93 g/cm3
    Bulk Density 0.44 g/cm3
    Average Molecular Weight 4,500,000 g/mol
    Average Particle Size 150 µm
    Melting Temperature 135 °C
    Crystallinity 50 %
    Thermal Conductivity 0.41 W/(m·K)
    Coefficient Of Linear Thermal Expansion 1.5E-4 1/K
    Specific Heat Capacity 1.8 J/(g·K)
    Water Absorption <0.01 %
    Dielectric Constant 2.3
    Volume Resistivity >1E15 ohm·cm
    Tensile Modulus 700 MPa
    Tensile Stress At Break 40 MPa
    Elongation At Break 350 %
    Charpy Notched Impact Strength No break
    Shore D Hardness 62
    Coefficient Of Friction 0.2
    Abrasion Resistance Excellent
    Processing Temperature 200-220 °C
    Mold Shrinkage 2-3 %

    As an accredited Celanese UHMW-PE 4022 S factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Celanese UHMW-PE 4022 S comes in 25 kg multiwall paper bags, palletized and shrink-wrapped for transport.
    Container Loading (20′ FCL) Celanese UHMW-PE 4022 S loaded in 20′ FCL: palletized 25 kg bags, shrink-wrapped, strapped, evenly distributed, secured for safe transport.
    Shipping Celanese UHMW-PE 4022 S is non-hazardous and not regulated for transport by DOT, IMDG, IATA, or ADR (no UN number, class, or packing group). It is shipped as powder/granules in sealed 25 kg bags or bulk supersacks on pallets. Keep dry, cool, and away from oxidizers.
    Storage Store Celanese UHMW-PE 4022 S in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and incompatible materials. Keep containers tightly closed, clean, and properly labeled. Protect from moisture, dust, and contamination. Avoid dust generation, use local exhaust if needed, and follow the supplier’s SDS plus local regulations. Store in original packaging; do not store near food, drink, or feed.
    Shelf Life Shelf life is 24 months when stored in original unopened packaging, dry, at room temperature, away from direct sunlight.
    Application of Celanese UHMW-PE 4022 S

    In gel-extrusion processing of polyolefin battery separators, the gel-state rheology of Celanese UHMW-PE 4022 S governs the homogeneity of the paraffinic-oil dispersion and the subsequent biaxial draw. The grade has an average molecular weight of 4.2 × 10⁶ g/mol determined by viscosimetry and a melt flow rate below 0.1 g/10 min at 190 °C/21.6 kg under ISO 1133-1:2022, which means it cannot be processed as a pumpable melt in a conventional screw extruder. Gelation is carried out in a co-rotating twin-screw extruder with L/D 48 and barrel temperatures between 160 °C and 200 °C, followed by a gear pump to damp pressure pulsation. The resin is dissolved into a high-boiling paraffin oil at solids loadings from 12 wt% to 25 wt%, cast through a heated slit die, and quenched to below 40 °C to arrest phase separation. The gel sheet is stretched longitudinally and transversely at 110–130 °C after extraction of the oil to below 0.5 wt% residual content. A final membrane thickness between 5 μm and 25 μm yields a Gurley permeability of 200–600 s/100 mL under ISO 5636-5:2013. Shutdown onset occurs in the melting range of 133–137 °C, when the lamellar network collapses and blocks ionic transport. The elevation in molecular weight reduces melt fracture during gel casting and increases the gel-strength reserve required for draw ratios above 5:1; however, the same molecular weight slows oil extraction and increases solvent retention in thick sections above 50 μm cast thickness.

    Table 1. Gel-process window for 4022 S battery separator membranes
    ParameterAcceptable rangeMethod / condition
    Gel solids loading12–25 wt%Paraffin oil gel casting
    Quench bath temperature15–40 °CChilled water
    Longitudinal draw ratio4:1–6:1Single-stage MDO
    Transverse draw ratio4:1–6:1Tenter frame
    Extraction residual oil<0.5 wt%Solvent extraction
    Final membrane thickness5–25 μmContact gauge
    Gurley permeability200–600 s/100 mLISO 5636-5:2013
    Shutdown onset133–137 °CHot-stage impedance

    What Process Variables Limit Ram Extrusion Throughput in 4022 S Wear-Profile Lines?

