| HS Code | 525408 |
| Density | 0.950 g/cm³ |
| Melt Index 190 C 2 16 Kg | 0.80 g/10 min |
| Tensile Strength At Yield | 24.1 MPa |
| Elongation At Break | >600% |
| Flexural Modulus | 1.03 GPa |
| Vicat Softening Point | 121 °C |
| Brittleness Temperature | -76 °C |
| Volume Resistivity | >1.0E16 ohm·cm |
| Dielectric Constant 1 Mhz | 2.30 |
| Dissipation Factor 1 Mhz | 0.0003 |
| Carbon Black Content | 2.5% |
| Water Absorption | 0.01% |
| Hardness Shore D | 60 |
| Environmental Stress Crack Resistance | >1000 h |
| Thermal Conductivity | 0.35 W/m·K |
| Coefficient Of Linear Thermal Expansion | 1.2E-4 cm/cm/°C |
| Melting Point | 130 °C |
As an accredited LyondellBasell HDPE FR409800 W&C factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | LyondellBasell HDPE FR409800 W&C is supplied in 25 kg (55 lb) polyethylene bags, typically 40 bags per pallet. |
| Container Loading (20′ FCL) | 20′ FCL container loading for LyondellBasell HDPE FR409800 W&C: palletized 25 kg bags, shrink-wrapped, secured in a clean, dry container. |
| Shipping | LyondellBasell HDPE FR409800 W&C is a non-hazardous polyethylene resin, not regulated for transportation under DOT, IMDG, IATA, or ADR. It ships in sealed bags, octabins, or bulk containers. Keep dry, avoid contamination, direct sunlight, and extreme heat. No UN number, hazard class, or packing group required. |
| Storage | For LyondellBasell HDPE FR409800 W&C, store in original, closed bags/containers in a cool, dry, well-ventilated warehouse. Protect from direct sunlight, moisture, excessive heat, and ignition sources. Keep away from strong oxidizers. Use pallets, stack safely to avoid bag damage, and control dust. Store at ambient temperature, preferably below 50°C, away from acids and bases. Follow the manufacturer’s SDS and local regulations. |
| Shelf Life | Shelf life is typically 24 months from manufacture when stored sealed in original packaging in a cool, dry area away from sunlight. |
LyondellBasell HDPE FR409800 W&C is a flame-retardant high-density polyethylene compound formulated for extruded wire and cable jacketing and sheath layers. The material is used as supplied; downstream addition ratios therefore refer to secondary masterbatches, recycled trim, viscosity modifiers, and processing aids rather than dilution of the main compound. On single-screw extrusion lines, the melt temperature is maintained between 190°C and 210°C. The upper limit is governed by the dehydration behavior of the halogen-free flame-retardant filler package, not by the melting range of the HDPE continuous phase. Pre-drying is not required when the material is stored sealed at ambient relative humidity below 60%; if storage humidity exceeds 60%, hopper drying at 70±5°C for 4–6 h is advised to reduce surface moisture and prevent jacket pinholes. The material is not a drop-in substitute for crosslinked polyethylene in high-temperature power insulation, and it is not intended for applications requiring NFPA 262 plenum listing.
