Celanese Uhmw Pe 4222 5

Celanese UHMW-PE 4222-5

    • Product Name: Celanese UHMW-PE 4222-5
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    VTB
    Specifications
    HS Code 730452
    Polymer Type Ultra-high molecular weight polyethylene (UHMW-PE)
    Form Powder
    Color White
    Volume Resistivity Ohm Cm >1e15
    Notched Izod Impact No break

    As an accredited Celanese UHMW-PE 4222-5 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Celanese UHMW-PE 4222-5 is supplied in 25 kg multiwall paper bags, typically palletized and stretch-wrapped for transport.
    Container Loading (20′ FCL) 20′ FCL: Celanese UHMW-PE 4222-5 in palletized 25 kg bags; load in dry, clean container, secure cargo, avoid direct sunlight.
    Shipping Celanese UHMW-PE 4222-5 is generally shipped as a non-dangerous, non-regulated solid polymer. Standard packaging: 25 kg bags or fiber drums, palletized. Use clean, covered transport; avoid moisture, contamination, and excessive heat. No special hazard placards or permits are normally required. Follow local regulations and SDS guidance.
    Storage Store Celanese UHMW-PE 4222-5 in a cool, dry, well-ventilated area. Keep containers tightly closed, away from heat, sparks, open flames, direct sunlight, moisture, and strong oxidizers. Avoid dust formation and ignition sources; use grounded equipment. Keep in original labeled packaging and follow SDS/local regulations. Maintain clean, segregated storage. Protect from physical damage and contamination. Do not store with incompatible materials.
    Shelf Life Celanese UHMW-PE 4222-5 has an indefinite shelf life when stored dry, unopened, and protected from UV, heat, and contamination.
    Application of Celanese UHMW-PE 4222-5

    Celanese GUR 4222-5 enters wet-process lithium-ion battery separator lines as the high-molecular-weight polyethylene fraction blended with a lower-molecular-weight HDPE carrier to raise puncture resistance and melt strength during biaxial orientation. In continuous separator formulations reported across production-scale lines, the total polyethylene solids content in the paraffinic process oil is kept between 25 wt% and 40 wt%; within the polymer fraction, the GUR 4222-5 addition is held between 15 wt% and 35 wt%, with the balance being an HDPE grade selected for gelation uniformity. Below 15 wt% the puncture resistance gain is insufficient for high-energy-density cell qualification under ASTM F1306, while above 35 wt% the slurry shows progressive filter-pack pressure rise and die-lip build-up in intermeshing twin-screw extruders with L/D 52:1 or larger. The slurry is compounded at temperatures below the oil flash point, cast through a slot die, quenched to induce thermally induced phase separation, and then biaxially stretched in machine and transverse directions. After stretching, the film passes through a solvent extraction bath of n-hexane or methylene chloride to remove the process oil, followed by a heat-setting pass that stabilizes the microfibrillar pore architecture. Compliance documentation for separator films includes IEC 62660-3 for cell safety, ASTM D882 for tensile properties of thin plastic sheeting, ASTM F1306 for low-rate penetration resistance, and ISO 527-3 for film anisotropy characterization; separator converters additionally require batch release data for Gurley air permeability, shutdown temperature, residual solvent content, and extractable fraction. Terminal products are microporous separator films with thickness from 5 µm to 25 µm used in lithium-ion cells for electric vehicles, stationary energy storage systems, and consumer electronics packs.

    When Gel Spinning Requires a Narrow Solvent Removal Window

    The dissolution viscosity of GUR 4222-5 in decalin or a suitable low-volatility paraffin becomes the controlling variable in gel-spun UHMWPE fiber manufacture; lot acceptance for this grade is based on solution viscosity measured under ISO 1628-3, because the molar mass of the polymer places it outside the range of stable melt flow rate determination. Gel-spinning operations dissolve the polymer at 5–10 wt% in decalin or paraffin oil, with hindered phenolic antioxidant addition limited to ≤0.1 wt% of total solution to avoid spinline filament breakage and spinneret plate residue. The dissolution window is narrow: insufficient residence time leaves microgels that elevate pack pressure and cause heterogeneous denier profiles, while residence above 180 °C accelerates chain scission and reduces the maximum hot draw ratio. Production lines use intermeshing twin-screw dissolvers followed by gear-pump-fed spinnerets, a water or solvent quench bath, solvent extraction, and multi-stage hot drawing at total draw ratios typically between 30:1 and 60:1, with the exact ratio determined by final denier and tenacity targets. For cut-resistant gloves, the fiber or fabric is tested under EN 388:2016+A1:2018; for ballistic panels, composite samples are evaluated under NIJ 0101.06; and the yarn tensile properties are reported according to ASTM D2256/D2256M. Terminal product types include ballistic helmet and panel liners, maritime ropes, cut-resistant sleeves, and composite reinforcement tapes.

