Products

Celanese UHMW-PE X 204

    • Product Name: Celanese UHMW-PE X 204
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    Specifications
    HS Code 480225
    Material Type Ultra-high molecular weight polyethylene (UHMW-PE)
    Density 0.930 g/cm³
    Molecular Weight 4,000,000 g/mol
    Bulk Density 0.45 g/cm³
    Average Particle Size 150 µm
    Water Absorption 0.01%
    Shore D Hardness 60
    Tensile Modulus 700 MPa
    Tensile Strength At Yield 17 MPa
    Tensile Strength At Break 22 MPa
    Elongation At Break 350%
    Flexural Modulus 800 MPa
    Notched Izod Impact Strength No break
    Coefficient Of Friction 0.15
    Abrasion Resistance High
    Melting Point 135 °C
    Vicat Softening Point 80 °C
    Maximum Service Temperature 80 °C
    Thermal Conductivity 0.40 W/m·K
    Coefficient Of Linear Thermal Expansion 200 µm/m·°C
    Dielectric Constant 2.3
    Dielectric Strength 45 kV/mm
    Volume Resistivity 1.0E+15 ohm·cm
    Flammability Ul94 HB
    Limiting Oxygen Index 20%

    As an accredited Celanese UHMW-PE X 204 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Celanese UHMW-PE X 204 is supplied in 25 kg multiwall paper bags, palletized at 1,000 kg per pallet.
    Container Loading (20′ FCL) Celanese UHMW-PE X 204 loaded into a 20′ FCL container, palletized, strapped, and secured for ocean transport.
    Shipping Celanese UHMW-PE X 204 is not classified as dangerous goods for transport. It is shipped in sealed bags, drums, or bulk containers. Keep dry, avoid dust and ignition sources, use clean, dry vehicles, maintain container labels, and follow supplier SDS/local rules. Handle to minimize static discharge and moisture exposure.
    Storage Store Celanese UHMW-PE X 204 in a cool, dry, well-ventilated area in tightly closed, labeled containers. Protect from moisture, direct sunlight, heat, and ignition sources. Keep away from strong oxidizers. Minimize dust generation and accumulation; use grounding and bonding where required. Do not exceed recommended storage temperatures. Maintain good housekeeping, avoid contamination, inspect containers regularly, and follow supplier guidance.
    Shelf Life No specific shelf life reported; stable under normal storage conditions—cool, dry, sealed, away from heat, sunlight, and contaminants.
    Application of Celanese UHMW-PE X 204

    In wet-process lithium-ion battery separator manufacturing, Celanese UHMW-PE X 204 is dry-blended with paraffinic process oil at a polymer loading of 18–28 wt%. The dry-blend is first passed through a high-speed ploughshare mixer at 800–1,200 rpm to break powder agglomerates and prevent gel-particle carryover into the cast film. It is then melt-blended in a counter-rotating twin-screw extruder with L/D ratio 36:1 and barrel zone set points from 160 °C to 220 °C. The resultant gel is cast onto a chill roll maintained at 15–40 °C and subsequently oriented in machine and transverse directions at ratios of 5:1 × 5:1 to 7:1 × 7:1. Process oil is extracted with methylene chloride or n-hexane, and the microporous membrane is heat-set at 100–130 °C to stabilise pore geometry. Final separator thickness is typically 9–20 μm with porosity controlled between 35% and 50%. Residual oil must remain below 1.0 wt% to avoid impedance rise in the assembled cell. Loading above 28 wt% increases gel viscosity to the point of die pressure instability and gel particle formation; loading below 15 wt% reduces puncture resistance after extraction and can produce localised thinning during orientation. Process-control references include ASTM D882-18 for film tensile, ISO 5636-5:2013 for air permeance, and IEC 62133-2:2017 for cell-related qualification. Because separator quality is sensitive to powder morphology, incoming X 204 lots should be screened for bulk density and particle size distribution against the converter’s internal wet-process specification before large-scale solvent-paste preparation.

    Table 1. Wet-process battery separator formulation and control window for X 204
    Parameter/componentTypical rangeProcess locationControl criterion
    UHMW-PE X 204 powder18–28 wt%premixer and extruder feedabsence of gel particles in cast film
    Paraffinic process oil69.5–78.9 wt%premixer and extractionresidual oil <1.0 wt%
    Antioxidant0.1–0.5 wt%premixerno thermally induced yellowing
    Extruder melt temperature180–220 °Cbarrel and diepressure stability and gel homogeneity
    Chill roll temperature15–40 °Ccast stationuniform gel-sheet thickness
    Orientation draw ratio5:1 × 5:1 to 7:1 × 7:1machine and transverse orientationcontrolled pore tortuosity
    Heat setting100–130 °Cpost-extractiondimensional stability and low thermal shrinkage

    What Changes in Capillary Flow Stability When the Spinning Dope Contains X 204 Instead of a Lower-IV UHMW-PE?