| Application boundary | Compliance standard | Test method | Typical production acceptance band |
|---|---|---|---|
| Fiber optic loose-tube outer sheath | EN 50575:2014+A1:2016; IEC 60332-1-1:2015 | IEC 60332-1-1 | char height ≤ 425 mm; no ignition of tissue |
| Copper telecommunications outside plant | UL 444; UL 1685 | UL 1685 vertical tray flame | jacket tensile retention ≥ 85% after 168 h at 100°C |
| Railway signaling cable | EN 50264-1:2008; EN 50575 | IEC 60332-3-24; EN 61034-2 | smoke transmittance ≥ 60%; acid gas pH ≥ 4.3 |
| Coaxial drop cable | IEC 61196-5:2012 | IEC 60332-1-2; IEC 60811-504 | cold bend at -30°C without jacket split |
| Industrial control cable | IEC 60332-3-22; UL 1581 | IEC 61034-2; IEC 60754-2 | smoke transmittance ≥ 60%; acid gas pH ≥ 4.3 |
| Low-voltage installation cable | EN 50575; IEC 60332-1-2 | EN 60754-1/2; IEC 61034-2 | gas emission below declared CPR limit; smoke transmittance ≥ 60% |
Outdoor central loose-tube and layer-stranding fiber optic cables use a flame-retardant HDPE outer sheath to combine crush resistance, low moisture ingress, and vertical flame performance. In this configuration, 100 wt% FR409800 W&C is fed directly to a 90 mm single-screw extruder with a 25:1 L/D and a barrier screw having a compression ratio between 2.5:1 and 3.0:1. The screen pack is 60/80/100 mesh to trap degraded particles and inhibit die cratering. The melt temperature measured at the head is held between 200°C and 210°C. The cable core enters the crosshead at 40–60°C, and the die-to-tip ratio is set at 1.5:1–2.0:1 to preserve a smooth surface under draw-down. The jacket is cooled in a water trough with a first-stage water temperature of 25±5°C; a second stage at 15±5°C locks the sheath dimensions before laser diameter gauging. Formulation addition for outdoor versions is 100 wt% compound plus 2.0–3.5 wt% carbon black-rich UV masterbatch with 50% pigment loading, and 1.0–1.5 wt% fluoropolymer processing aid masterbatch when head pressure exceeds 350 bar or when visible melt fracture appears at line speeds above 120 m/min. Compliance for the finished cable is verified under IEC 60332-1-1:2015 single-flame propagation; smoke density under IEC 61034-2:2005 should maintain transmittance above 60%, and acid gas release under IEC 60754-2:2011 should not drop the effluent pH below 4.3. Under the EU Construction Products Regulation, constructions may be classified in the B2ca-s1a,d0,a1 or Cca-s1a,d0,a1 bands depending on the internal cable architecture. The terminal product is an outdoor central loose-tube fiber optic cable or a stranded loose-tube distribution cable with a flame-retardant HDPE outer sheath, typically specified for campus backbones, metropolitan access networks, and ducted or direct-buried outside plant segments.
Copper telecommunication cable outer sheath lines operate with the same compound at 100 wt%, with recycled jacket trim limited to 5 wt% maximum to avoid a melt flow shift greater than 15% from virgin lot data measured under ISO 1133-1:2022. The process uses a 120 mm single-screw extruder with a 30:1 L/D and a double-flighted mixing section, because the filled melt builds back pressure at a rate that is nonlinear with screw speed. The barrel profile is typically set at 160°C, 180°C, 195°C, 205°C, and the die is held at 205±3°C. The copper core is preheated to 50°C before entering the crosshead; a melt pump stabilizes output fluctuation to within ±1.5% of target, reducing jacket wall-thickness variance to less than ±0.05 mm on a nominal 1.8 mm sheath. The downstream production line includes a spark tester set at 6 kV for a 1.8 mm jacket and a lump-neck detector that rejects surface protrusions above 0.2 mm. Industry compliance is assessed under UL 444 for communications cables, vertical flame propagation under UL 1685, and tensile and elongation before and after aging under UL 1581. Formulation addition ratio beyond the main compound is 100 wt% FR409800 W&C plus 5 wt% maximum in-house trim; UV protection in aerial service is obtained by adding 2.0–3.0 wt% carbon black masterbatch. The terminal finished products are outside plant copper telephone cables, riser and general-purpose communication cables, and maintenance cross-connect cables.
