| HS Code | 718493 |
| Polymer Type | High Density Polyethylene (HDPE) |
| Density | 0.950 g/cm³ |
| Melt Flow Rate | 0.086 g/10 min (190°C/2.16 kg) |
| Hardness Shore D | 62 |
| Tensile Strength At Yield | 26.0 MPa |
| Tensile Strength At Break | 30.0 MPa |
| Elongation At Break | >=600% |
| Flexural Modulus | 1.10 GPa |
| Izod Impact Notched | 0.160 J/cm |
| Vicat Softening Point | 126°C |
| Brittleness Temperature | -70.0°C |
| Environmental Stress Crack Resistance | >1000 hr |
| Thermal Conductivity | 0.350 W/m·K |
| Specific Heat | 1.90 J/g·°C |
| Melt Temperature | 130°C |
As an accredited LyondellBasell HDPE 50-0863 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | LyondellBasell HDPE 50-0863 is supplied in 25 kg (55 lb) polyethylene bags, 40 bags per pallet, totaling 1,000 kg. |
| Container Loading (20′ FCL) | Loading LyondellBasell HDPE 50-0863 into a 20′ FCL container: palletized bags, shrink-wrapped, secured, and ready for sea export. |
| Shipping | LyondellBasell HDPE 50-0863 ships as non-hazardous polyethylene resin pellets in 25 kg bags, bulk boxes, or bulk trucks/railcars. It is not regulated by DOT, IMDG, or IATA. Store cool, dry, and clean, away from ignition sources, moisture, and direct sunlight; prevent package damage and contamination. |
| Storage | Store LyondellBasell HDPE 50-0863 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep original bags or containers closed to prevent moisture, dust, and contamination. Avoid prolonged UV exposure and extreme temperatures. Protect from physical damage. Use first-in, first-out inventory rotation. Do not store near strong oxidizing agents. |
| Shelf Life | Typically 24 months from manufacture when stored in original unopened packaging, dry, cool, away from direct sunlight, and below 50°C. |
Thin-wall food-contact packaging produced from HDPE 50-0863 is molded at a nominal melt flow rate of 8 g/10 min under ISO 1133-1:2022, a value that permits fill-time reductions in 24- to 64-cavity stack tools but narrows the acceptable hold-pressure window. In a representative high-cavitation tool with valve-gate hot runners and cavity wall thickness between 0.8 mm and 1.5 mm, the melt temperature is maintained at 190°C to 220°C; mold cooling circuits are held at 10°C to 30°C, and peak injection pressure ranges from 80 MPa to 120 MPa. The compound consists of 100 phr HDPE 50-0863, 2–4 wt% white or custom color masterbatch, 0.5–1.5 wt% nucleating masterbatch, and 0.05–0.2 phr antioxidant. Nucleating additions above 1.5 wt% are avoided because notched impact resistance measured under ISO 179-1/1eA may fall below the level required for fill-line drop tests. In stack molds with sub-1.0 mm wall sections, valve pin sequencing must be delayed by 0.5–1.0 s to prevent premature gate freeze; premature freeze at the gate produces short shots in distal cavities even when cavity pressure sensors report adequate pack at the near-gate location. Compliance for direct food contact is established under 21 CFR 177.1520, EU Regulation 10/2011 with an overall migration limit of 10 mg/dm² under Annex V, and GB 9685-2016 for additive allowances. Pre-drying is not normally required for the neat resin; however, surface condensation on silo-stored material during high-humidity cycles should be removed by a 1–2 h hold at 80°C before processing to prevent splay in thin-wall fill sections. Terminal parts include single-serve condiment cups, delicatessen bowls, dairy spread containers, and thin-wall food-storage boxes.