    Gel-spun fibre conversion of X 204 uses a solution of 8–12 wt% polymer in decalin or white mineral oil. The dope is conditioned under nitrogen at 180–200 °C for 45–90 min, then metered by gear pump through a spinneret with capillary diameter 0.2 mm and capillary L/D 10:1. Spin draw ratios are constrained to 30:1–70:1 in the gel state; higher spin draw accelerates surface fracture and filament breakage because chain entanglement density in X 204 prevents localised slip. The gel yarn is extracted in trichloroethylene or heptane, then hot-drawn at 140–150 °C to a total draw of 80:1–120:1. Resultant filament is used in cut-resistant gloves, ballistic composites, high-modulus ropes, and tendon replacements. Qualification for cut-resistant gloves refers to EN 388:2016 clause 6.2; filament tensile testing follows ISO 2062:2009. Intrinsic viscosity of incoming X 204 powder should be screened by ASTM D4020-18 because lot-to-lot molecular weight shifts alter dope filtering behaviour and maximum stable draw.

    Solvent recovery and residual solvent mass fraction below 0.5 wt% are non-negotiable for fibre compliance. The dope preparation unit should include sintered stainless steel filter packs with absolute rating 20 μm because X 204 lots with elevated gel count can block spinnerets and destabilise capillary flow. Dope concentration above 12 wt% elevates extensional viscosity and produces coarse filament denier, whereas concentration below 8 wt% reduces economic yield and increases solvent recovery load. Published data for X 204-specific gel-spun fibre tenacity is limited; processors should generate baseline dope rheology and draw maps under production conditions before commercial campaigns.

    Compression molding of X 204 into food-contact chain guides for PET bottling lines uses no plasticizer or external lubricant. Powder is filled into a matched-metal mould and consolidated under 10–15 MPa at 200–210 °C for 20–30 min for a 25 mm slab. Cooling under pressure at 0.5–2 K/min to below 70 °C is required before demoulding to prevent dimensional bow and residual stress. Holding the mould above 220 °C accelerates thermo-oxidative chain scission and discolouration; pre-drying at 80 °C for 4 h is advised when storage relative humidity exceeds 60%. Finished guides include star wheels, rail profiles, and scraper blades. Food-contact compliance is based on FDA 21 CFR 177.1520(c) 2.1 and EU 10/2011 overall migration limit of 10 mg/dm². Friction against polished steel is measured by ASTM D1894-14, and wear resistance by ASTM G133-05(2016). The converter must confirm that the specific X 204 lot is covered by the vendor food-contact declaration and that no reprocessed off-spec wear stock is blended into the moulding powder. The material is not recommended for continuous exposure to steam above 121 °C or for contact with strong oxidising acids, because oxidative degradation produces carbonyl species detectable by infrared surface analysis.

    Sintered Porous Components Show a Narrow Necks-Growth Window

    Free sintering of X 204 powder into porous filter elements is performed without high compaction. The powder is screened to a particle fraction of 100–300 μm, charged into a steel mould, and heated at 180–195 °C for 2–5 min per mm of wall thickness. Under these conditions, neck formation occurs at particle contacts without complete loss of interparticle porosity. A mean flow pore size of 20–80 μm is typical when the particle fraction is tightly controlled, but X 204 lot-to-lot bulk density and particle shape affect final permeability. Sintering above 195 °C or extending residence beyond 5 min/mm causes pore collapse and a sharp drop in bubble point pressure. Under-sintering below 180 °C yields weak particle bonding and surface dusting. End components include fine-bubble aeration discs for wastewater facilities, pneumatic silencers, and porous vent membranes that prevent pressure differentials in battery enclosures. Filtration rating is measured by bubble point method ISO 2942:2018; permeability is evaluated by ISO 4022:2018; retention efficiency for hydraulic or air systems may be confirmed by ISO 16889:2016 or ISO 29463-4:2011. Because X 204 is non-melting, sintered tensile strength can be 30–60% lower than solid compression-moulded stock; mechanical qualification should therefore be done on identical sintered specimens rather than extrapolated from solid-sheet data.