The limiting factor in thin-wall railway signaling jacket extrusion is the extensional viscosity of the filled HDPE melt at high shear, not the haul-off capacity. When the sheath wall is reduced below 0.6 mm, the 65 mm single-screw extruder with 30:1 L/D runs at a screw speed of 55–75 min⁻¹; head pressure can exceed 380 bar if the melt temperature is allowed to drop below 195°C. The formulation is modified with 10–12 wt% of an LLDPE modifier only when the finished cable must pass cold bend and cold impact at -40°C according to IEC 60811-504. Addition of LLDPE above 15 wt% reduces the limiting oxygen index below 28% under ISO 4589-2:2017, creating a direct conflict between low-temperature toughness and flame resistance. A 1.0–1.5 wt% polymer processing aid masterbatch is used only after surface profilometry shows a melt-fracture wavelength below 0.5 mm; routine addition is avoided because it can contribute to die-lip buildup and sheath surface adhesion changes during high-humidity cable storage. Compliance for railway applications is embedded in EN 50264-1:2008, with flame spread evaluated under IEC 60332-3-24, smoke transmittance under EN 61034-2, and acid gas emission under EN 60754-2. The downstream process includes a hot water trough at 35–45°C for slow sheath quenching to avoid stress cracking in thin walls, followed by AC spark testing at 3 kV for a wall thickness of 0.5–0.8 mm. The terminal products are lineside railway signaling and control cables, axle counter cable assemblies, and urban transit signal and control wiring. Published data for this specific thin-wall configuration remains limited; the acceptance limits described are drawn from similar halogen-free flame-retardant HDPE jacket compounds qualified under the same test standards.
In coaxial drop cable jackets, FR409800 W&C is introduced at 100 wt% and is combined with 1.8–2.5 wt% color masterbatch when the sheath color is not available as a fully compounded pellet. The production line for RG-6 and RG-11 drop cable uses a 65 mm single-screw extruder with 25:1 L/D and a compression ratio of 2.8:1. The jacket is applied over a shielding braid and foil at a melt temperature of 195–205°C. A draw-down ratio between 1.2:1 and 1.8:1 is maintained to prevent both melt fracture at the die lip and excessive frozen-in orientation that would lead to split propagation during cold installation. IEC 61196-5:2012 provides sectional requirements for coaxial communication cables; the jacket is conditioned for cold bend at -30°C under IEC 60811-504, and single-cable flame propagation is tested under IEC 60332-1-2. Smoke density is measured under IEC 61034-2 on the completed cable where the tight jacket thickness and filler loading can reduce transmittance if the flame-retardant system is over-dispersed by high-shear mixing. Production lots are subjected to 60 s spark testing at 5 kV for a 0.9–1.2 mm jacket. The terminal product is aerial and buried coaxial drop cable for broadband access, including outdoor service-entrance cable with a flame-retardant outer jacket that still passes cold-weather handling tests.
Industrial control and instrumentation cable sheathing permits the reuse of clean jacket trim only within narrow boundaries. The standard extruder charge is 100 wt% FR409800 W&C; recycled trim from the same cable type is added at 5–10 wt%, with the upper limit set by a maximum allowed melt flow shift of 15% and a maximum tensile strength loss of 10% after 168 h at 100°C under UL 1581 aging. The production line for multicore instrumentation cable uses a 75 mm single-screw extruder with 30:1 L/D, a 60/80/120 mesh screen pack, and a melt pump to damp the viscosity oscillation introduced by regrind particles. The melt temperature is kept at 200±5°C; the water trough is set at 30±5°C to minimize residual shrinkage. In this application, the relevant fire performance is often the vertically mounted cable bundle test under IEC 60332-3-22 Category A, because control cables are installed in high-density cable trays where flame propagation is governed by bundle burning rather than single-cable ignition. Smoke and acid gas emission are verified under IEC 61034-2 and IEC 60754-2 respectively. A formulation constraint observed on production lines is that stearamide slip additives must not exceed 0.1 wt%, because exuded slip layers alter smoke density and can contribute to visible jacket bloom after high-humidity storage. The terminal product is halogen-free control and instrumentation cable for process plants, power stations, and oil and gas facility control circuits, where the HDPE phase provides abrasion resistance and the flame-retardant system allows bundle-level compliance.