    Ram Extrusion Tooling Pressure and Die Land Residence in Food-Grade Wear Strip Production

    In food and beverage conveying lines, GUR 4222-5 is ram-extruded without a conventional screw because the polymer forms a high-melt-strength plug that is processed by a reciprocating hydraulic ram. The powder is charged into the ram barrel and consolidated at tooling pressures between 10 MPa and 30 MPa, with die zone temperatures held within 160–220 °C; die land residence is extended to fuse powder boundaries without reducing molecular weight through shear heating. The grade is not processed by conventional injection molding or melt blowing because the zero-shear viscosity exceeds standard barrel pressure capacity; attempts to force the material through a reciprocating screw typically produce unmelted particle domains and melt fracture at the gate. For profiles intended for direct food contact, the formulation is 100 wt% virgin UHMW-PE with no processing aids, because external lubricants can conflict with FDA 21 CFR 177.1520(c) and EU Regulation (EU) No 10/2011; framework compliance is also documented under EC 1935/2004. The EU compliance verification applies an overall migration limit of 10 mg/dm² under EN 1186-1 using food simulants corresponding to the filling line temperature. Non-food industrial wear strips may contain 2–5 wt% solid lubricant or antistatic concentrate, but such modifications are excluded from direct food-contact stock and reduce weld line tensile strength measured under ISO 527-2. The material specification for extruded profiles is covered by ISO 11542-1 and ASTM D4020, with the latter addressing viscosity and density test methods for UHMW-PE molding and extrusion materials. Terminal products are chain wear strips, bottle guide rails, starwheel segments, and conveyor slide profiles used in high-speed filling lines; the limiting failure mode observed on production lines is ram-frequency pulsation marking when barrel temperature is too low or die land length is insufficient.

    Compliance matrix for Celanese GUR 4222-5 downstream application segments
    Application segmentMaterial or process standardTest method / acceptance conditionTerminal product type
    Wet-process lithium-ion battery separatorIEC 62660-3, ASTM F1306ASTM D882 tensile, Gurley air permeability, shutdown temperatureMicroporous separator film 5–25 µm
    Gel-spun UHMWPE fiberNIJ 0101.06, EN 388:2016+A1:2018ISO 1628-3 solution viscosity, ASTM D2256/D2256M tensileBallistic panels, cut-resistant gloves, maritime ropes
    Food-grade ram-extruded wear profilesFDA 21 CFR 177.1520(c), EU 10/2011Overall migration 10 mg/dm², ISO 11542-1 design dataChain wear strips, guide rails, starwheel segments
    Compression-molded industrial linersREACH Regulation (EC) No 1907/2006, RoHS Directive 2011/65/EUASTM D4020 material specification, ISO 179-1 impactHopper liners, truck bed liners, pump volute liners
    Sintered porous gas diffusion elementsNSF/ANSI 61 if potable contact, ASTM F316Bubble point pore size 10–100 µm, ISO 2942 integrityAeration diffusers, vacuum chucks, filter support plates

