| HS Code | 576897 |
| Density | 0.954 g/cm3 |
| Meltflowrate 190c 2 16kg | 0.35 g/10 min |
| Tensilemodulus | 1300 MPa |
| Tensilestressatyield | 28 MPa |
| Tensilestrainatyield | 9% |
| Tensilestrainatbreak | >600% |
| Flexuralmodulus | 1300 MPa |
| Charpynotchedimpactstrength 23c | 14 kJ/m2 |
| Charpynotchedimpactstrength Minus30c | 5 kJ/m2 |
| Shoredhardness | 65 |
| Vicatsofteningtemperature | 128 °C |
| Meltingtemperature | 130 °C |
| Crystallizationtemperature | 115 °C |
| Thermalconductivity | 0.38 W/mK |
| Coefficientoflinearthermalexpansion | 1.5E-4 /°C |
| Specificheatcapacity | 1.9 kJ/kgK |
| Escr 10pctigepal 50c | >1000 h |
| Waterabsorption | <0.01% |
| Volumeresistivity | >1E15 ohm·cm |
| Dielectricconstant 1mhz | 2.3 |
| Dissipationfactor 1mhz | 2E-4 |
| Dielectricstrength | 20 kV/mm |
| Oxygenindex | 17% |
As an accredited LyondellBasell HDPE L5440 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | LyondellBasell HDPE L5440 is supplied in 25 kg polyethylene bags, typically 40 bags per pallet, totaling 1,000 kg. |
| Container Loading (20′ FCL) | Standard dry 20′ FCL loading of LyondellBasell HDPE L5440: palletized 25 kg bags, evenly distributed, secured, container sealed for export. |
| Shipping | LyondellBasell HDPE L5440 is a non-hazardous, solid thermoplastic resin supplied as pellets. It is typically shipped in 25 kg bags, 1,000 kg jumbo bags, or bulk trucks/railcars. Keep containers closed, dry, and away from heat. No special DOT/IMDG hazardous classification applies. |
| Storage | Store LyondellBasell HDPE L5440 in a cool, dry, well-ventilated indoor area away from direct sunlight, heat, flames, and strong oxidizers. Keep original packaging closed and palletized to prevent moisture, dust, and contamination. Avoid prolonged UV exposure and extreme temperatures. Use first-in, first-out stock rotation. Handle with clean equipment to maintain product quality and safe processing. |
| Shelf Life | LyondellBasell HDPE L5440 has an indefinite shelf life when stored in original, unopened packaging under cool, dry conditions away from sunlight. |
A 32-cavity hot-runner closure line molding LyondellBasell HDPE L5440 for tamper-evident beverage caps uses a 1,200 kN clamp force, a screw diameter of 35 mm, an L/D ratio of 22:1, and a compression ratio of 2.5:1. The barrel profile from feed throat to nozzle is maintained at 180/200/215/220°C. Melt temperature at the nozzle is held between 215°C and 225°C. Gate diameter for the cap body is fixed at 0.8 mm to 1.0 mm on a part wall section of 1.6 mm to 2.0 mm. Hot-runner manifold temperature is set at 215°C, which prevents gate freeze-off before the holding-pressure phase completes. Holding pressure is set at 35 MPa to 45 MPa for 0.4 s to 0.8 s, followed by a cooling time of 4.0 s to 5.5 s. Back pressure is limited to 0.5 MPa to 0.8 MPa and screw speed to 60 rpm to 90 rpm. This suppresses shear-induced melt-temperature spikes that would reduce environmental stress-crack resistance measured according to ASTM D1693-21, condition B, using a 10% Igepal CO-630 solution at 50°C. No pre-drying of natural L5440 is required when silo storage is below 60% relative humidity; if condensation is present, drying at 80°C for 2 h to 4 h is applied. The molded cap is release-tested in tension according to ISO 527-2/1B at 50 mm/min; tensile yield strength of the wall-stock specimen is expected to be not less than 20 MPa.
