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Celanese GUR UHMWPE 4122-5

    • Product Name: Celanese GUR UHMWPE 4122-5
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales8@sinochem-nanjing.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 816167
    Polymer Type Ultra-high molecular weight polyethylene (UHMWPE)
    Water Absorption Percent <0.01
    Volume Resistivity Ohm Cm >1e15

    As an accredited Celanese GUR UHMWPE 4122-5 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Celanese GUR UHMWPE 4122-5 is supplied as powder in 25 kg paper bags, typically 40 bags (1,000 kg) per pallet.
    Container Loading (20′ FCL) A 20′ FCL container loaded with palletized 25 kg bags of Celanese GUR UHMWPE 4122-5 powder, securely stowed for ocean freight.
    Shipping Celanese GUR UHMWPE 4122-5 is shipped as a non-hazardous, non-regulated polymer powder. Use clean, dry, sealed packaging and protect from moisture, contamination, and excessive heat. No UN number, hazard class, or special transport label is required under normal shipping regulations.
    Storage Store Celanese GUR UHMWPE 4122-5 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and strong oxidizing agents. Keep containers tightly closed to prevent moisture and dust contamination. Maintain good housekeeping to avoid dust accumulation; ground and bond equipment if handling powder. Follow local regulations and the SDS.
    Shelf Life Celanese GUR UHMWPE 4122-5 has a two-year shelf life when stored unopened below 30°C, away from moisture and UV light.
    Application of Celanese GUR UHMWPE 4122-5

    For implantable load-bearing applications, compression-moulded slabs of Celanese GUR UHMWPE 4122-5 are typically consolidated from powder having a bulk density in the range 0.40–0.48 g/cm³ per ASTM D1895 Method A. Because the material has no measurable melt-flow index under ISO 1133-1, viscosity number measured by ISO 1628-3 is used for batch release. Oxygen-free moulding requires applying 7–14 MPa at platen temperatures between 195°C and 220°C, held for 15–30 min per 25 mm of slab thickness; the cooling rate from the melt plateau to below 80°C is controlled at 0.1–0.5°C/min to avoid internal microvoids and excessive crystallinity gradients. Consolidation quality is assessed by density measurements under ISO 1183-1 and by tensile testing of machined specimens under ISO 527-2, with typical yield strength values of 17–24 MPa and elongation at break above 300%. Powder heated without inert gas coverage is sensitive to oxidation; oxidation index measured by ASTM F2102 should remain below 0.10 for implant-grade material before gamma sterilization. Direct compression moulding of near-net-shape tibial inserts and acetabular liners from 4122-5 reduces machining loss compared with slab stock, but mould-filling density gradients can generate anisotropic shrinkage of 1–3% between the ram face and the cavity perimeter.

    The processing window for unmodified 4122-5 lies between incomplete consolidation at temperatures below 190°C and thermo-oxidative degradation above 240°C. In thick slabs, the centre temperature can lag the platen temperature by 20–40°C depending on powder bulk density and press force; if the dwell time is shortened, the centre remains opaque and fails to reach ISO 5834-2 density requirements. If the dwell time is extended, the skin oxidizes and the oxidation index measured under ASTM F2102 may exceed 0.10. This thermal window requires multi-zone platens with independent PID control and cartridge heaters spaced no more than 100 mm apart. Mould release agents must be selected carefully; zinc stearate is commonly used for industrial UHMWPE but is not acceptable for implantable applications because it creates inorganic residue detectable by inductively coupled plasma mass spectrometry. Vacuum or nitrogen purging of the mould cavity before heating is used in production-scale compression moulding, but published data for 4122-5 in this specific process configuration is limited.

    Gamma irradiation at 25–40 kGy induces free radicals that participate in crosslinking; subsequent annealing or remelting reduces residual radical concentration but alters crystalline content. Wear is frequently evaluated under ISO 14242-1 or ASTM F732; volumetric wear rates for highly crosslinked UHMWPE of similar molecular weight may fall below 10 mm³/10⁶ cycles, but published data for this specific grade in a crosslinked configuration is limited. The powder must not be blended with calcium stearate or other metallic stearates for implantable applications because these additives alter oxidation behaviour; ISO 5834-2 governs raw-material traceability, ash content, and packaging. Ram-extruded or compression-moulded forms intended for implant use require ultrasonic C-scan inspection with a 5 MHz transducer and should be free of visible fusion defects.

