| HS Code | 271377 |
| Density | 0.946 g/cm3 |
| Melt Flow Rate | 6.0 g/10 min at 190°C/2.16 kg |
| Tensile Strength At Yield | 28 MPa |
| Tensile Elongation At Break | >600% |
| Flexural Modulus | 1100 MPa |
| Shore D Hardness | 62 |
| Vicat Softening Temperature | 122°C |
| Heat Deflection Temperature | 65°C at 0.45 MPa |
| Brittleness Temperature | < -70°C |
| Environmental Stress Crack Resistance | 10 h |
| Notched Izod Impact Strength | 40 J/m at 23°C |
| Molding Shrinkage | 1.5-2.0% |
As an accredited LyondellBasell HDPE M4661 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | LyondellBasell HDPE M4661 is packaged in 25 kg polyethylene bags, palletized, or 1000 kg bulk bags. |
| Container Loading (20′ FCL) | A 20′ FCL container loaded with LyondellBasell HDPE M4661 bags, palletized, shrink-wrapped, and securely lashed for ocean shipment. |
| Shipping | LyondellBasell HDPE M4661 is a non-hazardous high-density polyethylene resin. It is typically shipped in 25 kg polyethylene bags, octabins, or bulk trucks/railcars. Store in a cool, dry, well-ventilated area; avoid contamination, moisture, direct sunlight, excessive heat, and static buildup. No special DOT/ADR/IATA hazard classification required. |
| Storage | Store LyondellBasell HDPE M4661 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and flames. Keep material in original sealed bags or containers, palletized off the floor, to prevent moisture pickup and contamination. Avoid excessive stacking. Observe good housekeeping and FIFO. Consult the SDS and local regulations for additional handling and storage requirements. |
| Shelf Life | Shelf life is typically two years when stored in unopened original packaging under cool, dry conditions, away from direct sunlight. |
Injection-moulded closures and dispensing caps constitute a production environment where LyondellBasell HDPE M4661 is assessed primarily through two interrelated variables: melt flow stability at high shear rates and organoleptic neutrality after repeated contact with packaged liquids. The grade’s nominal density of 0.946 g/cm³ and melt flow rate of 6.0 g/10 min at 190 °C/2.16 kg per ISO 1133-1:2022 position it for thin-wall sections between 0.7 mm and 1.4 mm in multi-cavity hot-runner tools. In eight-cavity to thirty-two-cavity valve-gated systems, screw recovery is usually the limiting factor: barrels with L/D ratios below 20:1 generate inconsistent melt temperature and widen shot-to-shot variation, while compression ratios above 2.8:1 can over-shear the melt and promote odour precursors in headspace analysis. Compliance for food-contact closures is anchored to FDA 21 CFR 177.1520 for olefin polymers, read with 21 CFR 174.5 for good manufacturing practice and, for EU markets, Regulation (EU) No 10/2011 with the Annex II overall migration limit of 10 mg/dm² under EN 1186-1:2002. Child-resistant or tamper-evident designs are tested to ISO 8317:2015 where applicable. The formulation addition ratio on production-scale systems is limited to 1.0 wt%–2.5 wt% pigment masterbatch and 0.5 wt%–1.5 wt% slip/anti-block masterbatch for low-removal-torque caps; total additive loading above 3.5 wt% has been associated with elevated removal-torque standard deviation and higher reject rates in statistical process control audits. Drying is not required when storage relative humidity remains below 60%; if cold-condensation occurs, predrying at 60 °C for 1 h–2 h eliminates surface splay. Downstream conversion typically uses high-speed injection moulding machines with clamp forces from 600 kN to 2,500 kN, injection pressures between 80 MPa and 110 MPa, and mould temperatures maintained at 12 °C–35 °C. The hold-pressure profile is staged from 60% to 80% of peak injection pressure to control gate vestige height below 0.1 mm on tamper-band closures. Terminal product types include dairy and beverage screw caps, push-pull sports closures, child-resistant over-caps, and dispensing caps for personal care formulations.
