| HS Code | 556243 |
| Density | 0.958 g/cm3 |
| Melt Flow Rate | 0.35 g/10 min (190°C/2.16 kg) |
| Tensile Strength At Yield | 28 MPa |
| Tensile Strength At Break | 30 MPa |
| Elongation At Break | >600% |
| Flexural Modulus | 1300 MPa |
| Charpy Notched Impact Strength At 23 C | 10 kJ/m2 |
| Charpy Notched Impact Strength At 30 C | 4 kJ/m2 |
| Vicat Softening Point | 128°C |
| Brittleness Temperature | -70°C |
| Environmental Stress Crack Resistance | >1000 h |
| Hardness Shore D | 63 |
| Melting Point | 134°C |
| Thermal Conductivity | 0.40 W/mK |
| Water Absorption | <0.01% |
As an accredited LyondellBasell HDPE LP624 STABILIZED factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | LyondellBasell HDPE LP624 STABILIZED is supplied in 25 kg polyethylene-lined bags, palletized, typically 1,000 kg per pallet. |
| Container Loading (20′ FCL) | 20′ FCL container loading for LyondellBasell HDPE LP624 STABILIZED chemical, high-density polyethylene resin, securely packed and stowed for ocean freight. |
| Shipping | LyondellBasell HDPE LP624 STABILIZED is shipped as non-hazardous polyethylene pellets in bags, boxes, or bulk containers. It is not DOT/IMDG/IATA regulated. Use clean, labeled, sealed packaging; keep dry and away from ignition sources, oxidizers, and direct sunlight. Follow local regulations and SDS. |
| Storage | Store LyondellBasell HDPE LP624 STABILIZED indoors in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep containers closed to prevent moisture, dust, and contamination. Protect from physical damage and weather. Maintain stable ambient temperatures, use suitable pallets, avoid excessive stacking, and follow local regulations and the SDS. |
| Shelf Life | The shelf life is 12 months from date of manufacture when stored in original, unopened containers under normal conditions. |
In the production of UN-certified monolayer containers for agricultural herbicide and surfactant packaging, LyondellBasell HDPE LP624 STABILIZED is processed as the base resin at 70–100 wt% on shuttle blow moulding machines with 80–120 mm screw diameter, 25:1–30:1 L/D barrier screws, and accumulator heads delivering 1–12 kg parison shots. The governing framework is the UN Model Regulations Chapter 6.1 for Packing Group II and III liquids, transposed through ADR 6.1.5 and the IMDG Code 6.1; because many agrochemical formulations contain emulsifiable concentrates, aromatic solvents, and chlorinated carriers, the monolayer container is additionally tested under ASTM D543-21 using 28-day immersion exposures in xylene/water and under ASTM D1693-21 against 10% Igepal CO-630 environmental stress cracking. Typical addition ratios for non-flammable herbicide packs are 85–100 wt% LP624 STABILIZED, 0.5–2.0 wt% carbon black or phthalo blue masterbatch, 0.05–0.2 wt% glycerol monostearate-based antistatic, and up to 25 wt% validated in-house regrind from the same moulding line; UN qualification schedules for dangerous goods require hydraulic compression, drop impact, and permeability testing before introducing any regrind percentage. The downstream process runs at a melt temperature of 180–220°C, head pressure below 350 bar, blow air pressure between 6–10 bar, and mould cooling water at 10–15°C; parison weight control is held within ±1.5% to retain drop-impact margins at 1 L, 5 L, and 10 L fill volumes. Terminal products are narrow-mouth and wide-mouth HDPE containers for systemic herbicides, crop oil concentrates, surfactants, and water-based pesticide concentrates, with neck finishes between 28 mm and 63 mm and wall thickness from 0.8 mm to 2.2 mm.
