Products

LyondellBasell HDPE XL5906WC

    • Product Name: LyondellBasell HDPE XL5906WC
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    VTB
    Specifications
    HS Code 503998
    Density 0.959 g/cm³
    Melt Index 190 C 2 16 Kg 0.9 g/10 min
    Tensile Strength At Yield 26.2 MPa
    Tensile Strength At Break 30.3 MPa
    Elongation At Break 600%
    Flexural Modulus 1170 MPa
    Vicat Softening Temperature 126 °C
    Brittleness Temperature -70 °C
    Environmental Stress Crack Resistance >1000 h
    Volume Resistivity >1E15 ohm·cm
    Dielectric Constant 2.3
    Dissipation Factor 0.0002
    Hardness Shore D 65
    Water Absorption <0.01%
    Carbon Black Content 2.5%
    Melting Point 130 °C
    Thermal Conductivity 0.4 W/m·K
    Coefficient Of Linear Thermal Expansion 120 µm/m·°C
    Oxidative Induction Time >30 min
    Moisture Content <0.1%

    As an accredited LyondellBasell HDPE XL5906WC factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing LyondellBasell HDPE XL5906WC is supplied in 25 kg polyethylene bags, 55 bags per pallet (1,375 kg total).
    Container Loading (20′ FCL) Container Loading (20′ FCL) for LyondellBasell HDPE XL5906WC: 25 kg bags, floor-loaded, dry container, secure stowage, approx. 18 MT net.
    Shipping LyondellBasell HDPE XL5906WC is shipped as non-hazardous polyethylene pellets in 25 kg bags, octabins, or bulk trucks/railcars. It requires no special transport placards. Store dry, away from direct sunlight, heat, and contaminants. Follow the SDS and local shipping regulations.
    Storage Store LyondellBasell HDPE XL5906WC in a cool, dry, well-ventilated warehouse. Keep original bags or containers closed, palletized, and off the floor. Protect from direct sunlight, heat, flames, moisture, dust, and contamination. Avoid prolonged high temperatures. Stack safely to prevent deformation or package damage. Use first-in, first-out rotation. Follow the SDS and local storage regulations.
    Shelf Life The shelf life is 2 years from date of manufacture when stored in original packaging in a dry, cool, well-ventilated area.
    Application of LyondellBasell HDPE XL5906WC

    In thin-wall insulation for low-voltage control cable, LyondellBasell HDPE XL5906WC is fed to a 24:1 to 30:1 L/D single-screw extruder fitted with a barrier screw and a 60/100/60 mesh breaker plate. Conductor preheat at 80–120 °C is maintained before the crosshead to reduce quench shock and improve circumferential wall thickness uniformity. Melt temperature measured at the die is held within 200–225 °C, while head pressure is kept below 45 MPa to limit residence-time degradation. The molten tube is drawn onto the conductor at a draw-down ratio of 1.5:1 to 3.0:1 and quenched in a water trough at 18–25 °C. Finished insulation is evaluated for tensile strength and elongation at break under IEC 60811-501, and heat shock resistance under IEC 60811-502. Shrinkback after ageing is measured according to IEC 60811-502 at 100 °C for 1 h; values above 2% are generally rejected for dense-wall HDPE insulation in cable constructions where back-twisting or connector insertion is required. The terminal product is a flexible control cable used in machine tools, conveyor systems, and industrial automation. In silane-crosslinked versions, a masterbatch containing vinylsilane and peroxide is absorbed or compounded into the melt; moisture-curing then proceeds in a sauna or water bath at 80–95 °C for 6–12 h. Excessive water carry-over into the extruder hopper from recycled edge trim is a known source of pre-crosslinking and die-buildup in this process. At ambient relative humidity above 60%, the pellets are dried at 80 °C for 2 h in a desiccant dryer before silane-grafted formulations are processed.

