| HS Code | 837302 |
| Density | 0.95 g/cm³ |
| Bulkdensity | 0.50 g/cm³ |
| Averageparticlesize | 120 µm |
| Molecularweight | 2.0 x 10^6 g/mol |
| Viscositynumber | 1600 ml/g |
| Meltingpoint | 135 °C |
| Crystallinity | 45 % |
| Tensilemodulus | 700 MPa |
| Tensilestrengthatyield | 17 MPa |
| Tensilestrengthatbreak | 20 MPa |
| Elongationatbreak | 300 % |
| Charpynotchedimpactstrength | No break |
| Shoredhardness | 60 |
| Waterabsorption | <0.01 % |
| Coefficientoffriction | 0.15 |
| Thermalconductivity | 0.42 W/mK |
| Coefficientoflinearthermalexpansion | 2 x 10^-4 /°C |
| Dielectricconstant | 2.3 |
| Volumeresistivity | >10^15 ohm-cm |
| Dielectricstrength | 45 kV/mm |
| Chemicalresistance | Excellent |
| Uvresistance | Good |
| Maximumservicetemperature | 80 °C |
| Processingtemperature | 200 °C |
| Moldingshrinkage | 2 % |
| Abrasionresistance | High |
| Carbonblackcontent | 6 % |
As an accredited Celanese UHMW-PE 4022-6 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Celanese UHMW-PE 4022-6 is supplied in 25 kg bags, palletized and shrink-wrapped for secure industrial shipping and storage. |
| Container Loading (20′ FCL) | Non-hazardous Celanese UHMW-PE 4022-6 is supplied in 25 kg bags, 40 bags per pallet, 20 pallets per 20′ FCL. |
| Shipping | Celanese UHMW-PE 4022-6 is not regulated as dangerous goods for DOT, ADR, IMDG, or IATA. Ship in original sealed packaging as general cargo. Protect from moisture, contamination, and prolonged sunlight. No special ventilation or temperature control required; avoid dust generation and follow local regulations. |
| Storage | Store Celanese UHMW-PE 4022-6 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and flames. Keep containers tightly closed to prevent moisture, dust, and contamination. Avoid strong oxidizers. Maintain clean handling equipment. Do not store near acids, bases, or combustible materials. Follow the manufacturer’s safety data sheet and local regulations. |
| Shelf Life | Store cool, dry, away from heat, UV, and moisture; Celanese UHMW-PE 4022-6 has an indefinite shelf life under these conditions. |
In wet-process lithium-ion battery separator manufacturing, Celanese UHMW-PE 4022-6 functions as the ultra-high-molecular-weight polyolefin backbone that determines pore size distribution, puncture resistance, and thermal shutdown response of the microporous membrane. The cast dope is formulated at 10–25 wt% 4022-6 in 75–90 wt% paraffin oil or a mixed aliphatic/cyclic hydrocarbon solvent system; the ratio is trimmed to keep solution viscosity between 2×10³ Pa·s and 5×10³ Pa·s at 130–150°C, since lower concentrations generate oversized pores and higher concentrations retard phase separation in the quench bath. The downstream production sequence is a thermally induced phase separation route: the dope is extruded through a flat die at 140–160°C, cast onto a chilled roll at 15–30°C, then biaxially stretched at draw ratios of 5:1 to 7:1 in the machine direction and 5:1 to 7:1 in the transverse direction while the film is held at 110–125°C; the stretching temperature must remain within ±3°C of the target because deviations below 108°C leave insufficient pore elongation and deviations above 127°C collapse the oriented tie-chain structure. Residual plasticizer is removed by continuous extraction with methylene chloride or n-hexane, and the extracted membrane is heat-set at 120–130°C to control thermal shrinkage. Finished separator formats typically have thickness from 7 μm to 25 μm, porosity from 40% to 50%, and Gurley air permeability from 200 s/100 mL to 500 s/100 mL; terminal products include separators for lithium-ion power cells, portable-device cylindrical cells, and energy-storage pouch cells. Compliance for this downstream sector is anchored to ASTM D882-18 for film tensile properties, ASTM F1306-21 for slow-rate puncture resistance, IEC 62660-3:2016 for cell safety, and UN 38.3 transport testing of finished cells.