    Compression molding of GUR 4222-5 into thick cross-sections for bulk solids handling equipment is selected when ram extrusion cannot produce sheet widths above 2,000 mm or thicknesses above 100 mm. In this process, the powder is filled into a mold, cold-compacted at 5–10 MPa, then sintered under platen pressure between 10 MPa and 15 MPa at platen temperatures from 200 °C to 230 °C; the controlled cooling step after the sintering plateau is maintained at 5–10 K/min to reduce core shrinkage voids and to avoid exothermic recrystallization defects in sections thicker than 40 mm. Formulation is normally 100 wt% UHMW-PE for hopper and chute liners, while 1–3 wt% molybdenum disulfide is added in lignite or ore handling liners to reduce surface friction; additions above 3 wt% reduce Charpy impact energy under ISO 179-1 and are generally not accepted for structural load-bearing wear parts. Compliance for mining and bulk solids components is typically limited to REACH Regulation (EC) No 1907/2006, RoHS Directive 2011/65/EU, and ASTM D4020, unless the liner will contact raw agricultural commodities, in which case converter verification against FDA 21 CFR 177.1520(c) is required; not all molybdenum disulfide-modified formulations meet food-contact status. Terminal products are hopper liners, truck bed liners, screw flight edges, pump volute liners, and guide blocks in dry bulk handling; the primary production failure mode is stress cracking around welded steel backing shells when thermal expansion is constrained by rigid bolt patterns, so installation clearances are specified by the equipment manufacturer.

    How Porosity Gradients Are Controlled in Sintered Gas Distribution Elements

    Sintered porous UHMW-PE elements manufactured from GUR 4222-5 are created by heating compacted powder in a mold to a temperature just below full fusion, leaving interconnected pores between particles. The average pore size depends on the particle size distribution of the powder fraction and the compaction pressure, with typical production targets from 10 µm to 100 µm; pore size is verified by bubble point testing under ASTM F316 and reported as maximum pore size and mean flow pore size. The forming process uses 100 wt% UHMW-PE powder, custom particle cuts, and sintering temperatures from 150 °C to 200 °C; gas distribution grades require no fugitive porogen because the pores are formed by incomplete fusion at the particle boundaries, while high-porosity filtration grades may be produced by molding with 40–60 wt% sodium chloride followed by water leaching after cooling. Compliance for effluent aeration and gas distribution service includes ASTM F316 for pore diameter, ISO 2942 for fabrication integrity by bubble point, and NSF/ANSI 61 when the element contacts potable water or air in drinking water systems; documentation should include differential pressure at rated flow and burst pressure. Published lot-specific data for GUR 4222-5 in porous gas diffusion elements is limited; converter validation of pore size distribution, burst pressure, and pressure drop at rated flow is required before release. Terminal products are cylindrical aeration diffusers for sequencing batch reactors, filter support plates, vacuum table porous beds, battery vent membranes, and laboratory vacuum chucks; the limiting operating boundary is tensile rupture of the sintered web at high differential pressures, which is reported as burst pressure by the converter.

    Free Quote

    Competitive Celanese UHMW-PE 4222-5 prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8618005193850 or mail to sales8@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8618005193850

    Email: sales8@ascent-chem.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    Celanese UHMW-PE 4222-5 is an ultra-high-molecular-weight polyethylene powder grade supplied as a free-flowing powder with molecular weight controlled through solution viscosity rather than melt flow rate. Because the polymer remains in the solid state during processing, melt flow rate values under ISO 1133-1:2022 are not used for lot release; the grade is specified by a viscosity number of 2000–2300 mL/g measured in decalin at 135 °C under ISO 1628-3:2010. The published density range is 0.930–0.935 g/cm³ under ISO 1183-1:2019, and the powder bulk density is typically 0.40–0.45 g/cm³ under ISO 60:1977. The grade is intended for solid-state processing by ram extrusion and compression moulding of wear components, guide rails, chain guides, filtration plates, and pump parts. Dynamic coefficient of friction against polished steel ranges from 0.20–0.30 when tested under ASTM D1894, and water absorption after 24 h at 23 °C is below 0.01% under ISO 62.

    The powder particle size distribution is controlled to support uniform feeding. Median particle size is typically in the 120–180 µm range, measured by laser diffraction under ISO 13320:2020. The fines fraction below 63 µm is limited to prevent dusting and irregular compaction in ram extrusion feed throats. Batch-to-batch variation in particle size distribution should be monitored by sieving under ASTM D1921; deviations above ±10% in the fraction retained on a 125 µm sieve can shift compaction density and produce variation in extruded part dimensions.

    The material is not melt-processable. Unlike high-molecular-weight high-density polyethylene grades that can be run on blown-film or sheet lines, 4222-5 has no practical melt-flow value under ISO 1133-1:2022 because the molecular chains remain entangled below the degradation temperature. Attempting to process it through a single-screw or twin-screw extruder results in high torque, poor output, and oxidative damage before a pumpable melt is formed. This distinction is the primary difference from standard HDPE and high-molecular-weight HDPE products; 4222-5 must be consolidated by pressure-assisted sintering rather than melt pumping.

