| HS Code | 377335 |
| Material Type | High Density Polyethylene (HDPE) |
| Density | 0.954 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 0.55 g/10 min |
| Tensile Yield Strength | 27 MPa |
| Tensile Modulus | 1250 MPa |
| Flexural Modulus | 1250 MPa |
| Elongation At Break | >600% |
| Notched Charpy Impact Strength 23 C | 20 kJ/m² |
| Notched Charpy Impact Strength 30 C | 10 kJ/m² |
| Hardness Shore D | 65 |
| Vicat Softening Temperature | 128°C |
| Melting Temperature Dsc | 132°C |
| Environmental Stress Cracking Resistance F50 10 Igepal | >1000 h |
| Water Absorption | <0.01% |
| Mold Shrinkage | 1.5-2.5% |
| Thermal Conductivity | 0.42 W/m·K |
| Coefficient Of Linear Thermal Expansion | 1.3E-4 /°C |
| Processing Method | Blow molding/extrusion |
As an accredited LyondellBasell HDPE M4855 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | LyondellBasell HDPE M4855 is supplied in 25 kg polyethylene bags, palletized, or 1,000 kg bulk bags. |
| Container Loading (20′ FCL) | LyondellBasell HDPE M4855 resin bags are typically palletized and loaded into a 20-foot FCL container, securely stowed for international shipment. |
| Shipping | LyondellBasell HDPE M4855 is typically shipped as non-hazardous polyethylene pellets in 25-kg bags, 500–1000-kg jumbo bags, or bulk trucks/railcars. Store in a dry, ventilated area away from heat, moisture, and direct sunlight. Use standard handling equipment, avoid package damage, and keep away from ignition sources. |
| Storage | Store LyondellBasell HDPE M4855 indoors in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, and open flames. Keep original packaging closed and palletized to prevent moisture, dust, and contamination. Avoid strong oxidizers and physical damage. Do not overstack. Maintain good housekeeping. Keep containers labeled. Use first-in, first-out rotation, and follow local regulations and SDS guidance. |
| Shelf Life | Typical shelf life is 24 months when stored in original unopened packaging, cool, dry, away from direct sunlight and heat. |
In thin-wall dairy packaging lines running 300–450 µm nominal wall sections, LyondellBasell HDPE M4855 is processed at a melt temperature of 210–225 °C and a mould temperature of 8–20 °C. The grade carries a nominal melt flow rate of 55 g/10 min under ISO 1133-1 and a nominal density of 0.948 g/cm³ under ISO 1183-1. Valve-gated hot runner tooling with 16–48 cavities is the standard configuration on high-output lines. Balanced 8-drop manifolds reduce fill pressure variation and prevent cavity-to-cavity short shots. Typical injection velocity is 80–140 mm/s, holding pressure is 35–55 MPa, and clamp force is 2000–4500 kN depending on total projected area. The reciprocating screw should provide L/D 22–25 and compression ratio 2.5–3.0, with back pressure held at 0.2–0.8 MPa and screw speed at 100–180 rpm. The high MFR under shear permits thin-wall filling without exceeding 70 MPa hydraulic peak pressure in 32-cavity tools.
The compound is generally 97–99 wt% M4855 and 1–3 wt% titanium dioxide masterbatch. The masterbatch carrier must stay within ±15 g/10 min MFR of the base resin to prevent flow marks on the finished cup sidewall. For food-contact articles, the final item is supplied against FDA 21 CFR 177.1520(c) olefin polymer extractable fraction limits and EU Regulation No 10/2011 overall migration limits of 10 mg/dm² for flat articles or 60 mg/kg for volumetric articles. China GB 4806.6 food-contact resin requirements apply for exports to PRC ports. Pigments are restricted to positive list substances. No primary aromatic amines or dual-use colourants are permitted. Antioxidant masterbatch additions, if used, must not exceed the specific migration limits assigned under EU Regulation No 10/2011 Annex II and China GB 9685.
Melt residence time above 230 °C must be kept below 4–5 min because HDPE homopolymer degrades by chain scission and generates off-odour. Hot runner valve pins should be set to open after polymer cushion reaches 4–6 mm. Mould cooling time for a 400 µm wall section ranges from 3–6 s. Post-fill packing is maintained until gate freeze. Gate diameter is typically 0.8–1.2 mm for side-gated entries in thin-wall stack tools. Terminal articles are dairy cups, margarine tubs, yogurt pots, ice-cream tubs and similar cold-fill containers. The grade is not intended for retort or hot-fill sterilisation because sustained temperatures above 75 °C in food contact can lead to part deformation and off-odour transfer.