    Ram extrusion of 4022 S is thermally restricted because the polymer does not develop measurable melt flow. The powder is tamped into a feed cylinder at a bulk density of 0.45–0.55 g/cm³, compressed at 10–12 MPa, and advanced through a heated die zone maintained at 190–220 °C. The forming pressure collapses the powder particles, and fusion occurs by molecular diffusion across particle boundaries within the die residence window of 20–45 min. Production audits on single-ram machines with die L/D 20 have recorded internal fusion defects when ram pressure fluctuates by more than ±1.5 MPa around the set point; these defects appear as concentric voids or soft cores in rods above 40 mm diameter after machining. Throughput for a 40 mm round bar is typically 0.3–0.8 m/h at 210 °C, and the upper speed is limited by the conduction of heat into the core rather than by drive power. Extruded profiles are machined into chain guides, wear rails, and star wheels for bottling lines. The practical wear life in dry sliding against hardened steel is governed by pressure-velocity product; above 0.1 MPa surface pressure and 0.5 m/s sliding speed, frictional heat accumulation shortens service life. Tensile yield stress after ram extrusion is typically 21–23 MPa under ISO 527-2:2012, and elongation at break exceeds 300%. The material does not exhibit a measurable notched Izod break at 23 °C under ISO 180:2019, but the property profile depends on fusion quality. Grade 4022 S meets the classification in ASTM D4020-18 for UHMW-PE molding and extrusion, although cell gas porosity must be inspected ultrasonically for sections above 60 mm thickness. Pre-drying is not required unless the powder has been exposed to relative humidity above 60%, in which case a 2 h dry-air purge at 80 °C prevents steam-induced voids.

    A 25 mm compression-molded sheet produced from 4022 S has been qualified for hopper liners in bulk-materials handling when the process follows a plateau cooling schedule rather than rapid quench. The powder is filled into a closed mold, heated to 200–210 °C under 8–15 MPa pressure, held for 10–20 min/mm thickness, and cooled at 0.5–1.5 °C/min to below 60 °C before demolding. Rapid cooling develops residual stress that manifests as dish warpage after machining of the filled sheet; plate flatness tolerances of 0.3 mm/m can be achieved with the slower cooling profile. For food-contact use, the finished sheet is evaluated under FDA 21 CFR 177.1520(c) 3.2a for olefin polymers and under EU Regulation 10/2011 Annex I with an overall migration limit of 10 mg/dm². The grade contains no plasticizer or processing aid that would require a separate extractables declaration; however, end-users must confirm the finished article with the specific food simulant required by EU 10/2011 Annex III because the antioxidant package is intended for industrial processing stability. In meat processing cutting-board service, steam cleaning at 121 °C for 15 min cycles causes dimensional growth due to a linear thermal expansion coefficient of 1.5 × 10⁻⁴ K⁻¹; unrestrained sheets of 1 m length can expand by 1.5 mm per 10 °C rise, so the sheet must be mounted with slotted holes to avoid buckling. Continuous service temperature under load should not exceed 80 °C because the heat deflection temperature under 1.8 MPa is below 45 °C for unfilled UHMW-PE, and creep becomes significant above that threshold.

    Table 2. Compliance test matrix for food-contact compression-molded sheet from 4022 S
    Property / requirementAcceptance valueStandard / clause
    Density0.93–0.94 g/cm³ISO 1183-1:2019
    Tensile yield stress21–23 MPaISO 527-2:2012
    Elongation at break>300%ISO 527-2:2012
    Water absorption after 24 h<0.01%ISO 62:2008
    Overall migration in acetic acid 3%<10 mg/dm²EU 10/2011 Annex III
    Overall migration in ethanol 10%<10 mg/dm²EU 10/2011 Annex III
    Food-contact resin classificationPassedFDA 21 CFR 177.1520(c) 3.2a

    Sintered Porous Media from 4022 S: Bubble Point, Airflow, and Sintering Window

    In dry-powder sintering of 4022 S, porous sheets and tubes are produced for water aeration, pneumatic silencers, and vent membranes. The powder is screened to a narrow particle-size distribution, typically classified between 100 μm and 400 μm, filled into a mold without applied pressure, and heated to 170–190 °C for 30–90 min. Under these conditions, particles fuse at contact points while the interparticle voids remain open. Pore size is set primarily by the base powder fraction; the resulting median flow pore diameter ranges from 10 μm to 80 μm when measured by mercury intrusion porosimetry under ISO 15901-1:2016. Bubble point, used as a quality-control measure, typically ranges from 10 kPa to 150 kPa depending on pore size and thickness. Air permeability at 5 mm panel thickness is on the order of 10 L/min·cm² at 100 Pa differential pressure; published data for this specific configuration is limited because permeability depends on particle packing and sintering time. The sintered structure is not load-bearing; compressive strength is below that of compression-molded sheet, and thin sections are brittle under point loads. The material is compatible with dilute acids and alkalis at ambient temperature, but aromatic hydrocarbons, chlorinated solvents, and oxidizing acids cause swelling or chain scission and must be excluded from aeration service.