    How does 4222-5 differ from lower-viscosity UHMW-PE grades?

    The grade sits between GUR 2122 and GUR 4120 in the Celanese UHMW-PE series. The higher viscosity number of 4222-5 relative to GUR 2122 produces improved abrasion performance in sand-slurry testing under ASTM G75, but increases ram extrusion pressures by approximately 10–15% on the same die. Compared with standard high-density polyethylene, 4222-5 shows a lower tensile modulus of 700–900 MPa under ISO 527-2/1BA/50 and a notched Izod impact strength that is reported as no break at 23 °C under ISO 180/A. Lower-viscosity grades such as GUR 2122 are easier to consolidate at lower pressures but exhibit higher wear volume loss; higher-viscosity grades such as GUR 4150 and GUR 4170 provide further abrasion resistance at the cost of longer sintering cycles and higher die pressures. The selection of 4222-5 is therefore driven by the balance between wear life and processability in parts with wall thicknesses above 10 mm.

    The following representative values are compiled from the manufacturer’s technical data sheet and adjacent grade literature for 4222-5. Lot-specific certification data should be requested for applications requiring traceable values.

    Typical property profile of Celanese UHMW-PE 4222-5
    PropertyValueTest method
    Density0.930–0.935 g/cm³ISO 1183-1:2019
    Viscosity number2000–2300 mL/gISO 1628-3:2010
    Tensile stress at yield18–22 MPaISO 527-2/1BA/50
    Tensile strain at break300–400%ISO 527-2/1BA/50
    Notched Izod impact at 23 °Cno breakISO 180/A
    Shore D hardness60–65ISO 868
    Vicat softening temperature75–85 °CISO 306/A50
    Melting peak temperature133–138 °CISO 11357-3
    Volume resistivity1×1014 Ω·cmIEC 62631-3-1
    Water absorption 24 h, 23 °C0.01%ISO 62

    No melt flow rate value is assigned because the material does not flow under conventional melt-flow testing.

    Ram extrusion and compression moulding boundary conditions

    Ram extrusion of 4222-5 requires a heated die with a temperature profile of 190–220 °C at the die inlet and a heated mandrel maintained at 120–180 °C to prevent premature solidification. Extrusion pressures at the ram face typically reach 25–40 MPa, with die land lengths of 30–50 mm and compression ratios between 2.5:1 and 4:1. The polymer does not form a homogeneous melt; therefore, single-screw and twin-screw extruders are not recommended regardless of screw L/D ratio. In compression moulding, platen temperatures of 200–230 °C, applied pressures of 5–10 MPa, and dwell times of 10–15 min per 10 mm of thickness are typical. Cooling under pressure at 10–20 K/min is required for wall thicknesses above 20 mm to control shrinkage and void formation. If the powder has been stored at relative humidity above 60%, hot-air drying at 80 °C for 4 h is advised before processing.

    The consolidation mechanism is sintering rather than melt fusion. At die temperatures below 190 °C, particle boundary healing is incomplete, and tensile strength can fall by 30–50% relative to the datasheet value. Above 220 °C, oxidative chain scission increases the carbonyl index and reduces notched Izod impact from no break to 20–40 kJ/m², a property cliff-edge that is not visible in standard density measurements. Therefore, the acceptable processing window is approximately ±15 K around 205 °C for long residence times.

    The thermal conductivity of 4222-5 is approximately 0.40–0.50 W/(m·K), which is lower than that of HDPE. This limits cooling rates in sections above 20 mm and makes internal residual stress more difficult to remove. Cooling rate after sintering controls final crystallinity and dimensional stability. Rapid cooling at 10–20 K/min suppresses secondary crystallite growth and produces lower crystallinity, which improves toughness but increases post-machining shrinkage. Slow cooling below 5 K/min increases crystallinity and hardness but can generate internal voids and dimensional variation exceeding ±1.5% in thick sections. Production lines commonly maintain pressure until the component core drops below 100 °C before demoulding.