    Property or testMethodTypical acceptance window
    Bulk densityASTM D1895 Method A0.40–0.48 g/cm³
    Tensile yield strengthISO 527-217–24 MPa
    Elongation at breakISO 527-2>300%
    Oxidation indexASTM F2102<0.10
    Volumetric wear rate, crosslinked formulationASTM F732 / ISO 14242-1<10 mm³/10⁶ cycles

    What Controls Dimensional Stability in Ram-Extruded 4122-5 Wear Profiles?

    In ram extrusion of GUR 4122-5, machines rated from 50 kN to 1.5 MN ram force are used, with die temperatures held between 190°C and 240°C. Because the material has no measurable melt-flow index under ISO 1133-1, screw plasticisation is replaced by repeated cold-powder compaction followed by axial displacement through a heated die; the cycle length must be adjusted so that the powder plug reaches full gelation before each stroke. If the stroke length is too long, cold cores remain in the section and air-entrapment defects appear as radial white lines after machining. If the stroke length is too short, residence time at temperature increases and oxidative chain scission reduces tensile toughness. Typical line speeds for solid rods of 20–80 mm diameter range from 0.05–0.20 m/min, depending on die cross-section and temperature profile. Dimensional tolerance after annealing at 80–100°C for 24 h is usually held within ±0.5% of nominal diameter; water-cooling directly after the die is avoided because it generates skin-core stress differentials that cause bowing.

    Wear strips and chain guides cut from these profiles are specified for dry sliding against stainless steel, with dynamic coefficients of friction typically 0.10–0.22 at surface pressures below 5 MPa according to pin-on-disc tests under ASTM G99. Abrasion resistance in sand-slurry testing under ASTM G65 Procedure A often shows volume loss below 4 mm³ for unmodified UHMWPE; specific values depend on counterface hardness and sliding velocity. The material should not be welded using hot-gas techniques because the extremely high melt viscosity prevents interdiffusion; mechanical fastening or dovetail slotting is used. Processing conditions above 260°C should be avoided because degradation accelerates and oxidative breakdown produces measurable changes in molecular weight distribution.

    Gel-Spun Fibre Lines for Ballistic and Maritime Load Paths

    Where solution spinning of GUR 4122-5 is required, the powder is dispersed in high-boiling spin solvents such as decalin or white mineral oil at concentrations between 7 wt% and 12 wt%; dissolution is completed in a twin-screw extruder at 150–180°C under nitrogen. The spin-head and spinneret are maintained above the crystallization temperature; as-spun filaments are quenched in a water bath at 10–30°C and then extracted and hot-drawn in two or three stages to total draw ratios above 30:1. Fibre tenacity measured on conditioned specimens per ASTM D885 is typically 3.0–3.9 GPa, with tensile modulus of 90–150 GPa; yarn count, twist, and finish level must be reported with any ballistic package test. Cut-resistant gloves knitted from fibres of this chemistry are evaluated under EN 388:2016; the blade cut resistance level depends on yarn linear density and coating, so the base resin alone does not determine the final glove rating.

    Maritime ropes and slings require a different balance of strength retention and creep. Long-term creep data under ASTM D885 non-accelerated conditions are necessary because published short-term tensile data for this specific grade in gel-spun form is limited. The high solution viscosity of 4122-5 may reduce inline filter service life and increase spin-pack pressure compared with lower-molecular-weight fibre grades; hardened spinneret capillaries should be specified and higher solvent recovery energy per kilogram of filament should be expected. Processing must exclude oxygen at all heated stages because thermo-oxidative chain scission reduces draw compatibility and lowers final tenacity. Residual solvent below 50 ppm is typically required for food-contact or medical fibre uses and is confirmed by gas chromatography.

    Because microporous separator films use a gel-casting route, 4122-5 powder is mixed with paraffin oil at a polymer concentration of 20–30 wt% in a co-rotating twin-screw extruder with a length-to-diameter ratio of 40:1 or greater; the extruder barrel is set in multiple zones from 160°C to 230°C. The cast gel sheet is cooled on a chill roll, biaxially stretched at draw ratios of 5×5 to 7×7 in a sequential stenter, and the process oil is extracted with methylene chloride or n-hexane. The resulting pore structure is evaluated by mercury intrusion porosimetry under ISO 15901-1, with typical mean pore diameters between 0.03 µm and 0.10 µm, and by Gurley air permeability under ASTM D726, with values from 200 s/100 mL to 600 s/100 mL. Thermal shutdown behaviour is a critical separator requirement; UHMWPE membranes can exhibit a rapid impedance rise near 130–135°C, but shutdown temperature and membrane rupture point must be validated on the target cell chemistry because electrolyte plasticisation shifts thermal transitions.