Ram extrusion of 4022-6 operates outside the assumptions of a conventional thermoplastic melting model because the polymer has no measurable melt flow rate under ISO 1133-1:2022 conditions and cannot be plasticated by a screw. The charge formulation is 100 parts 4022-6 powder; some production lines dry-blend 0.1–0.3 wt% calcium stearate or zinc stearate to reduce die friction, but levels above 0.5 wt% interrupt inter-particle diffusion and produce helical weld lines or radial delamination in thick profiles. Amine-based lubricants are avoided because they are not listed in the relevant olefin polymer positive lists for food contact and can exude to the part surface. Barrel zones are held at 180–200°C, the die land is maintained at 205–220°C, ram pressure is set between 30 MPa and 70 MPa, and stroke rate is controlled at 0.5–2.0 min⁻¹. The die exit is matched to a water-cooled mandrel at 10–30°C; this cooling stage is critical for sections above 20 mm because the solidified outer skin must restrain the still-relaxing core and prevent internal voiding. Production-scale failure modes include oxidation-induced yellowing when powder is held above 220°C for more than 30 min, and inconsistent fusion when powder bulk density shifts outside the supplier-controlled range after storage above 60% RH; pre-drying is therefore specified before charging when ambient humidity exceeds that threshold. Terminal products include bottle-handling guide rails, star wheels, wear strips, chain guides, and neck guide inserts for filling and packaging lines. Food-contact compliance is evaluated under FDA 21 CFR 177.1520(c) extractive limits, EU Regulation 10/2011 overall migration limit of 10 mg/dm², and NSF/ANSI 51-2019 for food equipment components.
Sintered porous elements manufactured from 4022-6 are produced without solvent and without a melt-phase processing window; the powder is cold-packed and thermally fused to create a rigid open-cell structure. The formulation is 100 wt% 4022-6 powder with no binder and no plasticizer; porosity is controlled entirely by particle size distribution and compaction ratio. Monomodal powder fractions from 80 μm to 250 μm typically produce mean flow pore diameters from 10 μm to 40 μm, while bimodal blends are used to generate finer mean pore diameters from 5 μm to 15 μm; incoming powder for critical filter grades is screened to a particle size tolerance of ±25 μm to limit lot-to-lot pore bias. In the production process, powder is charged into matched metal moulds, pressed at 3–10 MPa at ambient temperature, then sintered in convection or infrared ovens at 190–210°C for 20–60 min depending on part thickness; the oven atmosphere is held below 50 ppm oxygen to prevent oxidative chain scission and surface embrittlement. The sintering plateau must not exceed 220°C because pore-wall integrity and tensile elongation decline rapidly above that threshold. Terminal product types include pneumatic exhaust mufflers, air sparging diffusers, fluidizing plates, porous filter tubes for water treatment, and venting membranes for chemical storage. Compliance for porous industrial components is verified by bubble point testing per ASTM F316-03(2019), water absorption per ASTM D570-98(2018), and where potable water contact applies, NSF/ANSI 61 extractive testing.
Gel spinning converts 4022-6 into high-tenacity fibre only when the solution concentration is held below the point where extensional viscosity destabilises the spinneret. The spin dope is formulated at 5–8 wt% 4022-6 in decalin or paraffin oil; concentrations above 10 wt% are generally avoided because thread-line resonance and die-face build-up increase with the longer polymer relaxation time. The production process uses a heated dissolver and screw pump at 130–150°C, a metering pump, and a multi-hole spinneret with capillary L/D ratios from 2:1 to 4:1. The extruded gel fibre is quenched in a water bath at 5–20°C, extracted continuously with n-hexane or dichloromethane, and hot-drawn at 120–150°C to a total draw ratio of 50:1 to 100:1. Residual solvent must be reduced below 50 ppm before final drawing; higher residuals plasticise the gel fibre and produce irregular draw resonance, while the solvent recovery train is operated above 98% efficiency to meet VOC emission limits. Terminal products include cut-resistant gloves, soft ballistic panels, maritime ropes, fishing netting, and reinforcement fabrics for lightweight composites. Compliance is assessed through EN 388:2016+A1:2018 cut resistance for protective gloves, NIJ 0101.06 ballistic resistance for body armour panels, and ASTM D2256/D2256M-21 for yarn tensile strength and elongation.