    When replacing GUR 2122 or GUR 4120 with 4222-5 in wear components

    Substitution of GUR 2122 with 4222-5 increases sand-slurry abrasion resistance under ASTM G75, but the higher viscosity number raises the pressure required to fill a given ram extrusion die by approximately 10–15% and may require a 5–10 K increase in die temperature. Replacing GUR 4120 with 4222-5 normally reduces die pressure slightly and improves powder flow in free-flowing feeding systems, but the wear rate may increase in high-load applications. In both cases, the replacement is not a drop-in for injection moulding lines because the grade remains solid-state-processable only. For parts thicker than 30 mm, a post-forming annealing step at 100–120 °C for 2 h is often applied to reduce residual stress and improve dimensional stability after machining.

    Sand-slurry abrasion testing under ASTM G75 for UHMW-PE grades typically uses a 1:1 sand-to-water mixture by volume and a total cycle count of 5000. Under these conditions, 4222-5 is reported to show lower volume loss than GUR 2122 and HDPE, with the difference becoming significant after the first 1000 cycles. The exact wear rate is dependent on slurry velocity, sand particle size distribution, and the hardness of the mating surface; published data for this specific configuration in high-velocity slurry transport is limited.

    Compliance of 4222-5 must be verified against the supplier’s current regulatory certifications. The base olefin polymer may be evaluated under FDA 21 CFR 177.1520 for food-contact use when the grade is listed in the supplier’s certification, and under EU 10/2011 for plastics intended for food contact. For food-contact use in the European Union, overall migration must be below 10 mg/dm² for many applications under EU 10/2011, but final verification depends on surface-to-volume ratio and simulant conditions. Electrical and electronic applications require confirmation of RoHS Directive 2011/65/EU limits for lead, cadmium, mercury, hexavalent chromium, PBB, and PBDE. The grade is typically considered REACH compliant under Regulation (EC) No 1907/2006 as a polymer, but article-level SVHC obligations remain with the downstream user. For load-bearing implant components, the grade must be evaluated under ISO 10993-1 and ISO 5834-2 because polymer powder characteristics and stabilizer packages vary by lot.

    Regulatory evaluation checklist
    Regulation or standardScopeVerification basis
    FDA 21 CFR 177.1520Olefin polymers in food-contact articlesSupplier certification required for end-use conditions
    EU 10/2011Plastics in food-contact materialsOverall migration and specific migration limits apply
    RoHS Directive 2011/65/EUElectrical and electronic equipmentPb, Cd, Hg, Cr(VI), PBB, PBDE thresholds
    REACH Regulation (EC) No 1907/2006SVHC and authorizationArticle-level obligations remain with downstream user
    ISO 10993-1Biocompatibility of medical devicesLot-specific testing required
    ISO 5834-2Implants for surgery, UHMW-PEPowder characteristics and stabilizer package verification

    Continuous service above 80 °C under load is not recommended for 4222-5 because creep and wear accelerate sharply near the Vicat softening temperature. The material is incompatible with strong oxidizing acids at temperatures above 60 °C and with high-aromatic hydrocarbon environments that can cause softening and dimensional change. The grade should not be exposed to ultraviolet radiation for extended outdoor service without a UV-stabilized formulation; otherwise surface cracking and molecular weight reduction occur. Sterilization by steam at 121 °C may be performed only for short cycles and with the understanding that repeated autoclave exposure can increase crystallinity and reduce toughness. Gamma irradiation above 25 kGy may cause oxidative degradation and increase the measurable carbonyl index; if irradiation is required, the component should be stored under nitrogen and tested for molecular weight retention.

    After forming, 4222-5 is commonly machined with high-speed steel or tungsten carbide tooling at cutting speeds of 300–600 m/min. The low thermal conductivity of UHMW-PE means that local frictional heating can exceed 150 °C; water or air cooling is required to prevent dimensional distortion. Tool geometry should use positive rake angles and polished chip flutes to avoid smearing and built-up edge on the polyolefin surface.

    Typical production-scale uses for 4222-5 include chain guides, wear strips, star wheels, filtration plates, and pump volutes produced by ram extrusion and subsequent machining. In these applications, the product is selected over lower-molecular-weight UHMW-PE grades when the part requires a measurable improvement in abrasion resistance without moving to the higher die pressures of GUR 4150 or GUR 4170. Published data for this specific configuration in high-velocity slurry transport is limited; pump users should conduct end-use testing under ASTM G75 or ISO 15527:2022 to confirm wear life.

    Top