| Closure requirement | Test standard | Critical parameter |
|---|---|---|
| Resin compliance for food contact | FDA 21 CFR 177.1520 | Olefin polymer specification |
| EU overall migration | EN 1186-1:2002 | 10 mg/dm² |
| Melt flow rate | ISO 1133-1:2022 | 6.0 g/10 min |
| Child-resistant package validation | ISO 8317:2015 | Sequential opening-closing protocol |
The conversion of HDPE M4661 into open-head pails for dangerous goods transport brings a specific process conflict: high melt flow reduces injection pressure and improves thin-wall filling, but the same parameter lowers low-temperature notched impact when wall sections are reduced below 2.0 mm and when weld lines form around the rim gate, measured by ISO 179-1:2010 at -18 °C. Production-scale machines for 5 L–25 L pails typically operate with clamp force between 800 kN and 4,000 kN and use sequential valve-gated hot runners to displace knit lines from the handle and gasket sealing areas. In-mould flow studies on these tools show that injection speed profiling with a fast-to-slow velocity transition reduces gas entrapment around the gate ring. Certification as UN dangerous goods packaging requires design type testing under ADR 6.1.5, IMDG 6.1, and 49 CFR 178. Packing Group II liquid pails must pass drop tests at 1.2 m, and Packing Group III at 0.8 m; stacking stability is evaluated at 95 kPa or equivalent height per ADR 6.1.5.2. The formulation addition ratio is limited to 1.5 wt%–2.0 wt% carbon black masterbatch for UV resistance and 15 wt%–25 wt% post-industrial regrind. When regrind fraction exceeds 30 wt%, drop failures at -18 °C and stress-whitening near the handle bosses increase in production audits. Published data for this specific M4661 configuration is limited; the 30 wt% boundary is plant-specific and must be revalidated by design type testing. The process route is conventional cold-runner or hot-runner injection moulding with wall sections of 2.0 mm–4.0 mm, mould temperatures from 15 °C to 35 °C, and post-mould cooling fixtures to maintain circularity. Terminal product types include UN-certified open-head pails, tamper-evident lid pails for liquid chemicals, and food-grade pails conforming to EU Regulation (EU) No 10/2011.
| Packaging Group | Drop height for liquids | Stack test load | Standard |
|---|---|---|---|
| Packing Group II | 1.2 m | 95 kPa | ADR 6.1.5.3 |
| Packing Group III | 0.8 m | 95 kPa | ADR 6.1.5.3 |
Rigid returnable logistics containers moulded from HDPE M4661 are evaluated primarily for dimensional stability after repeated industrial washing at 65 °C and for stacking load retention in closed-loop distribution. Unlike one-trip packaging, these crates must survive 200 or more wash cycles without tongue-and-groove distortion that would alter pallet stack height. The grade’s narrow molecular weight distribution supports fast screw recovery on machines with L/D 20:1–25:1, but the absence of broad-molar-mass chains reduces melt strength at the end of fill; thick ribs above 6.0 mm require optimized hold pressure to avoid sink marks. Regulatory compliance for food-contact transport crates is based on EU Regulation (EC) No 1935/2004 Article 3 and, for direct contact, EU Regulation (EU) No 10/2011; REACH 1907/2006 applies to substances of very high concern in recycled content. The formulation addition ratio in outdoor-grade crates includes hindered amine light stabilizer masterbatch at 0.5 wt%–1.5 wt% and colour concentrate at 1.0 wt%–2.0 wt%; regrind content can reach 30 wt% where notched impact is not the limiting property. If pigment masterbatch exceeds 3.0 wt%, viscosity shifts in the melt phase are measurable but generally within process capability. Downstream production uses multi-nozzle hot-runner injection tools with gas-assist channels for ribbed bases; gas injection pressure is maintained at 10 MPa–20 MPa in nitrogen-assisted cycles. Terminal product types include stackable crates, perforated logistics trays, and folding crate panels used in automated high-bay warehouses.
The use of HDPE M4661 in toy components is constrained less by mechanical performance than by elemental migration from pigment masterbatches. Under EN 71-3:2019+A1:2021, toy materials are tested for migration of nineteen elements into simulated gastric fluid; cadmium- and lead-based pigments are therefore excluded from formulation specifications before compounding. Compliance also requires conformity with Toy Safety Directive 2009/48/EC and mechanical testing under EN 71-1:2014+A1:2018. The addition ratio for organic or inorganic non-hazardous pigment masterbatch is held between 1.5 wt% and 3.0 wt%. Higher loadings may improve colour saturation but increase the risk of local pigment agglomeration and surface roughness on textured mould surfaces. A slip/anti-block masterbatch is normally omitted because it introduces extractable additives whose migration would require additional testing under the same standard. Processing is performed on injection machines with polished or lightly brushed mould surfaces; melt temperature is maintained at 190 °C–215 °C to reduce odour and residual monomer levels. Terminal product types include stacking blocks, construction panels, toy storage bins, and puzzle boards. Published data for this specific M4661 toy formulation is limited, so each pigment change requires revalidation of migration limits.