Thick-section compression moulding of 4022-6 is used where ram-extruded profiles cannot be cooled uniformly; the process is the least shear-intensive conversion route and is specified for solid slabs and near-net liners. The formulation is 100 wt% 4022-6 with no plasticizer or processing aid; where static dissipation is required for ATEX environments, 1–5 wt% conductive carbon black masterbatch may be added, but this modification reduces impact strength and must be qualified separately for each part thickness. In the production process, powder is loaded into a mould frame, compacted at 5–15 MPa at ambient temperature, heated to 200–220°C under maintained pressure, and then cooled at 0.5–2.0 K/min while the platens remain closed. Premature pressure release before the core drops below 80°C causes warpage and residual stress in sheets above 30 mm. Terminal products include hopper liners, chute liners, silo liners, truck bed liners, and cut-resistant wear pads for bulk solids handling. Compliance and material acceptance are based on ASTM D4020-18 for UHMW-PE moulding and extrusion material, ISO 21304-1:2019 for designation and specification, and ISO 15527:2018 for slurry abrasion resistance.
In HDPE modification, addition of 4022-6 is not a conventional melt-blending operation because the ultra-high-molecular-weight component remains in a gel-like dispersed state at HDPE processing temperatures. The addition ratio is 10–25 wt% 4022-6 in a 75–90 wt% HDPE matrix; the upper limit is set by visible surface roughness and melt-pressure fluctuation during profile extrusion, and published data for loadings above 25 wt% in this specific 4022-6/HDPE configuration is limited. Pilot-scale trials are required because laboratory torque rheometry does not predict field-scale dispersion quality. The production process uses a co-rotating twin-screw extruder with an L/D ratio of 44:1 or higher, side feeding of 4022-6 powder downstream of the HDPE melting zone, melt temperature 220–240°C, and screw speed 300–600 rpm; the screw configuration must include two or more high-shear mixing zones after the side feeder, otherwise the UHMW-PE domains survive as visible gels and create surface defects in the final profile. Terminal products include conveyor rollers, idler wheels, chain guide profiles, and wear strips for dry bulk handling. Compliance for mechanical performance is verified through ASTM D638-14 for tensile properties, ISO 178:2019 for flexural modulus, and ISO 15527:2018 for slurry abrasion resistance.
Competitive Celanese UHMW-PE 4022-6 prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618136850665 or mail to admin@ascent-chem.com.
We will respond to you as soon as possible.
Tel: +8618136850665
Email: admin@ascent-chem.com
Flexible payment, competitive price, premium service - Inquire now!
Celanese UHMW-PE 4022-6 is an ultra-high-molecular-weight polyethylene powder grade supplied for conversion by compression molding, ram extrusion, and specialty densification. The material is identified in supplier documentation as part of the GUR 4022 series, with a reported viscosity-average molar mass of approximately 4.4 × 10⁶ g/mol derived from dilute-solution viscometry in decalin at 135 °C under ISO 1628-3:2010. Density is typically 0.930–0.940 g/cm³ under ISO 1183-1:2019, and apparent bulk density measured by ISO 60:1977 generally falls between 0.40 g/cm³ and 0.50 g/cm³. The grade does not exhibit a conventional melt flow rate at 190 °C/2.16 kg because the chain length suppresses viscous flow; processing therefore differs fundamentally from lower-molecular-weight polyethylenes.
At the molecular level, polyethylene has an entanglement molar mass of approximately 1.2 × 10³ g/mol. For a chain of 4.4 × 10⁶ g/mol, this corresponds to roughly 3.7 × 10³ entanglement strands per molecule. The resulting zero-shear viscosity exceeds practical melt-processing limits, and the longest relaxation times are orders of magnitude above those of standard injection-molding grades. These properties are the source of both high toughness and the need for quasi-static consolidation processes.
The standard ISO 1133-1:2022 procedure conditions polymer at 190 °C under a 2.16 kg piston load. For a linear polyethylene with molar mass in the 10⁶ g/mol range, zero-shear viscosity exceeds 10⁸ Pa·s, and the specimen does not leave the capillary within the specified interval. High-load testing at 21.6 kg may force flow through shear-induced disentanglement, but the result is not a reliable processability index because it can coincide with thermo-oxidative changes at the test temperature. Consequently, 4022-6 is not processed by conventional single-screw extrusion, injection molding, or blow molding. It is limited to operations in which powder is heated and consolidated under pressure in a closed cavity or a heated ram barrel. This constraint separates UHMW-PE from standard HDPE, which is routinely processed at melt flow rates of 0.2–10 g/10 min under the same standard.