Closure torque retention is measured after 24 h at 40°C and 60% relative humidity. The bridge-and-band tamper-evident structure is formed by an undercut of 0.35 mm, split-segment ejection occurs only after mold opening reaches 12 mm, and the gate vestige is maintained below 0.15 mm to avoid lip interference. Color masterbatch is loaded at 2 wt% with a 50:1 let-down ratio; the carrier is a low-viscosity HDPE, not LDPE, to avoid shifting the gate pressure curve. Erucamide-based slip masterbatch is omitted from beverage closures because migration of amide waxes to the neck finish reduces removal torque below the lower specification limit. A slip additive may be used at 0.05 wt% to 0.10 wt% only in cosmetic-closure applications where low release torque is desired. For beverage closures sold in the EU, overall migration is tested under Regulation (EU) No 10/2011 with the limit of 10 mg/dm². The dominant failure mode is not cap breakage but cap-to-neck stress whitening at the hinge point after side-load removal; this is controlled by converting with a melt temperature below 225°C.
Thin-walled dairy containers molded from L5440 operate at wall sections of 0.45 mm to 0.65 mm. The processing conflict is the intersection of filling pressure, melt temperature, and off-taste. A butter tub with a flow-path length of 90 mm is filled at an injection speed of 35 mm/s to 50 mm/s; cavity fill time is 0.25 s to 0.45 s. Melt temperature above 230°C produces a detectable paraffinic off-taste in high-fat dairy contact, while melt temperature below 200°C creates short shots at the rim and hinge. Mold cooling water is set at 8°C to 12°C, and cycle time is between 4.8 s and 6.0 s for a 0.5 mm sidewall. Food-contact compliance is anchored to FDA 21 CFR 177.1520(c) 3.1b for polyolefins and EU Regulation (EU) No 10/2011. The overall migration limit is 10 mg/dm², and the article is tested with the food simulant assigned under Annex III of Regulation (EU) No 10/2011. Published data for the specific combination of L5440 with high-fat dairy simulants is limited; converter-specific migration testing is therefore mandatory before commercial release.
A nucleating agent masterbatch is added at 0.05 wt% to 0.15 wt% active content to raise the crystallization temperature by 3°C to 5°C, permitting a cooling-time reduction of 0.8 s to 1.2 s for 0.5 mm walls. Over-nucleation above 0.20 wt% produces brittle rims and early gate freeze-off; the resulting hinge failures are detected after 200 flex cycles at 23°C. The cavity is vented to 0.02 mm depth at the rim to avoid gas burn marks at high fill speed. Because the container is in direct food contact, only additives listed in the Union List in Annex I of Regulation (EU) No 10/2011 are permitted, and the specific migration limit for any slip agent must be verified for the actual wall thickness used. Terminal products include dairy tubs, deli containers, and snap-on lids; each article is subjected to drop testing at 1.2 m onto a rigid surface after 2 h at 4°C to detect cold-temperature hinge fracture.
A 45-L rectangular storage box with a projected area of 0.25 m² is molded from L5440 using a sequential valve-gated hot runner. Melt temperature is held at 210°C to 220°C. Injection speed is profiled at 15 mm/s for the first 5% of cavity fill to prevent air entrapment, then increased to 45 mm/s. Packing pressure is set at 40 MPa for 6 s. The mold cooling channels are arranged so that the temperature difference between fixed and moving halves remains below 5°C. Differential shrinkage between the flow and transverse directions is measured at 1.3% to 1.8% using ISO 294-4; the open-rim section is compensated by a 0.3 mm inward pre-bend in the tool. Without a post-mold cooling jig, a 45-L box withdrawn at 35°C surface temperature can develop a sidewall bow of 3 mm to 4 mm on the long axis. The part is designed with a minimum rib thickness of 1.5 mm to reduce notch sensitivity at the base corner. Cycle time for a 1.8 mm sidewall is 28 s to 35 s, cooling-limited. Colorant is added at 2 wt% with a high-dispersion PE carrier; pigment survival at 220°C is validated after 3 successive regrind cycles because storage boxes are marketed with recycled content.
For general household storage, REACH screening is applied to the resin and masterbatch package; SVHC disclosure under Article 33 of Regulation (EC) No 1907/2006 is required only if a listed substance exceeds 0.1 wt% in the final article. If the box is sold as a food-storage container, the same EU No 10/2011 overall migration limit of 10 mg/dm² applies as in dairy packaging, but the test simulant changes according to the intended food type. The long-flow dimensional stability of L5440 is used on 60 mm to 80 mm screw-diameter machines with clamp force from 3,000 kN to 8,000 kN; ejection is timed after the pressure transducer at the end of fill falls to 5 MPa.