Beverage and dairy closure production with this grade is concentrated in 64- to 128-cavity hot-runner molds with cycle times between 4.0 s and 7.0 s, where gate diameter, cooling water temperature, and slip agent loading interact with gate-seal time. The base formulation is 100 phr HDPE 50-0863, 0.05–0.2 phr primary antioxidant, 0.5–1.5 wt% color masterbatch, and 1.0–2.0 wt% erucamide slip masterbatch. In contact-sensitive applications requiring organoleptic neutrality, slip loading is reduced to 0.3–0.8 wt% and a lower-torque liner seal is used instead of high-slip surface modification. Melt temperature is set at 200°C to 230°C, cooling water at 8°C to 14°C, and pin opening sequenced to avoid core deflection during ejection. When slip masterbatch exceeds 2.0 wt%, plate-out on core surfaces increases ejection force and can reduce print adhesion on the closure top; torque retention after 24 h at 40°C is checked under ISO 16047:2015 or ASTM D3198-97. Regulatory alignment includes 21 CFR 177.1520 and EU Regulation 10/2011 for food-contact closures, USP chapter 661.1 for pharmaceutical closures when applicable, and ISO 8317:2015 for child-resistant closure systems. Terminal products are water and juice beverage closures, dairy snap caps, detergent and personal-care flip-top caps, and pharmaceutical closure shells.
Open-head pails from 1 L to 20 L and jerrycan bodies from 5 L to 30 L are molded with wall thicknesses of 1.8 mm to 3.5 mm on 600- to 1600-tonne injection molding machines. The formulation uses 100 phr HDPE 50-0863, 2–3 wt% UV-stabilized color masterbatch, and up to 20 wt% clean post-industrial regrind when food-contact statutes do not apply. Carbon black masterbatch concentration is held at 2.0–2.5 wt% for outdoor weathering resistance; lower loadings often produce opacity below the level defined in customer specifications for UV protection and surface uniformity. Processing uses melt temperatures between 200°C and 230°C, mold temperatures of 10°C to 25°C, and sequential valve gating with a 0.5–1.0 s delay across the flow front to move the knit line away from handle bosses and pail attachment features. The critical compliance anchor for dangerous-goods pails is UN 1H2 performance under Chapter 6.1 of the UN Model Regulations and ADR 6.1.5, which includes drop testing at -18°C or lower conditioned loads and hydrostatic pressure retention. Standard physical property tests for batch release include density by ISO 1183-1:2019, melt flow rate by ISO 1133-1:2022, tensile yield by ISO 527-2, and notched Charpy impact by ISO 179-1. Regrind levels above 20 wt% are operationally discouraged for UN-certified pails because batch-to-batch variance in low-temperature impact can shift drop-test performance toward the failure threshold. Terminal parts include open-head industrial pails, paint buckets, ink cans, lubricant and grease pails, and jerrycan bodies for non-hazardous liquid transport.
Returnable beverage crates and logistics totes are molded from HDPE 50-0863 with wall sections of 2.0 mm to 4.0 mm and rib heights up to 8.0 mm; the key process risk is sink formation at rib intersections, which is controlled by maintaining packing pressure at 50 MPa to 70 MPa for 5–12 s depending on wall thickness and gate geometry. The typical compound is 100 phr resin, 2–4 wt% UV-stabilized masterbatch, 0.2–0.5 phr antistatic concentrate, and 10–15 wt% process regrind. Melt temperatures are set at 190°C to 220°C, mold temperatures at 15°C to 30°C, and injection speed is profiled to avoid jetting in deep rib sections and corner junctions. Industrial washing systems at 60°C with 0.5–2.0% sodium hydroxide are used for returnable logistics; repeated thermal-mechanical cycling beyond 200 cycles can reduce Charpy impact by up to 15%, so the regrind ratio is limited and fresh stabilizer is added when recycled content is introduced. Compliance is anchored to EN 13117-1:2000 for reusable rigid plastic distribution boxes, RoHS 2011/65/EU for heavy metal restrictions, and REACH SVHC declarations. Mechanical acceptance tests include flexural modulus under ISO 178:2019 and notched impact under ISO 179-1/1eA. Terminal products include bottle crates, bread trays, agricultural harvest crates, fish handling totes, and general logistics boxes.
Automotive fluid reservoirs below 3 L internal volume, including washer reservoirs and coolant overflow bottles with molded-in bracket features, are produced from HDPE 50-0863 when the part design requires injection molding instead of continuous blow molding. The material is compounded with 100 phr resin, 0.5–1.5 wt% carbon black masterbatch for UV stability, 0.1–0.3 phr hindered-amine light stabilizer, and 0.05–0.2 phr processing stabilizer. Melt temperatures are held at 200°C to 230°C; mold temperature is kept at 15°C to 30°C, and weld-line strength is protected by locating gate lands away from wall transitions with an overlap angle greater than 45° between flow fronts. Long-term hydrostatic pressure resistance and thermal cycling performance are validated under customer-specific OEM specifications rather than a single ISO standard; generic exposure tests often reference ISO 22088-1 for environmental stress cracking. Compliance for interior and under-hood materials requires REACH, RoHS 2011/65/EU, and in many cases OEM material standards that remain proprietary. Low-temperature Charpy notched impact testing under ISO 179-1 at -30°C is used to screen batches; published data for this specific configuration is limited. Terminal parts include injection-molded washer reservoirs, coolant overflow bottles, and bracket-integrated fluid tanks.