Closure moulders running 64–128 cavities with cold-runner sub-gated tools operate M4855 at a melt temperature of 200–215 °C and a mould temperature of 10–15 °C. Unlike thin-wall food packaging, closure production places more emphasis on post-fill dimensional control than on extreme fill speed. Injection velocity is typically 60–100 mm/s, with holding pressure maintained at 45–65 MPa for 0.5–1.5 s after gate freeze. Gate diameter is set at 0.5–1.0 mm. When high-cavitation tools are used, melt cushion must remain stable between 3–5 mm because excessive cushion loss on one hot runner bank creates inconsistent residual stress that shows as white stress-whitening around the gate. Tool maintenance frequency is usually linked to gate wear. Worn sub-gates produce feather-like gate residue on the underside of the closure and require inspection under 5–10× magnification. Published data for this specific configuration is limited; closure validation therefore relies on in-line torque and drop testing.
The formulation is 96–98 wt% M4855 and 2–4 wt% colour masterbatch. For closures exposed to dairy fat or edible oil, the colour masterbatch must itself be FDA 21 CFR 177.1520-compliant and EU Regulation No 10/2011-compliant. In some lines, 5–10 wt% LLDPE is dry-blended to improve stress crack resistance for still liquids. Levels above 10 wt% reduce the melt flow enough to produce short shots in narrow gate rings. The closure liner, if present, is a separate compliance boundary. Aluminium foil or EVA-based liners are checked under EU Regulation No 10/2011 total migration and sensory panel testing.
M4855 is used for tamper-evident overcaps on milk, flavoured milk, still juice, edible oil and condiment bottles. It is not specified for carbonated soft drink closures. HDPE homopolymer has insufficient environmental stress crack resistance under ASTM D1693 Condition A for aggressive carbonated pressure retention, and closure manufacturers switch to copolymer HDPE with higher molecular weight for those geometries. Weld line strength in the cap knurl area must be checked by axial compression testing on the finished cap rim against the filling line capping torque specification. Terminal products include tamper-evident overcaps and cap shells for still-liquid bottles.
Dry-colouring M4855 with 2–5 wt% masterbatch for stackable storage boxes, drawer organisers and household baskets eliminates the need for pre-compounding. The melt temperature is 200–220 °C, mould temperature 10–25 °C and injection velocity 50–90 mm/s on two- to six-cavity cold-runner tools. These are heavier wall sections, often above 1.5 mm, so packing time is longer and gate freeze is used to control sink marks on the outer face. Clamp force is usually 800–1500 kN for single-face tools. RoHS Directive 2011/65/EU and REACH Regulation (EC) No 1907/2006 Annex XVII restrictions apply. Cadmium, lead, mercury and hexavalent chromium are normally below detection limits when compliant masterbatch is used. If the finished article is intended for food storage in the EU, EU Regulation No 10/2011 and FDA 21 CFR 177.1520 apply. No drying is required under normal warehouse conditions. Condensation on pellet surfaces at relative humidity above 80% can produce splay, and pre-drying at 70 °C for 1 h is recommended only in that case. Terminal products include stackable storage boxes, shoe crates, drawer units, waste bins and utility totes. The grade is not recommended for unsupported outdoor use without UV stabilisation or carbon black. Ultraviolet exposure causes surface chalking and loss of impact strength.
Toy parts such as building blocks, stacking cups, bathtub toys and simple storage toys are moulded from 98–99 wt% M4855 and 1–2 wt% approved colour masterbatch. The melt temperature is 195–210 °C for small multi-cavity tools, mould temperature 8–18 °C, injection velocity 70–120 mm/s, and holding pressure 30–50 MPa. In toys with wall sections under 1.0 mm, a stable melt cushion of 3–6 mm is critical because the high MFR of 55 g/10 min makes the machine barrel susceptible to poor screw recovery if cushion drops below 2 mm. Shot size is maintained at 20–60% of barrel shot capacity to avoid residence time degradation and oxidation. Wall-thickness transitions are kept below 1.5:1 to reduce sink marks on visible surfaces. Gate diameter is 0.6–1.0 mm for sub-gated cold runners.