Toy components molded from L5440 use a lower melt temperature of 190°C to 210°C and a mold temperature of 10°C to 20°C when tight interlocking fits are required. The cavity pressure sensor triggers holding-pressure switch-over at 30 MPa, after 95% of the cavity volume is filled. Color concentrates are dosed at 4 wt% with a polyolefin carrier. Migration of certain elements is tested according to EN 71-3:2019+A1:2021; in Category III scraped-off material, lead must not exceed 2.0 mg/kg and cadmium must not exceed 1.3 mg/kg. Since HDPE contains no orthophthalate plasticizer, REACH Annex XVII entries 51 and 52 are documented by raw-material specification rather than batch measurement. Regrind addition above 15 wt% lowers the notched Charpy impact value at 23°C below the release limit, making snap-fit tabs crack at the injection-weld line when a toy is drop-tested from 1.0 m onto a rigid surface.
Cosmetic jars and airless piston reservoirs molded from L5440 require a barrel residence time below 5 min at melt temperature 205°C to 220°C. Screw tips with slit check rings are replaced by ball-check or open-discharge designs; dead spots behind split check rings generate brown specks after 8 h to 12 h of continuous running. High-gloss cavity steel is hardened to HRC 50 to 54 and polished to Ra 0.015 µm; holding pressure of 50 MPa for 3 s is required to replicate the tool gloss on the outer jar wall. Odor and taste transfer are evaluated by ASTM E1870-11 with a sensory panel; no panelist shall detect an off-odor from a 60°C headspace sample after 24 h conditioning. An antistatic additive is dosed at 0.3 wt% to prevent dust attraction on the outer surface. The additive must not increase overall migration above 10 mg/dm² if the jar is dual-marketed for food or oral-care contact under Regulation (EU) No 10/2011. For packages that contact essential-oil-containing formulations, compatibility testing is performed for 72 h at 60°C; weight gain above 2% indicates unacceptable oil absorption and is rejected.
For cosmetic closures, the low-slip formulation may be used at 0.05 wt% to 0.10 wt% erucamide masterbatch to adjust release torque. The closure is then pre-conditioned at 40°C for 48 h to allow surface migration to equilibrate before torque testing. The terminal articles include cream jars, serum-pump collars, and compact bases; each part is evaluated for dimensional stability after 24 h at 50°C because secondary decoration with heat-transfer film demands a diameter tolerance of ±0.05 mm.
| Regulatory instrument | Specified limit or test condition | Application segment |
|---|---|---|
| FDA 21 CFR 177.1520(c) 3.1b | HDPE with density greater than 0.94 g/cm³ per ASTM D1505 | Dairy and food containers |
| Regulation (EU) No 10/2011 | Overall migration limit 10 mg/dm²; specific limits per Annex II | Food-contact packaging |
| Regulation (EC) No 1907/2006, Annex XVII entries 51 and 52 | DEHP, DBP, BBP, DIBP total 0.1 wt% in plasticized material | Toys and childcare articles |
| EN 71-3:2019+A1:2021 | Lead 2.0 mg/kg; cadmium 1.3 mg/kg in Category III scraped-off material | Toy components |
| Directive 2011/65/EU Annex II | Cadmium 100 mg/kg; lead 1000 mg/kg per homogeneous material | Electrical and electronic housing parts |
For 20-L industrial pails, the process is well-established. L5440 is injected at 200°C to 220°C with a mold temperature of 15°C to 25°C; the handle boss is reinforced by a rib of 2.5 mm thickness to avoid creep under a 40°C stacking load. Outdoor storage formulations incorporate a UV stabilizer masterbatch at 2 wt% and a hindered amine light stabilizer at 0.15 wt%; weathering is evaluated by ASTM D4329-21 for 200 h to 400 h. The terminal articles are pails for non-dangerous goods; UN certification for dangerous goods requires additional drop and stack testing on the actual pail design.
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LyondellBasell HDPE L5440 is an injection-molding-grade high-density polyethylene supplied as pellets. The grade designation appears in technical datasheets with a nominal melt flow rate of 4.0 g/10 min at 190°C under 2.16 kg, determined in accordance with ISO 1133-1:2022 or ASTM D1238-20, and a nominal density of 0.954 g/cm³ by ISO 1183-1:2019 or ASTM D1505-18. The density places the material in the upper range of injection-molding HDPE grades and contributes to flexural modulus values commonly reported between 1,100 MPa and 1,300 MPa by ISO 178:2019 or ASTM D790-17. Tensile yield strength is typically 25–28 MPa under ISO 527-2:2012 or ASTM D638-14, with yield elongation near 9–13%. Notched Izod impact at 23°C is normally 3–5 kJ/m² by ISO 180:2019 or ASTM D256-10. The published Vicat softening temperature, A50, falls in the range 123–129°C. These values are typical pellet data, not lot-specific specification limits; acceptance should be governed by certificate of analysis and lot-to-lot process capability.