Houseware and small appliance parts made from HDPE 50-0863 include storage boxes, waste containers, and appliance housings where dimensional stability after 24 h at 50°C is more critical than extreme impact toughness. The formulation uses 100 phr resin, 1.5–4.0 wt% color masterbatch, 0.2–0.5 wt% antistatic concentrate, and up to 15 wt% clean post-industrial regrind. Molders using less than 2 wt% masterbatch let-down may observe color variation along flow lines in parts with wall thickness below 1.5 mm; this is due to inadequate distributive mixing in machines with screw L/D below 18:1. Processing uses melt temperatures of 180°C to 215°C, mold temperatures of 20°C to 40°C, injection pressures of 70 MPa to 110 MPa, and pack times adjusted to gate-seal based on part weight stabilization. Food-storage items must comply with 21 CFR 177.1520 and EU Regulation 10/2011; non-food articles are assessed under REACH and the RoHS Directive 2011/65/EU. Dimensional shrinkage is evaluated after 48 h at 23°C ± 2°C and 50% relative humidity using ISO 294-4:2018; batch acceptance frequently uses a 24 h at 50°C heating test to simulate warehouse conditions. Terminal products include modular storage totes, waste bins, small appliance housings, and HDPE drawer systems.
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LyondellBasell HDPE 50-0863 is a high-density polyethylene resin supplied in pellet form. The nominal density is 0.950 g/cm³ when tested according to ASTM D1505, and the melt flow index is 0.63 g/10 min when tested according to ASTM D1238 at 190 °C under a 2.16 kg load. The same melt flow index may be reported under ISO 1133-1:2022 using the equivalent 190 °C/2.16 kg condition. The grade is positioned between low-melt-flow blown-film resins and high-melt-flow injection-molding resins, and the resulting balance of melt strength and drawability supports sheet extrusion, profile extrusion, and heavy-gauge thermoforming. The property values in the following table are representative published values for the natural grade; certificates of analysis and lot-specific data should be obtained for production qualification.
| Property | Typical Value | Test Method |
|---|---|---|
| Density | 0.950 g/cm³ | ASTM D1505 |
| Melt flow index | 0.63 g/10 min | ASTM D1238 |
| Tensile strength at yield | 26.2 MPa | ASTM D638 |
| Tensile elongation at break | 600% | ASTM D638 |
| Flexural modulus | 1,170 MPa | ASTM D790 |
| Vicat softening temperature | 124 °C | ASTM D1525 |
| Shore D hardness | 65 | ASTM D2240 |
| Notched Izod impact, 23 °C | 5.0 kJ/m² | ISO 180/A |
| Environmental stress crack resistance, Condition B, 10% Igepal | >600 h | ASTM D1693 |
Because the density is 0.950 g/cm³ rather than 0.960 g/cm³, the resin contains a short-chain comonomer fraction that reduces lamellar thickness and improves stress-crack resistance relative to an unbranched homopolymer. The 0.63 g/10 min melt flow index is high enough to limit melt temperature rise in high-shear extrusion and low enough to retain melt strength during sheet take-off and thermoforming sag. In capillary rheometry at 190 °C, the viscosity-shear-rate relationship should be used to determine die pressure because published data sheets may not include power-law parameters. The ratio of high-load melt flow index at 21.6 kg to the standard 2.16 kg melt flow index is used to infer molecular weight distribution, but grade-specific ratios should be taken from the certificate of analysis.