Toy safety compliance is governed by EN 71-3:2019+A1:2021 for migration of 19 elements, ASTM F963-23 for heavy metals in accessible substrates, and EU Directive 2009/48/EC chemical requirements. REACH Annex XVII entries 51 and 52 prohibit phthalates above 0.1 wt% in plasticised toy parts. Because HDPE is unplasticised, this risk is minimal but must be documented in the technical file. The colour masterbatch must not contain azo colorants that release restricted primary aromatic amines. The use of recycled content may require additional documentation under EU Regulation No 10/2011 if food-mimicking play is claimed. Terminal parts include stackable toy crates, toy tool components, bathtub toys and lightweight building blocks. M4855 is not used for living hinges or snap-fit features that require repeated flexure beyond 10,000 cycles. Polypropylene is used in those zones because HDPE has lower flex fatigue strength.
Small open-head pails in the 5–20 L range are produced from 70–100 wt% virgin M4855 and 0–30 wt% in-house regrind generated from the same grade. The melt temperature is 220–230 °C, mould temperature 10–20 °C, injection velocity 50–80 mm/s, holding pressure 40–60 MPa, and cooling time 15–25 s for wall sections of 1.2–2.5 mm. Clamp force ranges from 5000 kN to 12000 kN depending on stack mould geometry. Mould shrinkage is typically 1.5–2.0% under ISO 294-4, and tooling should compensate accordingly on pail diameters. Handling of regrind must include melt-flow verification under ISO 1133-1 after every milling cycle. A drop below 45 g/10 min or a rise above 65 g/10 min requires virgin ratio adjustment.
When the pails are intended for dangerous goods transport, UN 1H2 certification is required under ADR, RID, IMDG Code and US 49 CFR Part 178. The certification is issued for a specific capacity, minimum wall thickness, closure type and stacking load, not for a raw resin alone. FDA 21 CFR 177.1520 applies when the pail is used for food ingredients. EU Regulation No 10/2011 and EU Regulation No 1935/2004 apply for EU food-contact use. If post-consumer regrind is used, the food-contact legal base is lost under EU Regulation No 10/2011 because post-consumer HDPE is not normally accepted without a functional barrier or decontamination process validated under EU Regulation No 2022/1616.
Terminal articles are paint pails, lubricant pails, adhesive cans, sealant containers and industrial powder pails. M4855 is used only for low and medium stack loads. Heavy pails for alkyd paint or aromatic solvents often require a bimodal HDPE or a fluorinated surface treatment to resist permeation. Drop testing at -18 °C under UN 1H2 is a known failure point for high-MFR homopolymer HDPE, so cold-impact validation data must be obtained before specification.
Appliance sub-components such as detergent drawer fronts, rinse aid reservoirs, outlet grilles and filter housings are moulded from 100 wt% M4855 or 98–99 wt% M4855 with 1–2 wt% colour and antioxidant masterbatch. The melt temperature is 210–225 °C, mould temperature 15–30 °C, and injection velocity 50–80 mm/s. These components are usually single-cavity to four-cavity moulds with hot-tip gating. Gate diameter is 1.0–1.5 mm. Because these parts are used in wet detergent environments, the HDPE grade is selected for acid and alkali resistance against household detergent concentrates. The material does not contain plasticisers that can migrate into dispensers. Electrical safety compliance is evaluated under IEC 60335-1 for household appliances. Parts that contact electrical live parts or are within 3 mm of live contacts require glow-wire testing according to IEC 60695-2-11. HDPE M4855 is not flame-retardant and typically falls into UL 94 HB at 3.0 mm thickness. It is therefore restricted to non-current-carrying external covers, drawers and reservoirs. RoHS Directive 2011/65/EU applies for lead, mercury, cadmium, hexavalent chromium, PBB and PBDE. REACH Regulation (EC) No 1907/2006 applies for SVHC declaration. Terminal parts include washing machine detergent drawer faces, dishwasher rinse aid tanks, humidifier water tanks and vacuum cleaner internal brackets. The grade is not specified for parts adjacent to heating elements or steam generators where continuous surface temperatures exceed 70 °C. Prolonged exposure to hot alkaline water can promote environmental stress cracking at weld lines.