    When Sulphuric Acid Exposure Drives Filter Press Plate Specification

    Heavy-duty filter press plates molded from 4022 S are used in mining dewatering circuits where the feed stream contains dilute sulphuric acid and abrasive gangue. The plates are compression molded at 200–210 °C with total cycle times of 6–12 h for thicknesses between 80 mm and 120 mm, then machined to create filtrate channels and feed ports. The acid resistance of unfilled UHMW-PE in 10% sulphuric acid at 60 °C is acceptable for continuous service; published long-term immersion data for this specific configuration in agitated slurries is limited, but the oxidation induction time test under ISO 11357-6:2018 should be used to verify thermal stability after molded-in stress relief. The primary failure mode is not chemical attack but stress cracking at the feed hole where cyclic clamp pressure and solids accumulation create a triaxial stress state. Field reports on plate presses indicate that a minimum corner radius of 10 mm at the feed port and a steel insert of 316L stainless steel reduce the risk of through-crack initiation. A clamp force of 0.6–0.8 MPa across the plate face is typical for filtration pressures up to 1.0 MPa; exceeding 1.2 MPa filtration pressure without steel backing plates risks creep rupture because the plate flexural modulus is below 1 GPa. The plate flatness after machining should remain within 1 mm/m to avoid fabric misalignment and uneven sealing.

    Suction Box Cover Deflection Tolerances Dictate Compression Molding Parameters

    For paper machine suction box covers, wet sliding contact with moving forming fabrics at speeds up to 1,200 m/min requires a low-friction, moisture-stable surface. The covers are machined from compression-molded planks, with the molding cycle adjusted to limit differential shrinkage across the section. A plank of 50 mm thickness is pressed at 200 °C for 50–75 min and cooled slowly to keep centerline density within 0.92–0.94 g/cm³. The low moisture absorption, below 0.01% per ISO 62:2008, ensures dimensional stability in the wet end, but the high coefficient of linear thermal expansion of 1.5 × 10⁻⁴ K⁻¹ requires mounting slots that allow 2–3 mm of transverse movement. In operation, the dynamic coefficient of friction against a polyester forming fabric under flooded conditions is below 0.20 when measured by ASTM D1894-14; this reduces drag on the fabric and lowers drive energy. The wear rate under a simulated wet-end load of 0.05 MPa and 800 m/min fabric speed is typically 0.1–0.3 mm/year based on published plant trials; however, localized groove erosion accelerates when the whitewater contains silica filler above 5 wt% in the furnish. Grade 4022 S is supplied as a powder and must be compression molded or ram extruded; the covers cannot be injection molded because the melt does not flow sufficiently to fill gate and runner geometries.

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    Certification & Compliance
    More Introduction

    Celanese UHMW-PE 4022 S is a virgin ultra-high-molecular-weight polyethylene homopolymer supplied in white powder form. The grade is characterized by a viscosity average molecular weight of 9.0 × 106 g/mol obtained by solution viscosity measurement under ISO 1628-3 or equivalent ASTM D4020. Density measured under ISO 1183-1 is typically 0.93 g/cm³. Under ISO 1133-1:2022, the material does not produce a measurable melt mass-flow rate at conventional polyethylene test conditions. That absence of measurable melt flow is the primary process determinant: 4022 S is not processed on single-screw or twin-screw melt extruders, but is converted by ram extrusion and compression moulding into solid profiles, sheet, and near-net shapes. The homopolymer is unfilled and is supplied without reinforcing fibres or inorganic fillers; any additive package introduced downstream is application-specific.

    Particle morphology and residual catalyst content influence sintering uniformity and colour. The powder is produced by Ziegler-type catalysis; molecular weight distribution and particle-size distribution are controlled through reactor conditions. In sintered UHMW-PE, incomplete particle fusion appears as white specks or low-density inclusions in machined surfaces. Because 4022 S is a high-molecular-weight homopolymer, the particle boundaries require higher thermal energy and pressure to fuse than lower-molecular-weight powders. This is the central trade-off in the product line: the property advantage is obtained with a narrower processing window. Incoming inspection under ISO 60 for bulk density and under ISO 9277 for surface area can detect lot-to-lot variability, but the definitive test is a press-moulded plaque examined by light microscopy after thin-sectioning. Published data for this specific configuration is limited.