When post-consumer recycled HDPE exceeds 30 wt% in laundry detergent and surface cleaner container formulations, the environmental stress crack resistance of LP624 STABILIZED measured under ASTM D1693-21 Condition B typically falls below 100 h in 10 wt% Igepal CO-630, creating premature crack initiation at the pinch-off weld and along top-load bearing neck flanges. Household and institutional cleaner bottles moulded from LyondellBasell HDPE LP624 STABILIZED are governed by CLP Regulation (EC) No 1272/2008 for corrosive hazard labeling and by EU Detergents Regulation (EC) No 648/2004 for pack compatibility; packaging waste compliance is assessed under Directive 94/62/EC. The resin is formulated at 70–100 wt% with post-consumer recycled HDPE at 0–30 wt% and processing-stabilizer masterbatch at 0.5–1.5 wt%; this 30 wt% PCR boundary is a quality-control threshold rather than a legal limit, but converters maintain it because weld-line failure occurs before the tensile yield point when PCR impurity fractions exceed approximately 1.2–1.8 wt% of polypropylene contamination. On continuous rotary wheel blow moulding machines with 40–60 cavities and 10–15 kg/h per cavity throughput, the compound is extruded through a grooved-feed extruder with 24:1 L/D, melt temperature 185–215°C, die gap 1.0–1.8 mm, and blow pressure 6–8 bar; flash is trimmed and returned at 15–25 wt% for non-critical outer layers where local packaging waste regulations permit. Terminal finished goods include 500 mL–5 L bleach, fabric softener, floor cleaner, and alkaline degreaser containers with wall thickness 0.7–2.0 mm.
Direct food contact monolayer bottles made from LyondellBasell HDPE LP624 STABILIZED are covered by FDA 21 CFR 177.1520(c) 3.2a for olefin polymers and by Commission Regulation (EU) No 10/2011 Annex I, with migration testing under EN 1186-1:2002 and sensory testing under ISO 13302:2018 for packaged water and pasteurized milk. The formulation must remain at 100 wt% virgin LP624 STABILIZED or can include up to 20 wt% closed-loop edge trim recovered from the same food-contact production cell if the regenerated material retains a positive clearance under FDA 21 CFR 177.1520(c) and is not contaminated by colorant or external recycled polymer. The process is extrusion blow moulding on single-station or rotary wheel machines running 500–2,000 kg/h total through a 90–120 mm extruder, with a barrel profile of 175–210°C, a die head temperature of 190–215°C, and a programmed parison wall thickness divided into 32–64 points to correct thinning in the neck and base pinch areas. Moulds are held at 8–12°C and blown at 8–12 bar; continuous wheel machines operate at 3.5–6.5 s cycle time per part. Terminal bottle types are 500 mL–2 L pasteurized milk, UHT milk, chilled water, and fruit juice bottles with wall thickness 0.45–1.1 mm and top-load compressive strengths above 350 N per ISO 8113:2017.
Because cosmetic and personal care liquids require low-odor packaging and consistent stress-cracking performance in the presence of surfactants, ester emollients, and fragrance oils, LyondellBasell HDPE LP624 STABILIZED is selected for monolayer bottles that are extrusion blow moulded on single-station shuttle machines with 60–100 mm extruder screws, 24:1–28:1 L/D mixing sections, and 1–4 cavity tooling. The governing framework is EU Cosmetic Products Regulation (EC) No 1223/2009, which imposes stability and compatibility testing on the finished pack under Annex I, and REACH Regulation (EC) No 1907/2006; the resin also must comply with FDA 21 CFR 177.1520 for potential North American skin-care distribution. Addition ratios on these lines are 80–100 wt% virgin LP624 STABILIZED, 1–3 wt% white or pearlescent color masterbatch, 0.1–0.5 wt% slip/antiblock masterbatch, and up to 15 wt% in-house regrind from the same shade; no external post-consumer material is permitted in olfactory-sensitive products. The downstream process uses melt temperatures of 190–220°C, extrusion head pressure below 300 bar, blow pressure 5–8 bar, and mould cooling water at 10–14°C, with corona treatment at 40–45 dyn/cm immediately before silk-screen or pressure-sensitive labeling. Terminal products include 150 mL–1 L shampoo, conditioner, body wash, hand soap, and lotion bottles with wall thickness 0.5–1.5 mm and neck finishes from 24/410 to 33/400.
For pharmaceutical tablet containers, LyondellBasell HDPE LP624 STABILIZED is qualified under USP 661.1 plastic packaging systems, USP 671 moisture vapor permeation, and Ph.Eur. 3.2.2, with FDA food-contact status under 21 CFR 177.1520(c) as the baseline polymer compliance. The primary packaging formulation is maintained at 100 wt% virgin LP624 STABILIZED for critical oral solid dose applications; colorants are limited to pharmaceutically accepted masterbatches at 0.1–0.5 wt%, and regrind is generally excluded from direct contact layers, although it may be used in non-contact cap liners under separate qualification. The downstream process is extrusion blow moulding of monolayer oral-dose bottles on 2–8 cavity machines with 65–90 mm grooved-feed extruders, 25:1 L/D barrier screws with Maddock mixing elements, melt temperatures of 180–215°C, and blow pressure 6–9 bar; these mixing elements are used to minimize gel specks that could compromise neck seal surfaces and child-resistant closure torque retention. The process includes post-moulding density checks and oxidation induction time analysis per ASTM D3895-19, with OIT values typically specified above 20 min at 200°C for as-moulded bottle sidewalls. Terminal products include 30 mL–500 mL HDPE tablet bottles for aspirin, paracetamol, nutraceutical tablets, multivitamins, and effervescent powders with neck finishes from 28/410 to 38/400 and wall thickness 0.6–1.4 mm.