    PropertyTest MethodTypical Measurement Condition
    Melt flow rateISO 1133-1:2022190 °C / 2.16 kg
    DensityISO 1183-1:201923 °C, water displacement
    Tensile strengthIEC 60811-501250 mm/min
    Elongation at breakIEC 60811-501250 mm/min
    Heat shockIEC 60811-502100 °C, 1 h
    Environmental stress crackingASTM D169350 °C, 10% Igepal CO-630
    Carbon black dispersionASTM D5596Microtome section, 100×

    What Limits Line Speed in Automotive Primary Wire Extrusion?

    For thin-wall automotive primary wire insulation, the extrusion line is typically configured with a 50 mm single-screw extruder and a dual-zone water trough capable of stepped cooling. The limiting variable is not melt output but insulation eccentricity and spark-test survival. The crosshead is operated with a tip draw of 0.15–0.35 mm and a die diameter selected for a draw ratio balance near 1.0; deviations greater than ±0.05 produce uneven wall thickness in 0.2 mm-class insulation. Conductor preheat is set at 100–140 °C. If preheat is insufficient, the insulation freezes before it shrinks onto the copper, reducing interface friction and allowing longitudinal movement during harness assembly. The compound is processed at 210–230 °C melt temperature. In peroxide-crosslinkable HDPE, the screw temperature profile must not exceed 120 °C before the compression section, otherwise scorch particles appear in the insulation and cause spark-test failures at 2.5 kV to 5 kV AC. Crosslinking is completed by passing the insulated conductor through a high-pressure steam tube or dry-curing section at 180–200 °C. Finished automotive primary wire is tested under ISO 6722-1 for short-term ageing at 150 °C for 4 h, and the insulation is examined for cracking after winding at specified mandrel diameters. In engine-bay harness applications, the formulation is also evaluated for resistance to hot diesel fuel, engine oil, and battery acid according to the fluid resistance clauses of ISO 6722-1. If the grade is run as a thermoplastic HDPE without crosslinking, the maximum continuous conductor temperature is typically limited to 75 °C, rising to 125 °C in crosslinked designs.

    Fiber Optic Loose-Tube Buffer Extrusion and Gel Compatibility.

    In loose-tube optical cable production, HDPE XL5906WC is extruded as a thin-walled tube around a thixotropic filling grease and a set of coloured optical fibres. The line uses a 60 mm single-screw extruder equipped with a vacuum-calibration tank and a laser diameter gauge. Melt temperature is held between 210 °C and 235 °C, and the tube is quenched in 18–22 °C water to limit post-extrusion shrinkage. Buffer tube shrinkage is measured after 24 h at 80 °C; typical acceptance limits are below 1.0% for cables subjected to temperature cycling under IEC 60794-1-2. The grade’s density and molecular weight distribution affect tube crush resistance and gel compatibility. Polycarbonate or polybutylene terephthalate fibres are sensitive to excess processing oils; the HDPE compound should be formulated without migratory lubricants exceeding 0.05 wt% of the final compound. In long-haul cable designs, the buffer tube must survive hot water filling compound contact at 70 °C for 10 days without stress cracking, evaluated under ASTM D1693 or IEC 60794-1-2. The terminal product is a fibre-optic cable used in duct and aerial installations. A production constraint is die build-up from fused gel residues; the tooling is cleaned at intervals not exceeding 8 h when running filled tubes. If the grade is crosslinkable, moisture-curing can be applied to improve dimensional stability, but the cure must be completed before stranding to avoid excessive tube stiffness.

    For buried cable protection ducting, the HDPE melt is extruded into a corrugator with vacuum forming blocks immediately downstream of the die. A 75 mm single-screw extruder with a length-to-diameter ratio of 30:1 feeds a side-fed die at 200–220 °C. The corrugator speed is matched to melt output to maintain a wall thickness of 0.8–1.2 mm at the root of the corrugation and 0.6–0.9 mm at the crest. Haul-off tension is controlled to avoid thinning at the inner radius. Finished ducting is evaluated for compression at 23 °C and -5 °C under EN 61386-1, and impact resistance is measured by falling-weight impact at -20 °C using a 2 kg striker. For outdoor cable protection, carbon black content is set between 2.0 wt% and 4.5 wt% in the final compound, with dispersion tested under ASTM D5596. The product is used as underground conduit for power and telecom cables, and as inner duct in microduct bundles. A recurrent processing bottleneck is corrugator vacuum loss, which produces collapsed ribs; vacuum levels below -20 kPa are corrected by cleaning the forming blocks. Published data for this specific configuration is limited; trial runs are required to define the maximum line speed for a given die gap. Regrind from start-up scrap is added at up to 10 wt% when the final duct requires smooth internal walls and consistent low-temperature impact.

