| HS Code | 357052 |
| Density | 0.958 g/cm³ |
| Melt Index 190 C 2 16 Kg | 0.15 g/10 min |
| Tensile Strength At Yield | 27.6 MPa |
| Tensile Strength At Break | 34.5 MPa |
| Elongation At Break | 800% |
| Flexural Modulus | 1.24 GPa |
| Environmental Stress Crack Resistance Escr | >1000 h |
| Vicat Softening Point | 124°C |
| Brittleness Temperature | < -70°C |
| Hardness Shore D | 66 |
| Thermal Conductivity | 0.45 W/m·K |
| Coefficient Of Linear Thermal Expansion | 1.1E-4 cm/cm/°C |
| Specific Heat | 2.3 J/g·°C |
| Water Absorption | <0.01% |
| Melting Point | 130°C |
| Crystallization Temperature | 115°C |
| Dielectric Constant | 2.3 |
| Dielectric Strength | 20 kV/mm |
| Volume Resistivity | >1E16 ohm·cm |
As an accredited Chevron Phillips Chemical HDPE LX8119 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Chevron Phillips Chemical HDPE LX8119 typically comes in 25 kg polyethylene-lined paper bags, palletized, or 1,000 kg bulk bags. |
| Container Loading (20′ FCL) | Chevron Phillips Chemical HDPE LX8119 loaded in a 20-foot FCL: 25kg bags on pallets, shrink-wrapped, labeled, secured for ocean export. |
| Shipping | Chevron Phillips Chemical HDPE LX8119 is a non-hazardous polyethylene resin, not regulated for transport by DOT, IMDG, IATA, or ADR. Ship in original sealed bags, supersacks, boxes, or bulk trucks/railcars. Keep dry, away from heat, sunlight, and contaminants. Avoid moisture and package damage. No special placards or UN number required. |
| Storage | Store Chevron Phillips Chemical HDPE LX8119 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep original packaging closed and off the floor to prevent moisture, dust, and contamination. Use first-in, first-out stock rotation. Maintain clean, segregated storage, avoid prolonged extreme temperatures, protect from UV exposure, and refer to the SDS for detailed guidance. |
| Shelf Life | HDPE LX8119: Shelf life not established; stable under normal storage. Store cool, dry, well-ventilated, away from direct sunlight and ignition sources. |
Chevron Phillips Chemical HDPE LX8119 is a hexene-copolymer high-density polyethylene with a nominal melt flow index of 0.45 g/10 min (ASTM D1238-20, 190 °C/2.16 kg) and solid density of 0.954 g/cm³ (ASTM D1505-18). The application set below excludes injection molding and pressure pipe because the melt flow, environmental stress crack resistance profile, and processing rheology do not align with those conversion methods. Each scenario identifies the governing compliance standard, additive letdown boundaries, production line configuration, and terminal article types.
| Scenario | Governing standard | Test designation / clause | Production boundary |
|---|---|---|---|
| Heavy-gauge sheet thermoforming | FDA 21 CFR 177.1520(c) where food contact is claimed; ASTM D1693-15 | ESCR condition B, F50 > 600 h | Regrind ≤ 30 wt%; sheet surface 160–175 °C |
| Large-part blow molded tanks | UN 31H1/Y, ASTM D1998-21 | Section 8 top-load retention at 50 °C | Melt ≤ 230 °C; regrind ≤ 25 wt% |
| Geomembrane sheet | GRI GM13, ISO 18553:2002 | Carbon black dispersion ≥ Category 9.0 | Thickness deviation ± 5%; die body ± 2 °C |
| Corrugated drainage pipe | AASHTO M294, ASTM F2648-21 | Pipe stiffness ≥ 320 kPa at 5% deflection | Carbon black 2.0–2.5 wt%; line speed ≤ 15 m/min |
| Marine structural profiles | ASTM G154-23, ASTM E84-23 | ΔE ≤ 3.0 after 1,000 h | Mineral filler ≤ 20 wt% |
In heavy-gauge sheet extrusion for thermoformed material-handling components, HDPE LX8119 is processed on a single-screw line with 90–150 mm barrel diameter, 30:1 L/D barrier screw, and screen pack no finer than 40/80/40 mesh to limit residence-time degradation. Melt temperature is maintained at 210–230 °C; die lips are set 2–4 mm wider than final sheet gauge. The cast roll stack operates at 80–95 °C for sheet thickness 4–12 mm. Thermoforming of the extruded sheet is carried out at 160–175 °C sheet surface temperature, with aluminum tooling held at 30–60 °C and vacuum pressure 0.4–0.7 MPa. For exterior service, a hindered amine light stabilizer masterbatch in HDPE carrier is let down at 2–4 wt%, and color concentrate is limited to 1–3 wt%; regrind from skeletal web and trim is incorporated at 20–30 wt% only after ESCR testing per ASTM D1693-15 condition B remains above 600 h. Compliance for industrial pallets and dunnage does not require food-contact clearance; where incidental contact exists, end users verify 21 CFR 177.1520(c) status with the converter. Finished part types include thermoformed pallet trays, machine enclosure panels, agricultural bin liners, truck bed liners, and dunnage sheets that are vacuum-formed after sheet reheating. Property verification is performed per ASTM D638-14 tensile yield, ASTM D790-17 flexural modulus, and ASTM D256-23 notched Izod impact at -40 °C for cold-storage handling.