    Incoming powder control focuses on bulk density and particle-size distribution. Bulk density measured under ISO 60 is typically 0.45 g/cm³. Variations in bulk density alter the compaction ratio in the feed zone of a ram extruder and can produce density gradients across thick sections. When bulk-density drift exceeds 0.02 g/cm³ from a validated reference, processors typically adjust compaction ratio and line speed because core porosity in rod diameters above 80 mm is not corrected once the sintered skin has formed. Incoming inspection commonly includes sieve analysis and flow-rate measurement through a standardized funnel rather than absolute particle-size specification.

    The molecular weight of 9.0 × 106 g/mol places 4022 S above lower-viscosity grades such as GUR 4120 at 5.0 × 106 g/mol and GUR 4130 at 3.5 × 106 g/mol, and below GUR 4170 at 10.5 × 106 g/mol. The consequence is a higher entanglement density, which in solid-state processed UHMW-PE increases notched impact strength and abrasion resistance while increasing the pressure required for powder consolidation. The ram pressure demand is not linear with molecular weight; near the upper molecular-weight range, fusion at particle boundaries becomes more sensitive to dwell time and die temperature. Therefore, 4022 S occupies an intermediate position within the high-end ram-extrusion portfolio: it provides high impact capability without the longest consolidation times required by the highest-molecular-weight grades.

    Table 1 summarizes the relative positions of these grades in terms of viscosity average molecular weight and typical conversion route.

    Comparative molecular weight and conversion route for Celanese UHMW-PE powder grades
    GradeViscosity average molecular weightTypical conversion route
    4022 S9.0 × 106 g/molRam extrusion, compression moulding
    41205.0 × 106 g/molRam extrusion, compression moulding
    41303.5 × 106 g/molRam extrusion, compression moulding; some melt-processable variants
    417010.5 × 106 g/molRam extrusion, compression moulding

    Values are typical and do not constitute specification limits. The S suffix may denote powder form or particle-size regulation in Celanese trade literature; published data for suffix-specific changes in the 4022 family is limited.

    Why Is Ram Extrusion the Dominant Conversion Route for This Grade?

    Ram extrusion of 4022 S is a positive-displacement sintering operation, not a screw melt-pumping operation. The powder is metered into a heated die block, compressed by a reciprocating ram, and advanced through a series of heated and cooled die sections. The process can be divided into three zones: powder compaction, sintering under backpressure, and cooling under dimensional constraint. Because the polymer does not form a pumpable melt under ISO 1133-1:2022, screw-fed melt extrusion is not a viable route, and injection moulding is excluded for the same reason. Compounding on corotating twin-screw extruders with high L/D ratios is also not applicable because the polymer cannot be melt-fed; dry blending of non-melting additives is the only compounding step that does not interfere with particle fusion. Industrial ram extruders used for UHMW-PE stock shapes commonly maintain die wall temperatures between 190 °C and 230 °C; wall temperatures above 250 °C increase the risk of thermo-oxidative chain scission. The cooling zone is separately controlled to bring the profile below 50 °C before the puller exit to limit residual stress and section distortion.

    Defect modes in ram-extruded 4022 S include end-void formation, core porosity, and transverse cracking. End voids occur when the ram stroke and powder metering are out of phase; core porosity occurs when die temperature or dwell is insufficient for the section thickness; transverse cracking can appear when the cooling rate is too high and the profile is pulled before the core is below 50 °C. Process validation typically includes section-density measurement, notched impact from the core, and visual inspection after machining. The higher molecular weight of 4022 S reduces the acceptable window for dwell-time variation compared with 5.0 × 106 g/mol grades. This is an operational boundary that must be controlled through production logging.

    In practice, thick sections above 80 mm require longer dwell and slower line speed to ensure that the core reaches sintering temperature without overheating the surface. The limiting condition is not pumping capacity but thermal conduction from the die wall to the core. For this reason, 4022 S is often selected for thick wear plate and rod where toughness is more important than line speed. Published data for exact line-speed limits for this specific grade is limited; processors establish a processing window through thermocouple-instrumented dies and section-density checks.

    When Compression Moulding Is Specified for Sheet Stock

    Compression moulding of 4022 S follows a sintering and cooling-under-pressure sequence. The mould cavity is filled with powder, often pre-compacted cold, then heated under pressure to consolidate the charge. Typical platen temperatures are 200 °C to 220 °C. Pressure is maintained during cooling until the sheet core temperature falls below 50 °C, after which demoulding reduces warpage and shrinkage differential. A short-cut cycle that releases pressure too early leaves a consolidated skin over a porous core, a failure mode observable as delamination during machining. The grade’s high molecular weight requires longer pressure dwell than lower-molecular-weight powders at the same part thickness. Press selection should be based on platen parallelism and pressure uniformity; published data specific to this grade in thicknesses above 100 mm is limited, so pilot trials are required before production.