    When Carbon Black Disperses Poorly in Outdoor Jacket Compounds

    In outdoor cable jackets based on HDPE XL5906WC, carbon black masterbatch addition is preferable to neat powder addition because of dust and dispersion control. A letdown ratio of 4:1 to 6:1 using a 45% carbon black masterbatch in the same polyethylene carrier is typical, yielding 2.0–2.5 wt% carbon black in the final jacket. The masterbatch is metered into the throat of a 60 mm single-screw extruder, and the screw is expected to contain at least one shear mixing section beyond the compression zone. Dispersion is assessed under ASTM D5596; agglomerates larger than 15 μm in a 0.5 mm jacket are visible as micro-voids after tensile elongation and can reduce weathering resistance. The jacket is extruded over the cable core at a draw-down ratio between 1.2:1 and 2.0:1. Cooling water temperature is held at 15–20 °C to minimise jacket ovality. The final sheath is subjected to UV exposure per ASTM D2565 using UVA-340 fluorescent lamps, and tensile elongation retention is recorded after 1000 h and 2000 h. In low-smoke zero-halogen formulations, a metal hydroxide loading below 150 phr is used; higher loadings make the melt less extensible and increase die pressure above 40 MPa. The terminal product is an outdoor aerial or duct cable jacket for power and telecommunications lines. In silane moisture-cure systems, the presence of carbon black can reduce the residual peroxide concentration; the graft initiator level is adjusted by jar-mould trials before production.

    In submersible pump cable sheathing, HDPE XL5906WC is selected for resistance to water absorption and abrasion. The cable is produced by extruding a dense outer sheath over polypropylene-insulated conductors in a single pass through a 90 mm single-screw extruder with a compression ratio of 3.0:1. Melt temperature is kept at 215–230 °C. The sheath wall is drawn down from a 2.0 mm die gap to a final thickness of 1.2–1.5 mm; the haul-off capstan speed is limited by the hot tear strength of the melt. Water absorption is measured after 24 h at 23 °C under ISO 62; HDPE of this density class typically exhibits values below 0.01% by mass, but the specific certificate of analysis should be consulted. The finished cable is tested under IEC 60092-353 if it is intended for shipboard or offshore pumping duty. If the sheath is crosslinked, the cable can be subjected to hot water at 90 °C for 1000 h without cracking. This application boundary is limited by the adhesion of the sheath to the underlying insulation; excessive adhesion makes field stripping difficult and is evaluated by peel tests on a 25 mm wide strip at a pull speed of 100 mm/min. For continuous immersion service, the compound should be formulated with a hindered phenol antioxidant and a metal deactivator, not with amine-based heat stabilisers, which accelerate copper-catalysed oxidation.

    Free Quote

    Competitive LyondellBasell HDPE XL5906WC 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

    LyondellBasell HDPE XL5906WC is supplied as a black, high-density polyethylene compound formulated for peroxide-crosslinked wire and cable insulation. The “XL” prefix designates crosslinkable behavior; “WC” identifies the wire and cable service segment. Producer technical literature lists a nominal density of 0.941 g/cm³ by ASTM D1505 and a melt flow rate of 0.6 g/10 min under ASTM D1238 at 190 °C and 2.16 kg. Carbon black content is approximately 2.5 wt% by ASTM D1603. The grade is intended for subsequent free-radical crosslinking, which converts the semicrystalline thermoplastic into a network structure with improved creep resistance at elevated temperature. Compared with low-density polyethylene-based XLPE, the high-density backbone increases hardness and tensile strength while reducing low-temperature flexibility. The compound is not a direct replacement for unfilled HDPE pipe or blow molding resins because its additive package and melt rheology are optimized for crosshead extrusion and cure.