In sheet extrusion, LyondellBasell HDPE 50-0863 is processed on conventional single-screw extruders with 24:1 to 30:1 L/D ratios and screen packs of 40/60/80 mesh. Melt temperatures are maintained between 200 °C and 220 °C. The lower boundary prevents excessively high melt viscosity and drive overload, while the upper boundary reduces oxidative degradation and gel formation. Polished roll-stack temperatures from 70 °C to 90 °C are typical, and the lower roll is often run slightly cooler than the middle roll to correct sheet curl. A die gap of 1.1–1.2 times the target sheet thickness is used to compensate for draw-down. On lines with 1200 mm sheet dies, gauge variation is held within approximately ±0.05 mm when automatic thickness control is combined with die-bolt temperature adjustment. A melt flow shift of 0.10 g/10 min between lots can produce a measurable change in die pressure and sheet thickness. Regrind fraction should therefore be controlled because repeated thermal history can reduce melt flow index and widen molecular weight distribution.
| Process Segment | Parameter | Reference Condition |
|---|---|---|
| Extrusion | Melt temperature | 200–220 °C |
| Extrusion | Roll-stack temperature | 70–90 °C |
| Extrusion | Die gap | 1.1–1.2 times sheet gauge |
| Thermoforming | Sheet surface temperature | 125–150 °C |
| Thermoforming | Mold temperature | 20–50 °C |
The lower forming limit is set by the Vicat softening temperature of 124 °C and by flexural recovery behavior. Sheet surface temperatures below 125 °C produce high forming stresses, incomplete replication of mold corners, and excessive springback. The upper practical limit is dominated by sheet sag and localized thinning. Radiant oven surface temperatures from 125 °C to 150 °C are used, with lower temperatures for shallow-draw parts and higher temperatures for deep-draw geometries. Plug-assist tooling made from syntactic foam or polyamide is maintained at 20–50 °C to control heat extraction and prevent sticking. Forming pressure is typically 0.3–0.6 MPa for plug-assisted pressure forming. Vacuum-only forming is limited by the density and melt strength of the sheet. Nonuniform sheet thickness greater than ±0.05 mm can translate into wall-thickness variation in the finished part, particularly in corner radii below 2 mm.
Environmental stress crack resistance is a differentiating feature of this density class. The reported >600 h Condition B result indicates resistance to stress cracking under a wetting-agent environment, but actual performance depends on molded-in stress, chemical exposure, and part geometry. For detergent, oil, or agricultural chemical contact, ESCR testing must be performed on finished parts rather than on pellet specimens because processing orientation and weld lines can reduce failure time from pellet-level values. Accelerated weathering of the natural grade is poor unless an ultraviolet stabilizer package or carbon black is added. Outdoor applications therefore require separate testing under ASTM D2565 or ISO 4892-2 to establish retention of tensile properties and surface integrity.
Compliance documentation for food-contact use is normally issued under FDA 21 CFR 177.1520(c) for olefin polymers, provided the thickness, additives, and use conditions remain within the regulatory limitations. For European Union applications, migration testing under EU Regulation (EU) No 10/2011 is required. REACH SVHC status and RoHS Directive 2011/65/EU compliance should be confirmed with the supplier. These statements are product-class general conditions; the certificate of conformance for the finished part remains the responsibility of the converter.
Compared with a 0.954 g/cm³ HDPE pipe grade having a melt flow index of 0.22 g/10 min, LyondellBasell HDPE 50-0863 has lower melt viscosity and lower die head pressure on the same extruder, but it is not rated for pressure-pipe service under ISO 9080. Compared with high-molecular-weight HDPE blown-film grades with melt flow indices near 0.05 g/10 min, 50-0863 has lower bubble stability and lower melt strength in high-stalk film, but higher throughput in flat-sheet tooling. Compared with HDPE injection-molding grades with melt flow indices above 2.0 g/10 min, 50-0863 produces higher part stiffness and ESCR but is unsuitable for thin-wall injection molding because of high filling pressure into narrow flow lengths. Direct substitution into blow molding should be evaluated against die swell, hang strength, and pinch-off weld strength. Published data for blow-molding-specific comparisons is limited.
At moisture contents above 0.05%, pre-drying for 2 h at 80 °C is recommended to prevent surface splay in sheet. Contamination with polypropylene above 5 wt% should be avoided because dispersed polypropylene can reduce ESCR and create delamination planes during thermoforming. Use of abrasive fillers or halogenated flame retardants requires separate melt filtration and corrosion-resistant tooling because the base resin data sheet does not cover compounded variants.