Large-part blow molding of agricultural spray tanks and intermediate bulk containers uses the 0.45 g/10 min melt flow grade in reciprocating-screw extruders of 80–120 mm diameter and 24:1 L/D with grooved feed sections, feeding an accumulator head that delivers shot capacities up to 30 L without intermittent melt fracture. Melt temperature is kept at 200–220 °C; exceeding 230 °C lowers zero-shear viscosity sufficiently to produce parison sag on tools requiring shot times longer than 12 s. Die gap programming is used to compensate for 35–50% parison swell, and blow air pressure is maintained at 0.6–0.8 MPa with mold temperature 15–40 °C. For UV-exposed outdoor tanks, a 40% active UV stabilizer masterbatch is let down at 5–7 wt%, yielding 2.0–2.8 wt% total stabilizer concentrate; color concentrate is limited to 2 wt% to avoid excessive die swell. Post-industrial regrind is not recommended above 25 wt% unless the mixture is tested for ESCR per ASTM D1998-21 and top-load deformation at 50 °C. Chemical containment tanks are produced to UN 31A/Y or UN 31H1/Y when packaging Group II/III liquids, and the molded articles are production-testable by ASTM D1998-21 Section 8 for elevated-temperature wall thickness retention. End products include 100–500 L agricultural sprayer tanks, intermediate bulk container bottles, stationary chemical dosing tanks, and fuel-transfer tanks for non-road service. The resin is not recommended for continuous immersion in aromatic hydrocarbons above 40 °C without chemical resistance validation under ISO 175:2010.
Because exposed geomembrane sheet is specified under GRI GM13, HDPE LX8119 is converted on flat-die sheet lines targeting 1.0–3.0 mm smooth and textured liner stock for landfill caps, mining heap leach pads, and secondary containment. The extruder is configured at 120–150 mm diameter, 30:1 L/D, with a barrier screw and gear pump downstream; melt temperature is controlled at 220–240 °C and die body temperature is kept within ±2 °C of the melt to prevent transverse thickness deviation beyond ±5%. Carbon black is introduced as a 40% active HDPE carrier masterbatch at 5–6 wt% to achieve the 2.0–2.5 wt% final carbon black content required by GRI GM13 Section 6.1, and the dispersion rating must remain at or above Category 9.0 in ISO 18553:2002; lower dispersion produces microvoids that propagate to pinholes under installation stress. Antioxidant packages are compounded for 100,000 h service life in buried applications, but exposed liner stock requires additional UV stabilizer masterbatch at 3–5 wt% letdown. Peel adhesion for textured sheet is verified by ASTM D7004-03, and sheet-to-sheet weld strength is qualified by ASTM D6392-12 shear and peel tests after hot-wedge welding at 360–420 °C wedge temperature and 0.8–1.2 m/min travel speed. Finished products include smooth HDPE liner panels, one-sided or double-sided textured geonet-compatible membrane, and prefabricated boot and pipe penetration seals. Processors must reject any lot with moisture-induced splay; at warehouse relative humidity above 60%, hopper drying at 70 °C for 2 h prevents surface voids. Published data for this specific grade under 50-year geomembrane service is limited; project-specific creep rupture testing per ISO 899-1 or ASTM D2990 is required before anchor trench design. Chemical resistance for leachate service is validated using EPA 9090 compatibility testing before project specification.