    What Process Differences Separate XL5906WC From General-Purpose HDPE Extrusion and Molding Grades?

    The distinction begins with melt flow. A typical injection molding HDPE may exhibit a melt flow rate between 4 g/10 min and 12 g/10 min at 190 °C and 2.16 kg; XL5906WC is specified at 0.6 g/10 min. The lower flow improves melt integrity during crosshead extrusion, reduces draw-down after the die, and limits conductor eccentricity, but it also increases screw torque and residence-time sensitivity. Compared with an HDPE blow molding grade having melt flow below 0.1 g/10 min, XL5906WC is more flowable and suitable for thin-wall insulation, yet retains sufficient molecular weight to resist conductor imprint during reeling. The 2.5 wt% carbon black loading differentiates it from unfilled HDPE pipe grades: the filler raises viscosity, increases die pressure, and requires breaker-plate screens with adequate active area to prevent pressure excursions. The additive package also includes antioxidant stabilizers intended to delay oxidative degradation during extrusion and long-term thermal ageing.

    Compared with low-density polyethylene-based XLPE compounds, XL5906WC has a higher crystalline melt temperature and higher tensile modulus, but lower stress-crack resistance in sub-zero applications. It should not be regarded as a direct substitute for semiconductive or jacket compounds where high elongation and low-temperature flexibility dominate. The high-density structure also influences peroxide uptake and crosslink density: XL5906WC generally requires controlled peroxide addition because the higher crystallinity reduces amorphous-phase mobility during cure.

    In wire and cable extrusion, the material is typically processed on a single-screw extruder with a crosshead die. If XL5906WC is run without peroxide, barrel temperatures may be profiled from 150 °C in the feed zone to 210 °C in the metering zone, with melt temperature at the die maintained below 220 °C. When a peroxide masterbatch is metered into the throat for cure, melt temperature must be reduced below 130 °C because dicumyl peroxide exhibits a half-life of approximately 1 min at 171 °C. Processing guidance for comparable crosslinkable HDPE compounds recommends a 24:1 L/D screw with a compression ratio from 2.5:1 to 3:1 and a shallow metering section to limit frictional heating. Production-scale observations show that carbon black agglomerates can accumulate on screen packs, producing pressure excursions greater than 0.5 MPa at the breaker plate; these excursions correlate with melt-temperature spikes and localized scorch in the crosshead. Pre-drying at 80 °C for 4 h is advised when storage relative humidity exceeds 60%, because surface moisture carried by carbon black can generate voids and reduce insulation breakdown strength.

    Crosslinking is commonly measured as gel fraction by decalin or xylene extraction. For peroxide-cured HDPE cable insulation, a gel fraction above 70% is generally required to achieve acceptable hot-set behavior. In hot-set testing according to IEC 60811-507, fully cured specimens under 0.2 MPa at 200 °C should exhibit elongation below 175% and permanent set below 15% after cooling. Published data for XL5906WC specifically may vary with peroxide type, dose, and extrusion thermal history; the compound must be qualified in the end-product cable design.

    Mechanical, Thermal, and Electrical Property Benchmarks

    The values in the following table are representative of producer technical data and material-class measurements for XL5906WC. They apply to test specimens prepared by compression molding or extrusion under the indicated methods and do not replace end-product certification.

    Representative property data for LyondellBasell HDPE XL5906WC
    PropertyTest methodTypical value
    DensityASTM D15050.941 g/cm³
    Melt flow rateASTM D1238 (190 °C/2.16 kg)0.6 g/10 min
    Tensile strength at breakASTM D63824.1 MPa
    Elongation at breakASTM D638750%
    Low-temperature brittlenessASTM D746< -76 °C
    Carbon black contentASTM D16032.5 wt%
    Shore D hardnessASTM D224065
    Dielectric constantASTM D150 at 1 MHz2.5
    Dissipation factorASTM D150 at 1 MHz0.0005
    Volume resistivityASTM D2571×1016 Ω·cm

    Electrical performance is strongly influenced by moisture, carbon black dispersion, and cure state. Because the grade contains 2.5 wt% carbon black, dispersion quality affects dielectric strength and dissipation factor. The reported dielectric constant and dissipation factor are meaningful only for dried, fully compounded, and properly cured specimens. Water immersion, poor dispersion, or under-cure can increase losses and reduce breakdown strength.