Powder morphology further influences process selection. Sieve analysis under ASTM D1921 typically places the median particle size (d50) of UHMW-PE powders in the 120–180 µm range. Narrow particle size distribution improves bed uniformity during compression molding, while broad or segregated fractions can produce density gradients and internal voids. The powder is not free-flowing in the same manner as spherical pelletized resins; hopper design for ram extrusion must account for bridging tendencies and inconsistent mass flow at low bulk density.
Compression molding of 4022-6 is carried out in hydraulic presses with platen parallelism controlled to 0.1 mm/m or better. The mold is charged, leveled without shear, and heated under contact pressure to 190–210 °C at the mold wall. Once the cavity reaches uniform temperature, the press is closed to 8–15 MPa and held long enough to eliminate powder particle boundaries; cooling is then conducted under pressure at a rate below 20 K/min. Inadequate peak-temperature dwell produces knit lines and particle boundaries that act as crack initiation sites. Excessive hold above 210 °C accelerates hydroperoxide formation and reduces elongation at break, so mold-wall thermocouples are used to control the heating cycle rather than relying on timer-based recipes alone.
Ram extrusion of rod, sheet, and profile stock uses a heated barrel and die with zone temperatures generally maintained in the 200–230 °C range and ram pressures of 20–40 MPa depending on cross-section and throughput. Published data for grade-specific ram extrusion settings are limited; converters typically establish the acceptable pressure-speed window by trial on a given machine. Pre-drying is not required at relative humidity below 60%. Powder stored in damp conditions is dried at 80 °C before mold charging to avoid steam-induced porosity.
UHMW-PE exhibits a thermal conductivity of approximately 0.4 W/(m·K) under ISO 22007-2:2008, higher than unfilled polyolefins but far below tool steels. For slab thicknesses above 50 mm, heating and cooling time is controlled by conductive heat transfer rather than press pressure or mold temperature setpoint. Cycle time in thick sections scales approximately with the square of wall thickness; doubling the part thickness can increase cycle time by a factor of approximately 4 under identical boundary conditions. This limits the practical thickness of compression-molded 4022-6 plates when cycle time is a production constraint.
Relative to standard high-density polyethylene (HDPE) with molar mass typically between 10⁵ g/mol and 5 × 10⁵ g/mol, 4022-6 has a much higher entanglement density. Under ISO 179-1:2010 Charpy impact testing at 23 °C, UHMW-PE specimens of this class commonly show no break, whereas notched HDPE values are typically reported in the 5–20 kJ/m² range. Tensile yield stress is not the decisive differentiator; the practical differences are elongation at break, impact response, and abrasive wear resistance. In three-body abrasive wear evaluated under ASTM G65-16 dry-sand rubber-wheel conditions, UHMW-PE grades show substantially lower volume loss than HDPE, but exact wear rates depend on sand type, wheel hardness, and normal load. Sliding wear against stainless steel evaluated by ASTM G99-17 pin-on-disc protocols commonly places the coefficient of friction of UHMW-PE in the 0.10–0.25 range, with increases at low speed, high roughness, or boundary-lubrication breakdown.
| Property | Test method | UHMW-PE class | HDPE reference class |
|---|---|---|---|
| Density | ISO 1183-1:2019 | 0.930–0.940 g/cm³ | 0.940–0.960 g/cm³ |
| Tensile yield stress | ISO 527-2:2012 | 20–24 MPa | 22–30 MPa |
| Elongation at break | ISO 527-2:2012 | >200% | 50–900% |
| Charpy notched impact, 23 °C | ISO 179-1:2010 | No break | 5–20 kJ/m² |
| Hardness, Shore D | ISO 868:2003 | 60–65 | 68–74 |
| Melt flow rate, 190 °C/2.16 kg | ISO 1133-1:2022 | Not measurable | 0.2–10 g/10 min |
Within the Celanese GUR UHMW-PE range, 4022-6 is positioned at the lower-to-intermediate molecular weight segment relative to grades such as GUR 4150 and GUR 4170. Higher molecular weight grades develop greater abrasion resistance and toughness but demand longer molding cycles, higher consolidation pressures, and stricter thermal control. Lower molecular weight grades may process faster in thin sections or high-output ram extrusion at the expense of wear life. The selection of 4022-6 therefore represents a processability-wear balance rather than a maximum in any single property.