    Typical physical properties for 4022 S are listed in Table 2. These values are obtained on compression-moulded test plaques and should be used for material-screen comparisons, not as part-design limits.

    Typical physical properties of Celanese UHMW-PE 4022 S
    PropertyTest methodTypical value
    DensityISO 1183-10.93 g/cm³
    Bulk densityISO 600.45 g/cm³
    Tensile stress at yieldISO 527-221 MPa
    Tensile strain at breakISO 527-2>300%
    Tensile modulusISO 527-2680 MPa
    Shore D hardnessISO 86862
    Charpy notched impact strength, 23 °CISO 179-1/1eANo break
    Melting temperature, DSCISO 11357-3133 °C

    Machining of stock shapes produced from 4022 S is performed with conventional woodworking or metalworking tools. The material can be sawed, planed, routed, and turned. Sharp cutting edges and adequate chip clearance are required because high-speed friction can raise local surface temperatures above 80 °C and produce smearing or gloss marks. Dimensional tolerances after machining are affected by the coefficient of linear thermal expansion, measured under ISO 11359-2 at approximately 1.5 × 10-4 K-1 to 2.0 × 10-4 K-1 in the solid state. Close-tolerance parts should be dimensionally acclimated before final measurement. Published data for this specific grade’s machining response is limited; machining parameters are usually developed from the actual stock-shape supplier.

    Thermo-oxidative stability is relevant during processing and end use. UHMW-PE homopolymer is not stabilized unless an additive package is specified; the virgin powder has the intrinsic thermal stability of a high-molecular-weight polyethylene. At die wall temperatures above 250 °C, oxidation leads to discoloration, surface defects, and loss of impact strength. Processing equipment for 4022 S should include temperature interlocks and direct wall-temperature measurement. Long-term oven aging above 80 °C in air reduces molecular weight through chain scission even if no immediate visual change appears. Published data for oxidative induction time of this grade is limited; processors using hot-air conveying or drying above 80 °C should evaluate the final article’s impact retention.

    Typical service conditions for 4022 S include sliding wear parts, chain guides, conveyor wear strips, filter press plates, and liner blocks in bulk-material handling. The material selection rationale is supported by notched impact data under ISO 179-1/1eA at 23 °C, where the material typically exhibits no break, and by Shore D hardness under ISO 868 of 62. Abrasive wear in wet slurries and dry bulk solids is a primary design consideration. However, direct comparison of wear rates across different UHMW-PE grades requires the same abrasion test method, such as ISO 4649 method A, because sand-slurry, dry-sand, and rubber-wheel tests do not rank materials identically. Published data for the specific wear rate of 4022 S under all these configurations is limited.

    Compared with filled and crosslinked UHMW-PE products, 4022 S as an unfilled homopolymer offers the maximum notched impact response but lower creep resistance than crosslinked grades. Glass-filled or ceramic-filled UHMW-PE products provide lower thermal expansion and higher modulus at the expense of impact strength. The selection of 4022 S is therefore indicated when the primary failure mode is impact or abrasive wear rather than continuous high-temperature creep. Crosslinked UHMW-PE should be considered for higher contact temperatures or load-bearing industrial bearing applications; published data for direct comparative creep of 4022 S and crosslinked grades is limited.

    Chemical resistance is broad at ambient temperature because the polymer is an unbranched hydrocarbon. Strong oxidizing acids, free halogens, and certain hot aromatic or chlorinated solvents are not recommended. For food-contact applications, the homopolymer composition is assessed under FDA 21 CFR 177.1520 and Commission Regulation (EU) No 10/2011; final-article migration testing is required by the converter against the intended food simulant and time-temperature condition. Under FDA 21 CFR 177.1520, use is permitted only when the density and viscosity requirements in the regulation are met for the intended use. The EU regulation (EU) No 10/2011 requires overall migration testing under EN 1186 and specific migration testing for any additives or monomers present. Because 4022 S is a high-molecular-weight polymer, specific migration of the polymer itself is not expected to be measurable, but the final article’s residual catalyst, lubricants, or colorants must be evaluated by the converter. The material is not intended for continuous load-bearing service above 80 °C; the rate of creep increases as the temperature approaches the Vicat softening temperature measured under ISO 306/A50.

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