    When Crosslinking Is Omitted or Inhibited, Which Failure Mechanisms Appear First?

    Without peroxide cure, XL5906WC retains the thermoplastic behavior of HDPE; the Vicat softening point is near 120 °C, but continuous load-bearing capacity begins to decline above 60 °C. Creep rupture in uncrosslinked HDPE can occur at stresses well below the short-term yield strength. In crosslinked form, the network structure suppresses large-scale chain sliding and reduces creep elongation under constant load. If cure is inhibited—for example, by addition of amine-based flame retardants that act as free-radical scavengers—the gel fraction may fall below 60%, and hot-set elongation may exceed 175% or fail entirely. Such under-cured insulation is prone to conductor indentation, shrinkage during overcurrent cycling, and reduced short-circuit temperature capability.

    Processors should also limit direct exposure to strong oxidizing acids and high concentrations of chlorine at elevated temperatures; these environments attack the polyethylene backbone and can reduce elongation retention after ageing. For applications requiring flame resistance, the base resin must be combined with appropriate flame-retardant additives and tested as a complete cable construction. XL5906WC alone is not flame-retardant to a vertical-flame cable test such as UL 1581 VW-1 or equivalent.

    Regulatory status at the resin level is separate from finished-cable compliance. XL5906WC is manufactured to support resin-level documentation under REACH and RoHS, but end-product compliance with EU Directive 2011/65/EU depends on the final compound and cable assembly. For US wire and cable constructions, qualification is typically performed against UL 44 or UL 83 after extrusion and crosslinking. The producer’s raw-material documentation does not replace these end-product listings. Pipe and food-contact standards such as NSF/ANSI 61 or FDA 21 CFR 177.1520 are not applicable to the carbon black and antioxidant package in this wire and cable grade.

    The following comparative table places XL5906WC alongside generic LDPE-based XLPE and general-purpose HDPE injection material classes. The values are class-typical and are not identical to any single commercial equivalent.

    Comparative profile across material classes
    PropertyXL5906WCLDPE-based XLPEGeneral-purpose HDPE injection
    Density0.941 g/cm³0.920 g/cm³0.953 g/cm³
    Melt flow rate0.6 g/10 min2 g/10 min8 g/10 min
    Tensile strength at break24.1 MPa18 MPa28 MPa
    Elongation at break750%600%30%
    Carbon black content2.5 wt%0–2.5 wt%0 wt%
    Shore D hardness655068

    The comparative data show that XL5906WC occupies a middle position between soft LDPE-based XLPE and rigid injection HDPE. It retains the high tensile strength of HDPE while its elongation at break remains closer to that of LDPE-based XLPE. The carbon black loading provides ultraviolet stabilization but does not make the compound semiconductive; at 2.5 wt%, volume resistivity remains above 1×1015 Ω·cm. This differentiates it from conductor-shield compounds, which commonly use carbon black loadings above 30 wt% and volume resistivity below 1×103 Ω·cm.

    In practice, XL5906WC is selected for thin-wall primary insulation where higher hardness and conductor-imprint resistance are required than LDPE-based XLPE can provide. It is not intended for direct-burial jacketing without an outer protective layer, nor for use with amine-based flame retardants unless the cure system is reformulated. Downstream fabricators must verify melt temperature, gel fraction, hot-set performance, and ageing retention under the specific cable standard being claimed, because raw-material property values do not transfer automatically to finished insulation. Published data for this specific configuration is limited in public literature; qualification should therefore be based on producer technical service data and full-scale extrusion trials.

    Top