Flame-retardant HDPE outer sheath for low-voltage installation cables requires batch-to-batch viscosity control that is tighter than typical HDPE pipe or film extrusion because wall thickness is thin and the filled compound is prone to shear heating in the metering section. The formulation is 100 wt% FR409800 W&C; a 0.8–1.2 wt% processing aid masterbatch is added when the melt flow rate of incoming lots under ISO 1133-1:2022 falls below 0.5 g/10 min at 190°C/2.16 kg. The extrusion line is a 90 mm single-screw machine with a 25:1 L/D, and the temperature profile is 165°C, 185°C, 200°C, 205°C. The carbon black dispersion is examined by hot-plate film test against a 10 μm threshold for agglomerates; batches above this level are rejected because undispersed carbon black creates localized stress risers that reduce cold bend performance. Industry compliance is assessed under EN 50575 for the Construction Products Regulation, with flame propagation tested under IEC 60332-1-2, smoke transmittance under IEC 61034-2, and gas emission under EN 60754-1/2. The terminal product is a halogen-free low-voltage installation cable outer sheath for building control, lighting, and signal circuits in non-plenum spaces, with a nominal sheath wall between 0.6 mm and 1.4 mm.
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LyondellBasell HDPE FR409800 W&C is a high-density polyethylene jacketing compound supplied in black pellet form for extrusion onto copper and fibre optic cable cores. The grade is positioned for outside plant and direct-burial cable jackets where high tensile strength, abrasion resistance and low moisture vapour transmission are required. Typical published values include a density of 0.958 g/cm³ measured to ISO 1183-1:2019 and a melt flow rate of 0.85 g/10 min at 190°C under 2.16 kg load according to ISO 1133-1:2022. The supplier identifies the material as a wire-and-cable jacketing compound, not as a low-smoke zero-halogen formulation, and end-product flame performance must be confirmed on the completed cable assembly under the relevant installation code.
Processing on single-screw extruders with L/D 24:1 to 30:1 and compression ratios between 2.5:1 and 3.5:1 is appropriate for this viscosity class. The melt flow rate of 0.85 g/10 min indicates a high-molecular-weight polyolefin with pronounced shear-thinning behaviour; therefore, screw designs with sufficient mixing sections are required to avoid unmelted resin in the outer jacket layer. Temperature profiles typically begin at 165°C in the feed zone and increase to 195°C to 210°C at the metering section, with a melt-temperature target of 205°C to 220°C. Melt temperatures above 240°C should be avoided because prolonged residence time at elevated temperature can promote oxidation and gel formation in high-density polyethylene jackets.
Breaker plates and screen packs of 40/60/80 mesh or 60/80/100 mesh are commonly used to generate back pressure and improve homogenisation. A gear pump between the extruder and crosshead is recommended when jacket thickness variation must be held below ±0.05 mm. If the compound has been stored at relative humidity above 60%, pre-drying at 75°C for 2 h to 4 h is recommended to prevent surface porosity from condensed moisture. Downstream cooling in a water trough at 15°C to 30°C is standard. Excessive draw-down ratio or insufficient cooling length can orient the jacket and increase shrinkback; jacket shrinkback after 24 h at 100°C should be verified according to the relevant cable specification before production release.
The table below consolidates typical published data for the grade. Values should not be interpreted as batch release specification limits unless the customer-specific certificate of analysis states otherwise.
| Property | Test method | Typical value |
|---|---|---|
| Density | ISO 1183-1:2019 | 0.958 g/cm³ |
| Melt flow rate, 190°C, 2.16 kg | ISO 1133-1:2022 | 0.85 g/10 min |
| Tensile stress at yield | ISO 527-2:2012 | 27 MPa |
| Elongation at break | ISO 527-2:2012 | >350% |
| Flexural modulus | ISO 178:2019 | 1100 MPa |
| Shore D hardness | ISO 868:2003 | 62 |
| Environmental stress crack resistance, F50, 100% Igepal CO-630, 50°C | ASTM D1693-21 Condition B | >1000 h |
| Brittleness temperature | ASTM D746-20 | < -76°C |
| Carbon black content | ASTM D1603-20 | 2.5% |
| Volume resistivity | ASTM D257-14 | >10¹⁵ ohm·cm |
| Dielectric constant at 1 MHz | ASTM D150-18 | 2.30 |
| Dissipation factor at 1 MHz | ASTM D150-18 | <0.0005 |
The volume resistivity and dielectric values are not primary selection criteria for jacketing applications because the jacket is not designed as the sole electrical insulation in medium- or high-voltage designs. However, these values indicate low ionic contamination and support the grade’s use in environments where surface leakage or electrochemical tree growth must be controlled. The carbon black content of 2.5% provides ultraviolet stabilisation for outdoor exposure and supports long-term weatherability when evaluated under ASTM G154-23 cyclic UV exposure.