In corrugated non-pressure drainage pipe production, HDPE LX8119 is applied only where the pipe cell classification under ASTM D3350 supports AASHTO M294 / ASTM F2648-21 requirements for agricultural drainage and culverts; pressure service is excluded because the grade is not listed as a PE100 material. Single-screw extruders of 60–90 mm diameter with grooved feed and 30:1 L/D run melt temperatures of 190–215 °C, feeding a rotating corrugator with vacuum sizing. The final carbon black content is maintained at 2.0–2.5 wt%, typically through a 40% carbon black masterbatch letdown of 5–6 wt%, to satisfy AASHTO M294 weathering. Impact strength after environmental stress cracking is checked by ASTM F2306-20 pipe stiffness and ASTM D1693-15 ESCR; pipe stiffness must remain above 320 kPa at 5% deflection for 100–300 mm diameters. Finished products include agricultural field drainage pipe, stormwater detention laterals, cable duct, and perforated leachate collection pipe for landfill cells. The resin is not specified for high-speed small-diameter tube lines above 15 m/min without adding process lubricant because melt fracture may develop at the corrugator entry.
Structural profile extrusion for dock fendering, bulkhead caps, and industrial wear strips uses HDPE LX8119 in 65–90 mm single-screw extruders with 28:1 L/D metering screws, melt temperature 195–215 °C, and vacuum calibration at -0.06 to -0.08 MPa for hollow or multi-chamber cross-sections. The formulation includes a UV stabilization masterbatch at 2–4 wt% and color concentrate at 2–3 wt%; calcium carbonate or talc filler may be added at 10–20 wt% to raise flexural modulus to 900–1,200 MPa (ISO 178:2019), but filler loadings above 20 wt% degrade ESCR below acceptable marine service limits. Coextruded cap layers may be used for color retention, with cap thickness 0.3–0.8 mm and total profile wall thickness 4–12 mm. Outdoor weathering qualification is performed under ASTM G154-23 cycle 1 for 1,000 h with ΔE not exceeding 3.0 for dark colors. Impact at freezing temperatures is verified by ASTM D256-23 notched Izod at -40 °C; cracking at stress concentrations is evaluated by bent-strip ESCR per ASTM D1693-15 condition B after 48 h conditioning in 10% Igepal solution. End product types include marine dock fender profiles, boardwalk planking clips, conveyor wear strips, and agricultural partition rails. Because HDPE LX8119 is not inherently flame-retardant, profiles used inside buildings must be evaluated against ASTM E84-23 surface burning characteristics; unfilled HDPE typically falls into Class C unless a fire-retardant additive is used, which would require revalidation of mechanical properties.
| Scenario | Additive / regrind | Letdown ratio | Final target | Constraint |
|---|---|---|---|---|
| Heavy-gauge sheet | UV HALS masterbatch; color concentrate; regrind | 2–4 wt%; 1–3 wt%; 20–30 wt% | ESCR > 600 h | Sheet surface 160–175 °C |
| Blow molded tanks | UV masterbatch; color; regrind | 5–7 wt%; ≤ 2 wt%; ≤ 25 wt% | Stabilizer concentrate 2.0–2.8 wt% | Melt ≤ 230 °C |
| Geomembrane | Carbon black masterbatch; UV masterbatch | 5–6 wt%; 3–5 wt% | Carbon black 2.0–2.5 wt% | Dispersion ≥ Category 9.0 |
| Drainage pipe | Carbon black masterbatch | 5–6 wt% | Carbon black 2.0–2.5 wt% | Line speed ≤ 15 m/min |
| Marine profiles | UV masterbatch; mineral filler | 2–4 wt%; 10–20 wt% | Flexural modulus 900–1,200 MPa | Filler ≤ 20 wt% |
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