    When Continuous Lengths of Low-Slip Guide Rail Must Be Produced Without Ordinary Melt Extrusion

    Ram extrusion of X 204 powder into continuous profiles is an alternative to compression moulding when long one-piece rail sections are required. A reciprocating densifier compacts the powder at 20–40 MPa and advances the compact through a heated die with preheat zone 180–200 °C, die body 190–210 °C, and cooling throat 80–120 °C. Because no screw mixing occurs, output is low, typically 0.5–3 m/h depending on profile cross-section and ram diameter. The process eliminates the melt-flow requirement that prevents conventional single-screw extrusion of UHMW-PE. Resulting rectangular guide rails, round bar stock, and conveyor wear strips are machined into bushings and slide plates. Stock shape tolerances should be checked against ISO 11542-2:2007; tensile properties are assessed by ASTM D638-14, and wear factor by ASTM D3702-94(2019). Ram-extruded X 204 retains low sliding friction against stainless steel, but the die surface controls static friction; a polished die with Ra below 0.8 μm is standard. Processors should monitor frictional heating when ram speed exceeds 0.5 m/h for thick profiles, because local internal temperatures above 210 °C can generate oxidation defects at the centreline.

    Table 2. Compliance and test matrix by downstream application
    ApplicationStandard/regulationMethod or clauseParameter
    Battery separatorASTM D882-18, ISO 5636-5:2013, IEC 62133-2:2017strip tensile, Gurley air resistance, cell safetyseparator strength and barrier function
    Gel-spun fibreISO 2062:2009, EN 388:2016, ASTM D4020-18filament tensile, cut resistance, intrinsic viscosityyarn quality and molecular weight
    Food-contact wear stripsFDA 21 CFR 177.1520(c), EU 10/2011, ASTM D1894-14food contact, overall migration, frictioncompliance and slip behaviour
    Sintered porous partsISO 2942:2018, ISO 4022:2018, ISO 16889:2016bubble point, permeability, multi-pass retentionfiltration rating and porosity
    Ram-extruded stock shapesISO 11542-2:2007, ASTM D638-14, ASTM D3702-94(2019)dimensions, tensile, wear factorstock quality and machinability
    Bearing insertsASTM G99-17, ASTM D3702-94(2019), ASTM D638-14pin-on-disk, thrust washer, tensiletribology and load capacity

    In NBR and HNBR compounds used for reciprocating seals, gaskets, and conveyor skirt boards, X 204 powder is added at 5–15 phr as a particulate solid lubricant and abrasion additive. Dispersion is best performed after carbon black and before curatives on a two-roll mill at 60–80 °C; the non-melting UHMW-PE particles form discrete low-shear domains that reduce stick-slip at the compound surface. Loadings above 20 phr are not recommended because the phase-separated particles reduce tensile strength by 20–40% and can lower elongation at break below specification limits. Sulfur-cured systems are generally unaffected at normal cure times, but peroxide-cured compounds may show scorch time shifts due to radical trapping by UHMW-PE chain ends; screening should include ISO 6502 cure rheometry. Conveyor belt applications may require flame-resistance compliance under ISO 340. For food-contact rubber goods, migration into food simulants must be verified against EU 10/2011 because X 204 powder can migrate mechanically from abraded surfaces under dynamic loading. Published data for X 204 in nitrile compounds is limited; compounders should first generate a lab-scale mixing curve, cure trace, and abrasion panel on production-similar equipment before specifying the grade in high-volume formulations.

    Dry Sliding Bearing Inserts and the PV Ceiling

    Bearing inserts machined from X 204 compression-moulded or ram-extruded stock are specified for dry-running pivots and idler bushings where external lubrication is undesirable. The continuous dry-running pressure-velocity ceiling is conservatively set below 0.10 MPa·m/s against polished 316L stainless steel with surface roughness Ra 0.2–0.4 μm. Intermittent operation may reach 0.20 MPa·m/s if frictional heat can be dissipated and bulk temperature remains below 80 °C. The coefficient of friction and wear rate are typically measured by ASTM G99-17 pin-on-disk and ASTM D3702-94(2019) thrust washer. Because UHMW-PE has a high coefficient of thermal expansion, approximately 1.5×10⁻⁴ K⁻¹, clearance in bearing housings must be increased by 0.003–0.005 mm/mm of journal diameter per 10 K temperature rise. X 204 inserts are not suitable for service in aromatic hydrocarbons, chlorinated solvents, or strong oxidising acids; swelling and oxidative chain degradation occur in these fluids. Under water-lubricated or food-oil emulsion conditions, the PV ceiling shifts, but published data for X 204-specific wet PV limits is limited and must be generated on production-machined test coupons.