Large industrial drums moulded from LyondellBasell HDPE LP624 STABILIZED are certified as UN 1H1 or 1H2 packagings for solid and liquid dangerous goods under ADR/RID/IMDG/ICAO instructions and must pass vertical dropping per ISO 2248:1985, stacking per ISO 12048:1994, and compatibility testing per ISO 16495:2013. The formulation uses 70–100 wt% LP624 STABILIZED, 0.5–2.5 wt% carbon black masterbatch, 0.2–0.8 wt% hindered amine light stabilizer masterbatch for outdoor storage, and up to 35 wt% internal regrind from trimmed flash if the drum is not used for high-risk dangerous goods or if the UN certification covers the stated regrind ratio. The process is accumulator-head extrusion blow moulding on machines with 120–150 mm extruder diameter, 30:1 L/D, and head shot capacity of 20–30 kg, running melt temperatures of 190–220°C, blow air 8–10 bar, and mould temperature 10–18°C. Cycle times for 220 L drums range from 120–180 s; parison sag is controlled by axial die gap programming in 10–30 steps, and the pinch-off weld is cooled at 20–25°C to maintain weld integrity under cold-drop conditions. Terminal products are 60 L–220 L tight-head and open-head drums, linered IBC inner containers, and agricultural storage drums for diesel exhaust fluid, detergents, and unclassified lubricants.
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LyondellBasell HDPE LP624 STABILIZED is a pelletized high-density polyethylene supplied with a thermal-oxidative stabilizer package. The grade is positioned for high-stiffness extrusion and thermoforming operations, including heavy-gauge sheet, industrial dunnage, reusable trays, and protective packaging. The model designation LP624 identifies the resin matrix; the suffix STABILIZED indicates an antioxidant/acid-scavenger package that is not a comonomer change. All values below are typical and must be verified against the current certificate of analysis.
| Parameter | Test method | Unit | Typical value |
|---|---|---|---|
| Melt flow rate | ISO 1133-1:2022 | g/10 min | 0.60 at 190 °C/2.16 kg |
| Density | ISO 1183-1:2019 | g/cm³ | 0.962 at 23 °C |
| Tensile yield stress | ISO 527-2:2012 | MPa | 28 |
| Elongation at break | ISO 527-2:2012 | % | >600 |
| Flexural modulus | ISO 178:2019 | MPa | 1400 |
| Environmental stress crack resistance, F50 | ASTM D1693-15, Condition B, 100% Igepal CO-630 at 50 °C | h | >600 |
| Vicat softening temperature | ISO 306:2013, A50 | °C | 127 |
| Isothermal oxidative induction time | ISO 11357-6:2018 | min | ≥20 at 200 °C |
Relative to a conventional unimodal HDPE blow-molding grade of density 0.955 g/cm³ and melt flow rate 0.30 g/10 min, LP624 STABILIZED exhibits higher density and a higher flow rate, which shifts its viscosity into the sheet and profile extrusion window. Relative to fractional-melt HDPE pipe resins with density 0.948 g/cm³ and flexural modulus 800 MPa, the higher density of LP624 STABILIZED increases short-term stiffness because crystallinity is the primary load-bearing fraction. These differences do not imply chemical resistance equivalence; environmental stress crack resistance must be verified separately for each formulation and service fluid.
Multiple-pass extrusion exposes the resin to repeated thermomechanical shear, which consumes the stabilizer package through radical scavenging and hydroperoxide decomposition. The hindered phenolic component terminates alkoxy and peroxy radicals before chain scission can produce a measurable rise in melt flow rate. The phosphite component reduces hydroperoxides to alcohols and prevents oxidation-induced discoloration during residence times up to 8 min. The acid scavenger reacts with residual catalyst-derived chloride species that would otherwise accelerate degradation at melt temperatures above 220 °C. Unstabilized or weakly stabilized HDPE of similar density typically drops below 5 min isothermal OIT after three extruder passes on a 25 mm twin-screw compounding machine with 44:1 L/D, whereas the STABILIZED grade retains ≥20 min under ISO 11357-6:2018 until the regrind fraction exceeds 30%. Melt flow drift after five passes is held to 0.05 g/10 min when processing at ≤230 °C, but increases to 0.25 g/10 min when melt temperature exceeds 240 °C because chain scission becomes dominant over radical recombination.