Component uses for 4022-6 include chain guides, wear strips, chute liners, star wheels, guide rails, and impact pads in materials-handling and food-processing equipment. These applications subject the polymer to sliding contact with metal or plastic countersurfaces, low-speed abrasive contact, and frequent mechanical shock. Moisture absorption under ISO 62:2008 is below 0.01%, which prevents the dimensional shift and friction variation observed in hygroscopic engineering thermoplastics such as polyamide PA66. Compared with polytetrafluoroethylene (PTFE), UHMW-PE is generally less chemically inert and has a lower continuous-use temperature limit near 80–100 °C, but it offers higher resistance to abrasive wear in many dry and slurry-type applications. The operational upper temperature is not governed by melting alone; creep under load increases rapidly above 60 °C, and load-bearing designs require time-dependent modulus data rather than short-term tensile values.
Under dry sliding, frictional heat input is the product of normal load, sliding speed, and coefficient of friction. For UHMW-PE, the pressure-velocity limit is lower than for filled engineering thermoplastics; localized surface temperature can exceed the bulk continuous-use limit even at moderate ambient temperature. Design calculations must therefore use measured or calculated contact temperature rather than bulk service temperature. At elevated sliding speed, lubrication or reduced contact pressure is required to avoid surface melting and transfer film breakdown. This constraint is relevant in high-speed conveyor guides and rotating wear pads, where short-duration frictional heating controls service life more than ambient thermal conditions.
In impact service, Charpy specimens of UHMW-PE do not break at 23 °C under ISO 179-1:2010. Ductility persists at cryogenic temperatures; standard published data report useful impact resistance at -196 °C, but grade-specific certification should be requested for cryogenic service. When the material is machined into components, carbide-tipped tools with positive rake angles and low cutting speeds prevent surface melting. Dimensional stability is limited by thermal expansion and stress relaxation; the coefficient of linear thermal expansion is typically 1.5 × 10⁻⁴ K⁻¹ to 2.0 × 10⁻⁴ K⁻¹ under ISO 11359-2:1999, approximately 10 times that of steel. Long wear strips therefore require slotted holes, expansion gaps, or preloaded spring systems.
In food-contact and packaging machinery, the polymer is often selected for low water absorption and resistance to impact rather than high continuous-use temperature. Wear plates in silos and hoppers operate under low sliding speeds and moderate loads; here the limiting failure mode is often not surface wear but slow creep at bolt holes and support points. Published data for 4022-6 in these specific large-part configurations is limited, so qualification should include creep testing under ISO 899-1:2017 at the intended service temperature and stress.
Compliance status for 4022-6 must be confirmed from the lot-specific certificate of analysis and the current supplier declaration. Typical virgin UHMW-PE grades in this molecular weight class are evaluated under FDA 21 CFR 177.1520 for olefin polymers in food-contact applications and under EU Regulation No 10/2011 for plastic materials intended for contact with food. Migration testing is performed according to EN 1186-1:2002 or equivalent national standards. The grade is not inherently flame-retardant, and continuous exposure to strong oxidizing acids, chlorinated hydrocarbons, or aromatic solvents at elevated temperature is outside the recommended service envelope. Ultraviolet exposure degrades unstabilized UHMW-PE; outdoor use requires carbon black or hindered-amine stabilization. Processing above 230 °C accelerates oxidative chain scission and should be avoided. Regrind addition in compression molding is generally limited to 20 wt% to preserve impact resistance, but the exact level must be validated against the part specification. Thermo-oxidative stability can also be screened by oxidation induction time under ISO 11357-6:2021; unstabilized UHMW-PE powders exhibit shorter induction times than stabilized molding grades, and the stabilization package should be matched to the service temperature.
| Requirement | Standard or regulation | Typical assessment |
|---|---|---|
| Food-contact olefin polymer | FDA 21 CFR 177.1520 | Extractables limits and end-use restrictions |
| EU food-contact plastic | EU Regulation No 10/2011 | Overall migration limit 10 mg/dm² |
| Migration testing | EN 1186-1:2002 | Food simulant exposure and gravimetric analysis |
| RoHS heavy metals | RoHS 2011/65/EU | Pb, Hg, Cr6+ < 1000 ppm; Cd < 100 ppm |
| Chemical resistance screening | ASTM D543-21 | Visual, mass, and mechanical property change |
Because published data for grade-specific chemical compatibility in mixed solvents is limited, qualification trials under ASTM D543-21 are required before use in aggressive media. The same reservation applies to hot-water or steam contact above 60 °C, where oxidation kinetics and mechanical load-bearing capacity must be evaluated together.