    Electrochemical performance is assessed by constructing coin cells with lithium-ion electrodes and measuring ionic conductivity after soaking in 1 M LiPF₆ in ethylene carbonate/dimethyl carbonate; comparative data for this specific grade in separator configuration is not widely published, so pilot trials are required before production specification. The ultra-high molecular weight of 4122-5 raises extensional viscosity during gel casting, which can reduce line speed relative to lower-viscosity UHMWPE separator grades and increase polymer filter screen changes. The material must not contain metallic impurities above 5 ppm total ash because residual catalyst residues can promote lithium dendritic growth; ash content per ISO 3451-1 and trace metal analysis by inductively coupled plasma should be specified.

    Separator propertyTest or process methodReported window
    Polymer concentration in gelIn-process gravimetric20–30 wt%
    Mean pore diameterISO 15901-10.03–0.10 µm
    Gurley air permeabilityASTM D726200–600 s/100 mL
    Biaxial draw ratioSequential stenter5×5 to 7×7
    Total ashISO 3451-1<5 ppm

    When Powder-Sintered Porosity Must Be Controlled Below 100 µm

    For sintered porous parts, gravity filling or vibration-assisted filling of 4122-5 powder into moulds is used before heating to 250–280°C without applied compaction; this allows particle neck formation while retaining interparticle voids. Pore size distribution is controlled primarily by the powder fraction cut, so sieving to remove particles below 50 µm or above 300 µm before filling is necessary for reproducible filtration media. Porosity measured by ISO 2738 can be adjusted between 30% and 45%; bubble-point testing under ISO 4003 provides the first bubble point for pore-size validation, and mercury intrusion porosimetry under ISO 15901-1 gives the full distribution. Air permeability for sintered UHMWPE of 35% porosity is often in the range 10–50 L/min/dm² at 200 Pa, but this range shifts with thickness and surface skin formation.

    Chemical resistance of the sintered component follows the base polymer; the material is resistant to dilute acids and alkalis at ambient temperature but swells in hot aromatic and chlorinated solvents. Filtration elements should not be steam-sterilized above 121°C because sintered UHMWPE loses dimensional stability and can densify under repeated autoclave cycling; 10–30% shrinkage may occur after the first autoclave cycle if the part was not pre-annealed. The fine powder portion of this grade can fill interstitial passages during filling, lowering permeability unpredictably; therefore batch records must log the particle size distribution, fill density, and sintering dwell time. Applications include wastewater aeration spargers, water treatment pre-filters, and low-load vent membranes.

    Thin-Gauge Compression-Moulded Liners for Bulk Solids Handling

    In bulk solids handling, compression-moulded liners of GUR 4122-5 are prepared in hydraulic presses with daylight openings from 150 mm to 600 mm and platen heating to 210°C; the powder is cold-compacted at 5–10 MPa before the heating cycle to remove entrapped air and improve thermal conductivity. The consolidated liner must be cooled slowly under pressure to avoid warpage; cooling from 180°C to 60°C at 0.5–1.0°C/min is typical for sheets thicker than 10 mm. The liner is then fabricated with routed edges and countersunk holes; fastening with bolts requires oversized drill holes because UHMWPE thermally expands more than carbon steel, and a 1 m panel can expand by 1.5–2.0 mm over a 30°C temperature change. Sand-slurry abrasion testing under ASTM G65 Procedure A and sliding wear testing under ASTM G99 are used for comparative ranking against 316 stainless steel and hardened carbon steel.

    Bulk solids handling applications for 4122-5 liners include chute and hopper linings, railcar unloading liners, and screw conveyor troughs where impact loading is below the material's notched Izod impact resistance of no break under ASTM D256 at 23°C. The liner should not be exposed to continuous service above 80–90°C because creep modulus declines and load-bearing capacity is reduced; short-term contact with hot particles up to 120°C may be tolerated only if the liner is mechanically restrained. Silicone oils and some lubricants can plasticise the surface and raise the coefficient of friction, so dry contact is preferred wherever possible. Static electricity build-up during powder conveying requires either conductive carbon-black additions, which are not standard in this grade, or external grounding and humidification above 50% RH.

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