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LyondellBasell HDPE M4855 is an injection-molding grade of high-density polyethylene supplied in pellet form. The nominal melt flow rate is 4.8 g/10 min when measured at 190 °C with a 2.16 kg load under ISO 1133-1:2022; nominal density is 0.955 g/cm³ by ISO 1183-1:2019. These values place the material in the medium-flow high-density polyethylene category used for thin-wall injection molding, where stiffness, fast cycle time, and dimensional reproducibility are the primary technical requirements. The public datasheet does not currently resolve comonomer type, molecular weight distribution breadth, or catalyst residue concentration; published data for these specific molecular variables is limited.
Lot-to-lot variation in melt flow and density is controlled by the manufacturer and reported on certificates of analysis. A shift of 0.5 g/10 min in melt flow rate can alter cavity fill pressure and gate-seal time in thin-wall tools, while a density variation of 0.001 g/cm³ can shift shrinkage predictions sufficiently to affect interference fits in closures. Converters should track both variables against tool-specific acceptance limits.
The following typical values are obtained from injection-molded specimens prepared according to ISO 1872-2 and conditioned at 23 °C and 50% RH according to ISO 291. They are nominal values for unpigmented material and are not to be construed as specification limits.
| Property | Typical value | Test method |
|---|---|---|
| Melt flow rate | 4.8 g/10 min | ISO 1133-1:2022 |
| Density | 0.955 g/cm³ | ISO 1183-1:2019 |
| Tensile modulus | 1350 MPa | ISO 527-2 |
| Tensile stress at yield | 31 MPa | ISO 527-2 |
| Tensile strain at yield | 9% | ISO 527-2 |
| Charpy notched impact strength, 23 °C | 5.5 kJ/m² | ISO 179-1/1eA |
| Shore hardness D | 65 | ISO 868 |
| Vicat softening temperature VST/A50 | 129 °C | ISO 306 |
| Heat deflection temperature HDT/B, 0.45 MPa | 78 °C | ISO 75-2/B |
Where ASTM-based specifications are required, equivalent test methods include ASTM D1238-23 for melt flow, ASTM D792-20 for density, ASTM D638-14 for tensile properties, ASTM D790-17 for flexural modulus, ASTM D256-10(2018) for impact, ASTM D2240-15(2021) for hardness, ASTM D1525-17e1 for Vicat softening, and ASTM D648-18 for deflection temperature. Data from ISO and ASTM methods are not numerically interchangeable.
For mold-filling simulation, the apparent shear viscosity and pressure-volume-temperature coefficients for M4855 should be fitted from capillary rheometry data obtained according to ISO 11443:2021. Generic library data for HDPE with 4.8 g/10 min MFR can approximate filling behavior, but lot-specific variation and shear-history sensitivity make measured data preferable for valve-gate timing and packing-pressure prediction.
Injection molding of LyondellBasell HDPE M4855 is generally performed with melt temperature set points between 220 °C and 260 °C; thin-wall packaging applications are frequently run at 230–245 °C. Above 270 °C, oxidative chain scission can produce a measurable reduction in melt viscosity, yellowing, and plate-out on mold vents. Below 210 °C, freeze-off in thin sections below 0.8 mm can cause short shots or weakened weld lines. Mold surface temperatures are normally maintained from 20 °C to 40 °C. The lower mold-temperature boundary shortens cycle time but increases frozen-in orientation and can reduce notched impact energy in thin sections; the upper boundary improves surface gloss and weld-line integrity but increases cooling time and the risk of post-mold shrinkage variation.
Screw geometry should follow general-purpose polyolefin design: L/D 20:1–25:1, compression ratio 2.5:1–3.5:1, with a check ring and shut-off nozzle. Shot size should occupy 40–70% of barrel capacity. Holding pressure is typically set at 50–70% of injection pressure and should be determined by gate-seal study; with tunnel gates of 1.5 mm diameter, gate seal is commonly observed within 2–4 s. Back pressure between 0.5 MPa and 1.5 MPa hydraulic is adequate for melt homogenization. Back pressure above 2.5 MPa can generate enough shear heating to reduce the effective processing window.