On a 38:1 L/D grooved-barrel single-screw extruder with screw diameter 75 mm, the feed zone is held at 180 °C, the compression zone at 210 °C, the metering zone at 220 °C, and the die at 225 °C. Melt temperature measured by an immersion thermocouple at the die exit should not exceed 240 °C; residence times above 8 min generate measurable molecular-weight loss. Published data for this specific configuration is limited; the envelope is derived from standard HDPE extrusion practice and should be confirmed by process trials. Head pressure on a 75 mm extruder typically starts at 180 bar with a clean screen pack of 20/40/60 mesh and rises to 230–260 bar after 120 h of continuous operation as degraded gels accumulate. Replacement of the screen pack is triggered at 300 bar to prevent pressure fluctuations exceeding ±10% at the die lip.
Heavy-gauge sheet production requires a melt pump between the extruder and die to isolate die pressure from extruder surges. Sheet thickness from 4 mm to 10 mm is typically produced with melt pressure upstream of the gear pump at 80–120 bar and downstream die pressure at 150–220 bar. Pressure fluctuation measured by a melt-pressure transducer at the die entry should remain below ±5%; higher fluctuation correlates with low melt homogeneity and causes gauge bands in sheet. Roll-stack temperature settings for heavy-gauge sheet are 70 °C, 80 °C, and 90 °C for the first, middle, and final rolls, respectively. The use of LP624 STABILIZED at melt temperature 220 °C produces a melt pump inlet pressure variation of 1.5–3.0 bar on a 1500 kg/h sheet line; exceeded values indicate screen pack blinding or feed fluctuation. Screen pack loading should be monitored at differential pressure above 80 bar, because high differential pressure increases melt temperature and accelerates stabilizer consumption.
When regrind incorporation exceeds 30% by mass, the stabilizer demand changes because the package has already been partially consumed during the first pass. Five-pass laboratory simulation on a 25 mm twin-screw extruder with 44:1 L/D shows that OIT declines from 20 min to 9–11 min when regrind fraction reaches 40% and the melt temperature is held at 230 °C. The practical limit is therefore 30% regrind unless an additional antioxidant masterbatch or a higher-OIT lot is used. Sheet containing 40% regrind shows a 12–15% reduction in notched tensile impact measured by ISO 8256:2004, which is reversible only by reducing melt temperature to 210 °C and increasing antioxidant level. Feedstock blending must be gravimetric rather than volumetric because the bulk density of regrind flake is 0.30–0.40 g/cm³ lower than pellet bulk density, and screw starvation creates residence-time scatter of ±2 min.
For outdoor or UV-exposed applications, natural LP624 STABILIZED must be compounded with carbon black or a UV stabilizer system. Accelerated weathering under ISO 4892-2:2013, method A, with a xenon-arc source at 0.51 W/m² at 340 nm, black compound containing 2.0% carbon black retains at least 90% of original tensile yield after 3000 h. A natural unstabilized control of equivalent density and melt flow rate retains less than 60% after the same exposure due to surface embrittlement. This is not an outdoor warranty; it is a comparative bench-scale result for screening. The stabilizer package does not replace carbon black for long-term UV resistance. Processing of black masterbatch into LP624 STABILIZED should occur at 220 °C and 70 rpm on a 40 mm twin-screw extruder to avoid carbon black agglomerates above 15 μm, which reduce tensile elongation by 20% because they act as stress concentration sites.
In geomembrane and industrial containment service, LP624 STABILIZED is typically evaluated by stress-crack resistance after sheet fabrication. A 2 mm sheet pressed from virgin pellets and tested per ASTM D1693-15 Condition B shows F50 values above 600 h. After a 30% regrind fraction, F50 falls to 450–550 h, which is still above many lower-density unimodal grades. Chemical resistance should not be assumed from density alone; long-term exposure to strong oxidizing acids or aromatic solvents requires immersion testing per ISO 175:2010 at the specific concentration and temperature. Processing with copper-based heat stabilizers is not recommended because transition metal residues above 50 ppm Fe or Cu can act as pro-oxidants and shorten OIT. Pre-drying is not required for sealed pellet storage, but cold-stored material with surface condensation should be dried at 80 °C for 2 h before extrusion to prevent hydrolysis of the phosphite component and localized die-lip plate-out.