Primary application areas include injection-molded crates, totes, housewares, caps, closures, and thin-wall containers. The combination of medium melt flow and density 0.954 g/cm³ supports part weight stability across multi-cavity tools. Published datasheets place the grade in the mid-flow segment, where cycle time is shorter than fractional-melt HDPE grades and injection pressure is higher than high-flow thin-wall grades. The resin is not intended for film extrusion, blow molding, or pressure pipe, because its melt strength and strain-hardening behaviour are insufficient for those processes. For rigid packaging, the grade can be processed on general-purpose injection presses with clamp forces from 500 kN upward, depending on projected area; required clamp tonnage is calculated from projected cavity area and peak cavity pressure, not from shot weight.
| Property | L5440 typical range | Test method | Comparative HDPE class |
|---|---|---|---|
| Melt flow rate at 190°C/2.16 kg | 4.0 g/10 min | ISO 1133-1:2022, ASTM D1238-20 | Fractional-melt pipe grades: 0.2–0.5 g/10 min |
| Density | 0.954 g/cm³ | ISO 1183-1:2019, ASTM D1505-18 | High-flow thin-wall HDPE: 0.948–0.952 g/cm³ |
| Flexural modulus | 1,100–1,300 MPa | ISO 178:2019, ASTM D790-17 | Fractional-melt blow-molding HDPE: 900–1,200 MPa |
| Notched Izod impact at 23°C | 3–5 kJ/m² | ISO 180:2019, ASTM D256-10 | Pressure-pipe HDPE assessed by slow crack growth rather than Izod |
| Mold shrinkage | 1.5–2.5% | ISO 294-4:2018, ASTM D955-08 | Low-shrinkage polypropylene compounds: 0.8–1.5% |
On a 1,600 kN hydraulic toggle injection molding machine with a 40 mm general-purpose screw and L/D 20:1, barrel zone settings from feed to nozzle of 190/200/210/220°C are adequate for melt preparation. Screw speed is normally 60–120 min⁻¹ depending on shot mass and color concentrate dispersion. Back pressure of 0.5–1.5 MPa is used to homogenize masterbatch, but excessive back pressure raises melt temperature and reduces output. Hot-runner manifolds should be controlled within ±5°C across drops; larger deviations cause shot-to-shot filling imbalance and differential shrinkage.
The practical lower temperature limit is controlled by melt viscosity and gate freeze. At 200°C melt temperature, the flow length of L5440 is reduced relative to high-flow grades; in thin-wall tools below 1.5 mm, short shots are observed when cavity pressure at end of fill falls below 10 MPa. The upper temperature limit is governed by thermal oxidation. Polyethylene undergoes free-radical chain scission in the presence of oxygen at temperatures above 270°C, causing yellowing and reduction of notched Izod impact. Barrel residence time should therefore be limited to 5–10 min or less at 250°C; longer residence at low shot weight can cause melt-flow drift and part weight variability.
Compared with high-flow HDPE grades of 20 g/10 min melt flow rate used for multi-cavity thin-wall packaging, L5440 generates higher injection pressure at equivalent flow length. Published spiral-flow data for this specific grade are limited, but the difference in melt flow rate corresponds to longer fill time or higher cavity pressure in the same tool. The higher density of 0.954 g/cm³ also raises flexural modulus relative to 0.948 g/cm³ HDPE, at the cost of slightly lower notched impact and higher shrinkage anisotropy.