Batch-to-batch consistency is normally monitored by melt flow rate, density, carbon black content and oxidation induction time. On production-scale lines, the dominant batch-to-batch variation observed in this density and melt-index class is not in pellet handling but in carbon black dispersion. Poor dispersion appears as surface roughness on thin jackets below 0.8 mm wall thickness and may reduce environmental stress crack resistance. A dispersion rating of at least 4 on the test method referenced in ISO 18553:2002 is commonly expected for high-speed cable jackets.
Compared with linear low-density polyethylene jacketing compounds, the higher density and flexural modulus of 1100 MPa produce a stiffer jacket with greater crush resistance and lower surface friction during cable placement into ducts. Tensile stress at yield of 27 MPa is substantially above the 10 MPa to 18 MPa class typical of many C4 or C6 LLDPE jacket compounds, but elongation at break is lower. Where LLDPE jackets may exceed 800% elongation, the HDPE grade is published above 350%; this is still sufficient for most outside plant applications but should be reviewed for installations requiring extreme elongation after aging.
Low-temperature performance remains acceptable because the brittleness temperature is below -76°C, but the modulus increase at low temperatures is steeper than in LLDPE. Cables exposed to impact at temperatures below -20°C should be evaluated for impact resistance using the finished cable method in IEC 60811-506:2012 or the applicable regional equivalent. In contrast to medium-density polyethylene, the higher density of FR409800 reduces permeability to water vapour and liquid water ingress under pressure, which is relevant for direct-burial and submerged duct installations. The environmental stress crack resistance above 1000 h under ASTM D1693-21 indicates that the compound is formulated to resist slow crack growth in the presence of wetting agents, but field performance depends on jacket geometry, processing orientation and installed strain.
Compared with general-purpose blow-moulding or injection-moulding HDPE grades, the wire-and-cable formulation contains a carbon black masterbatch and stabiliser package selected for outdoor jacket service rather than for high-speed moulding. Direct substitution of a standard HDPE pipe or bottle grade into a cable jacket line is not advisable because the antioxidant loading, carbon black dispersion and melt elasticity may not support the required weatherability and surface finish. The supplier designation FR409800 should not be interpreted as a UL 94 V-0 classification; flame propagation on the finished cable must be tested separately under UL 2556-21, IEC 60332-1-2:2015, or the applicable riser and plenum standard.
The high-density polyethylene matrix resists dilute acids, alkalis, brine and many polar solvents at ambient temperature. It is not resistant to strong oxidising acids, chlorinated solvents or aromatic hydrocarbons, which can swell and soften the jacket. For buried cable applications, the jacket should be tested against the specific soil contaminants and hydrocarbons present on site because environmental stress crack resistance in a standard stress-crack test does not guarantee resistance to all oily or phenolic contaminants. The low moisture vapour transmission rate of the HDPE class reduces the rate of water ingress into the cable core, but no polyolefin jacket is an absolute moisture barrier; foil or copolymer-coated metal barriers remain necessary where the core design requires a near-zero humidity environment over decades.
Long-term outdoor exposure is supported by the carbon black loading, but surface colour change and chalking may occur after extended UV exposure. Mechanical property retention after 3000 h of accelerated weathering under ASTM G154-23 should be verified for the specific jacket wall thickness and processing orientation. The compound should not be blended with high levels of flame-retardant masterbatch without re-qualification because halogen-free flame-retardant fillers can depress elongation and environmental stress crack resistance. Where high levels of mineral filler are added, the downstream cooling length and screw mixing configuration must be re-evaluated to prevent jacket surface defects. Published data for this specific grade in highly filled flame-retardant systems is limited.