    Free Quote

    Competitive Celanese UHMW-PE X 204 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

    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 X 204 is a grade designation within the ultra-high-molecular-weight polyethylene class covered by ISO 11542-1. Public product-specific data for the X 204 configuration are limited; certificates of analysis and manufacturer technical datasheets remain the controlling documents. The class is distinguished from standard high-density polyethylene by the near-absence of measurable melt flow under ISO 1133-1 at 190 °C and 21.6 kg, and by a molecular mass threshold commonly stated as 3.1 × 10⁶ g/mol in ASTM D4020. The solid-state behaviour of UHMW-PE grades follows from the high entanglement density of very long linear chains rather than from comonomer short-chain branching.

    Manufacturing indicators for this category are powder bulk density, viscosity number, and tensile properties after compression moulding. Powder bulk density for UHMW-PE conversion grades is frequently reported in the range 0.40–0.50 g/cm³ under ISO 60; viscosity number is specified in the designation system of ISO 11542-1. Tensile yield stress values from compression-moulded sheet are commonly reported between 20 MPa and 24 MPa under ISO 527-2, with elongation at break in excess of 200%. These values are not a substitute for X 204 lot data but define the performance envelope in which the grade operates.

    Product designation X 204 is intended for applications in which compressive loading, sliding wear, and cyclic impact occur simultaneously. Typical conversion routes include compression moulding, ram extrusion, and skiving from moulded block. The resin is supplied as a powder rather than pellets; particle morphology and bulk density are therefore materials-handling parameters rather than mere packaging details. On plant-scale powder handling equipment, discharge from silos can be rate-limited by bridging if powder is not conditioned at low humidity; the material itself absorbs negligible moisture, but surface moisture on particles can alter packing and fusion uniformity.

    What Separates X 204 from Standard HDPE in Solid-State Property Testing?

    The most significant separation occurs in solid-state mechanical response and abrasion, not in density. The comparison below uses UHMW-PE family ranges; X 204-specific values must be obtained from the current certificate of analysis.

    Material propertyTest methodUHMW-PE family rangeHDPE comparison range
    DensityISO 1183-10.930–0.940 g/cm³0.952–0.965 g/cm³
    Tensile yield stressISO 527-220–24 MPa25–30 MPa
    Elongation at breakISO 527-2200–400%100–800%
    Shore D hardnessISO 86860–6664–68
    Charpy notched impact at −30 °CISO 179-1/1eANo break in standard laboratory tests4–12 kJ/m²
    Abrasion lossISO 464970–100 mm³200–400 mm³

    For X 204, the effective comparison against HDPE is observed not only in laboratory data but also in conversion behaviour. High-density polyethylene can be pelletised, transported, and screw-plasticised; UHMW-PE powder requires near-zero shear consolidation. The property advantage in impact and abrasion is therefore tied to a processing penalty: the same molecular entanglement that prevents brittle fracture also prevents melt flow. This trade-off is the central differentiator between X 204 and standard HDPE grades.

    Relative to other high-performance polymer materials, the UHMW-PE class shows lower density than PTFE and higher notched impact than unfilled POM at sub-zero temperatures. Moisture absorption is lower than PA6 under ISO 62. The continuous-use temperature of UHMW-PE is lower than that of PTFE or PEEK, with most conversion literature placing the practical hot-air exposure limit near 90–100 °C for sustained load. These boundaries are relevant when X 204 is evaluated as a replacement for metal wear plates or as an alternative to filled POM and PA6 in sliding applications.

    Thermal and Rheological Boundaries During Gel-State Conversion

    Differential scanning calorimetry of UHMW-PE typically identifies a crystalline melting range near 130–137 °C under ISO 11357-3. The gel-state conversion range for compression moulding is generally reported between 190 °C and 230 °C. The material does not form a freely flowing melt; therefore, the melt mass-flow rate test in ISO 1133-1 is not a suitable quality-control parameter. Consolidation under pressure is time- and temperature-dependent: a 30 mm thick powder charge may require 30–60 min dwell at pressure, depending on platen temperature and powder bed density. The exact dwell time for X 204 must be established with the manufacturer’s thermal data.

    The thermal boundary is narrow. In air, extended exposure above 250 °C can produce oxidative chain scission and surface yellowing; heating below approximately 185 °C leaves residual powder-particle boundaries that act as crack initiation sites under sliding wear. Production-scale compression presses with platen temperature uniformity of ±5 °C are therefore considered critical equipment. Published conversion guidance recommends an inert gas blanket or vacuum when the cycle must exceed 230 °C; without such protection, the maximum practical platen set point is normally held at 220 °C to preserve molecular integrity. The exact set point for X 204 may vary with additive package and powder morphology.