In thin-wall tools, injection velocity is profiled to fill rapidly until 90–95% cavity volume and then reduced to prevent flash and jetting. Melt shear rate in the gate should not exceed 100,000 s⁻¹; beyond this value viscous heating can increase local melt temperature by 5–15 °C. Hot runner systems, when used, should be internally heated with valve-gate or thermal-gate drops and should avoid stagnant zones. Total residence time at melt temperature should remain below 10–15 min; longer residence can generate acetaldehyde and carbonyl degradation species.
Pre-drying is not required under normal storage conditions because the polymer is not hygroscopic. If outdoor storage or chilled warehouse handling produces condensation, drying at 80 °C for 2–4 h in a desiccant dryer with a dew point below −30 °C removes surface moisture. Prolonged exposure above 80 °C can accelerate antioxidant consumption and should be avoided.
Mold shrinkage for unfilled HDPE of this density range is generally 1.5–2.5% in the flow direction and 1.0–2.0% transverse to flow under ISO 294-4; actual shrinkage depends on holding pressure, gate location, wall thickness, and mold temperature. Post-mold dimensional change continues for 24–48 h at ambient storage. Dimensional inspection should be conducted after this period to avoid false acceptance of warped components.
Typical application areas for LyondellBasell HDPE M4855 include injection-molded dairy cups, thin-wall food containers, overcaps, closures, and general-purpose housewares with wall thickness between 0.8 mm and 2.5 mm. The tensile modulus of 1350 MPa under ISO 527-2 supplies stacking strength and top-load resistance. The notched Charpy impact energy of 5.5 kJ/m² at 23 °C under ISO 179-1/1eA is suitable for room-temperature service but should not be extrapolated to sub-zero drop impact or aggressive pressure-pulse conditions without part-specific testing.
The resin is normally combined with polyolefin-based masterbatch at addition levels of 1–3 wt%. Color concentrates based on polyethylene carriers are preferred to maintain melt-phase compatibility. Pre-compounding on a corotating twin-screw extruder with L/D 36:1 and barrel temperatures from 220 °C to 240 °C is technically feasible; published data for this specific grade under those compounding conditions is limited, and dispersion quality should be verified by filter pressure rise and microscopic dispersion analysis.
M4855 differs from fractional-melt HDPE blow molding grades mainly in melt flow and melt strength. A blow molding grade with MFR near 0.3 g/10 min has chain length sufficient to maintain parison geometry during extrusion, but demands higher barrel pressure and longer cooling. M4855 at 4.8 g/10 min cannot support parison stability in large accumulator-head blow molding and is confined to injection molding. Conversely, the higher flow reduces fill pressure in thin-wall tools. Compared with high-flow injection molding grades of 20–40 g/10 min, M4855 has higher tensile modulus and better top-load resistance, but longer fill time and greater tendency to freeze in sections below 0.5 mm. Compared with pipe grades near 0.2 g/10 min and density 0.949–0.952 g/cm³, M4855 does not carry PE 80 or PE 100 pressure classification and is not intended for pressure pipe service.
Environmental stress-crack resistance data are not consistently published for medium-flow injection-molding HDPE. Because M4855 has higher melt flow and lower molecular weight than fractional-melt grades, environmental stress-crack resistance is expected to be lower; for applications involving wetting agents, detergents, halogenated preservatives, or continuous hoop stress, the absence of a published ESCR result for this specific grade should be resolved through specimen testing under ASTM D1693 or equivalent.
For food-contact use, the finished article, not the resin alone, must satisfy the applicable jurisdiction. In the United States, olefin polymers are evaluated under 21 CFR 177.1520; the applicable paragraph under 21 CFR 177.1520(c) depends on density, extractables, and end-use conditions. In the European Union, plastic food-contact materials must comply with Regulation (EU) 10/2011 and the overall migration limit of 10 mg/dm². Overall migration testing is performed with the food simulants assigned to the intended contact category and temperature. Published data for this specific product’s migration under all simulants is limited; the converter bears responsibility for finished-article verification.
For general industrial applications, regulatory screening under REACH Regulation (EC) 1907/2006 and the EU RoHS Directive 2011/65/EU is typically addressed through the resin manufacturer’s compliance statement. Unfilled polyolefin grades do not normally contain restricted heavy metals, phthalates, or brominated flame retardants; the presence of pigments, flame-retardant additives, or processing aids may alter this determination.