Differentiation from other HDPE grades is primarily determined by melt flow rate, density, and molecular weight distribution. Fractional-melt blow-molding grades with melt flow rates of 0.2–0.5 g/10 min and density 0.950–0.957 g/cm³ provide the parison sag resistance required for large containers but require higher extruder power and produce thicker process flash in injection tools. High-flow injection grades with melt flow rates of 8–20 g/10 min fill thin-wall parts at lower pressure but generally exhibit lower tensile yield and lower heat resistance. L5440 occupies an intermediate position: the 4.0 g/10 min melt flow rate supports moderate thin-wall geometry while retaining a flexural modulus commonly reported above 1,100 MPa. In comparison with lower-density injection grades such as 0.948–0.952 g/cm³ HDPE, the increase in density reduces notched impact and raises shrinkage anisotropy, so part designs with sharp corners may require radii above 0.5 mm to avoid stress concentration. The grade is not classified as a PE100 pressure pipe resin under ISO 12162:2009 and is not evaluated under ISO 9080:2022 for hydrostatic design stress; use in potable water pressure piping is outside the datasheet scope.
Reported mold shrinkage for L5440 in injection-molded plaques is 1.5–2.5% by ISO 294-4:2018 or ASTM D955-08, with stronger shrinkage in the flow direction than in the transverse direction. This anisotropic behaviour promotes warpage in flat lids and large rectangular crates; tool design must include differential cooling and gate placement that directs shrinkage uniformly toward the ejection side. Weld-line strength is controlled by melt temperature, mold temperature, and oxygen exposure. Raising mold temperature from 20°C to 40°C generally improves weld-line strength but can increase cycle time by 5–15%. Gate freeze time scales with the square of wall thickness; in a 2 mm wall, the gate freezes in the order of 1–2 s, after which holding pressure no longer transmits to the cavity. Hot-runner systems with valve gates reduce shear history and improve color change performance, but may raise melt temperature at the gate.
These characteristics distinguish L5440 from lower-flow blow-molding and pipe HDPE grades, which have higher molecular weight and longer relaxation times. L5440 does not provide the parison melt strength needed for large blow-molded containers; its melt flow rate of 4.0 g/10 min is approximately an order of magnitude higher than typical HDPE blow-molding grades, so parison sag occurs before mold closure in large tools. Conversely, in injection molding it fills thin sections at lower clamp force than fractional-melt grades. Compared with polypropylene homopolymer injection grades, L5440 has lower heat deflection temperature and lower flexural modulus; polypropylene homopolymer typically offers flexural modulus above 1,400 MPa but lower notched impact at 0°C than HDPE. For applications requiring high environmental stress crack resistance at ambient temperature, HDPE is preferred; for hot-fill above 90°C, polypropylene is preferred.
When the grade replaces a lower-MFR HDPE in an existing multi-cavity tool, the melt pressure at the injection nozzle usually decreases and the fill phase can be shortened. The available pressure reserve can be used to lower melt temperature, reduce cycle time, or balance hot-runner shear. However, the higher melt flow does not alter the fundamental relationship between gate freeze time and holding pressure; hold time must be re-established by part-weight measurement as a function of holding time. Weight stability below 0.3% coefficient of variation is a practical production criterion, measured with an electronic balance over 30–50 consecutive shots. Shrinkage and warpage may change because the new grade’s higher flow direction orientation leads to greater in-flow shrinkage.
Existing tools with undersized gates may require gate enlargement to prevent jetting and surface bands. On hydraulic presses, clamp force can be reduced when cavity pressure is verified below 40 MPa, but the nozzle contact force and sprue bushing dimensions must remain within original design. Insufficient venting causes burn marks at the end of fill and weakens knit lines; vents of 0.02–0.04 mm depth are typical for HDPE. Drying is not normally required when pellets are retained in closed containers below 60% relative humidity; surface moisture from cold pellets may require 1–2 h at 70–80°C before processing. Mold temperatures below 15°C can cause condensation and surface splay in humid production rooms.
Regulatory acceptability is application-dependent. As a high-density polyethylene, L5440 can be formulated to comply with FDA 21 CFR 177.1520 for olefin polymers in contact with food, but the end-use article must meet extractive limitations and use conditions. In the European Union, migration testing under Regulation (EU) No 10/2011 must cover the finished article, including colorants and processing aids; compliance of the base resin alone does not establish finished-article compliance. RoHS Directive 2011/65/EU compliance requires confirmation of the additive package; unfilled natural HDPE typically contains no intentionally added heavy metals. Outdoor use of unpigmented L5440 is not advised without UV stabilizer and carbon black or titanium dioxide; photo-oxidation will cause surface chalking, loss of tensile elongation, and eventual brittle failure. Storage should avoid direct sunlight and temperatures above 40°C; prolonged storage under high ultraviolet exposure can shift melt flow rate and yellow index before processing.