    Sintering converts powder into porous or partially fused blanks; this route is distinguished from full fusion compression moulding by lower heat input and higher residual porosity. The choice between sintered and fully fused forms changes final density, chemical resistance, and wear life. For X 204, the optimum route is controlled by the final part cross-section and by the mechanical load; thin sections can be skived from compression-moulded cylinders, while thick sections are usually machined from fused slab to avoid skin-core density differences.

    In wear-part manufacturing, the difference between an acceptable component and a bowed reject often appears at the post-fusion cooling stage. A 40 mm compression-moulded slab cooled faster than 0.5 K/min from 180 °C to 80 °C may retain residual internal stress; machining after cooling releases that stress as concave bowing. Controlled cooling rates of 0.5–1 K/min, press parallelism of 0.05 mm/m, and post-machining annealing at 120 °C for 4 h are cited in UHMW-PE conversion literature as countermeasures. These requirements are more restrictive than those for standard HDPE, which can be rapidly cooled with lower distortion risk because of faster stress relaxation and lower molecular entanglement.

    On ram extrusion lines, feedstock for UHMW-PE grade X 204 should be characterised by powder flow and bulk density before metering into the zone-fed barrel. Published processing literature for UHMW-PE ram extrusion reports barrel temperature zones in the range 200–240 °C and crosshead pressures typically between 20 MPa and 40 MPa, depending on profile wall thickness and die land length. The grade-specific pressure requirement for X 204 must be validated on the target machine because packing density, lot viscosity number, and die geometry interact to determine product porosity and impact strength. A ram speed that exceeds the fusion rate at the barrel wall produces unmelted core material; this failure mode is visible as axial voids or opacity in the extruded section.

    When Screw Plasticisation Is Proposed, the Grade Boundary Must Be Re-Evaluated

    If a downstream process uses a twin-screw extruder with an L/D ratio of 40:1 or an injection-moulding machine clamp force in the range 1,000–5,000 kN, the use of unmodified UHMW-PE X 204 is generally not appropriate unless the manufacturer explicitly classifies the grade as an injection-moulding or screw-extrudable modification. Standard UHMW-PE does not develop a stable melt front; it can block a screw, overtorque the drive, and produce severe chain degradation at the barrel wall. Published failure modes on production lines include feed-block bridging and screw bypass at compression ratios above 2:1. Release of the grade for screw processing must be based on the manufacturer’s documented rheological designation, not on HDPE-equivalent flow assumptions.

    Within the UHMW-PE family, product differentiation is largely a function of viscosity number and powder morphology. Grades with lower viscosity number consolidate more rapidly under heat and pressure but may show lower abrasion resistance; higher-viscosity grades offer longer wear life but demand longer dwell times and higher press force. Filled variations containing glass, carbon, or internal lubricant modify stiffness, thermal conductivity, or friction, but they also alter fusion viscosity and require separate welding and machining parameters. The selection of X 204 should therefore be based on a comparison of its viscosity number and powder bulk density with the specific ram extrusion or compression moulding equipment on the shop floor, not on HDPE melt-flow data.

    In sliding wear against steel, UHMW-PE materials are reported to operate in a low-wear regime at contact pressures below 10 MPa and surface velocities below 1 m/s; outside this region, frictional heating raises surface temperature and can initiate softening. For X 204, the limiting pressure-velocity envelope should be obtained from application testing. The mechanism shift from abrasion to adhesion is accompanied by a rise in contact temperature above the crystalline softening interval, not necessarily by visible melting.

    Where food-contact profiles are manufactured from X 204, verification against FDA 21 CFR 177.1520 and EU 10/2011 is required for the specific formulation and lot. Electrical and electronic applications require assessment against RoHS 2011/65/EU for lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE. These regulatory frameworks do not automatically apply to the base resin; they apply to the final article and to additives, colorants, and processing aids used in conversion. Celanese lot-specific documentation is required for any compliance statement.

    Published data for the specific X 204 configuration is limited; therefore, the values in this text are UHMW-PE family data and are not a substitute for the current technical datasheet. Lot release should include viscosity number, bulk density, and tensile or impact properties after a defined compression-moulding procedure. In applications involving a process temperature window of ±5 °C or a cooling-rate threshold, engineering trials on the target production press are required to establish acceptable limits because powder bed heat transfer changes with charge mass and geometry.

    Top