For HDPE M4661 converted into filter housings and water-contact appliance components, the certification entity evaluates the finished article rather than the raw resin alone. North American installations reference NSF/ANSI/CAN 61; UK water fittings require WRAS BS 6920; French and German market access commonly invokes ACS and KTW-BWGL. The raw HDPE contributes to compliance when the processor excludes regrind from contact surfaces and uses additive packages with documented extractables. The formulation addition ratio for potable-contact components is typically 0.5 wt%–1.0 wt% carbon black or blue masterbatch for opacity; non-pigmented natural resin is used where certification of colourants has not been completed. Injection moulding uses low-shear screw designs with L/D 20:1–24:1 and melt temperatures from 190 °C to 220 °C. Mould temperatures are set at 15 °C–30 °C to maintain dimensional accuracy of thread forms and sealing faces. Terminal product types include filter housings, pump housings, water reservoir shells, and appliance connection fittings. Published data for this specific M4661 configuration is limited; the performance of the finished article, not the raw resin, determines certification status.
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LyondellBasell HDPE M4661, typically listed within the Alathon high-density polyethylene range, is an injection-molding-grade HDPE characterized by a narrow molecular weight distribution and a nominal melt flow rate of 6.6 g/10 min at 190 °C under 2.16 kg load when tested according to ASTM D1238-20 or ISO 1133-1:2022. The nominal density is 0.966 g/cm³ when measured by ASTM D1505-10(2018) or ISO 1183-1:2019. This combination places the grade in the medium-to-high-flow segment of HDPE injection molding, above blow-molding resins that commonly operate below 1.0 g/10 min and below ultra-high-flow thin-wall grades that may exceed 20 g/10 min. The material is supplied as pellets, and lot-specific certificates of analysis should be consulted for actual melt flow, density, and additive composition before tooling or production is finalized.
M4661 differs from HDPE blow-molding grades such as those with melt flow rates below 1.0 g/10 min primarily in molecular weight and melt elasticity. Blow-molding grades rely on high melt viscosity and high melt strength to maintain parison shape during extrusion; M4661, with a nominal melt flow rate of 6.6 g/10 min, exhibits lower sag resistance and is not specified for continuous extrusion blow molding of large containers or drums. Pipe-grade HDPE materials, particularly PE 100 resins, are classified by long-term hydrostatic strength determined through ISO 9080 testing at 20 °C and 80 °C, with a minimum required strength of 10.0 MPa at 50 years. Published data for M4661 in pressure-pipe service are limited; the grade is not intended for pressure pipe applications where hydrostatic design basis must be established through ISO 9080 and related national standards.
The molecular design of M4661 also produces lower environmental stress crack resistance than typical low-melt-flow blow-molding and pipe grades. In HDPE, increasing melt flow rate generally corresponds to shorter chain length and lower ESCR as measured by ASTM D1693 under 10% Igepal CO-630 at 50 °C. Blow-molding grades with melt flow rates below 0.5 g/10 min frequently exceed 100 h in such tests, whereas injection-molding grades in the 6–7 g/10 min range often report F50 values below 50 h. M4661 should therefore be evaluated under the specific chemical contact conditions of the intended package or part rather than substituted directly for a higher-molecular-weight blow-molding resin in aggressive detergent or solvent service.
Mechanical property testing of M4661 under ASTM D638-14 Type IV specimens typically reports tensile yield stress between 24 MPa and 30 MPa, with elongation at break frequently above 500% in thinner specimens. Flexural modulus values determined by ASTM D790-17 or ISO 178:2019 normally fall between 1,200 MPa and 1,500 MPa, providing rigid sidewall behavior in pails and crates. Notched Izod impact values at 23 °C commonly exceed 35 J/m and may be reported as partial break or no break by ASTM D256-10e1. At -20 °C, impact performance decreases, and validation is required for freezer containers molded at wall thicknesses below 1 mm. Heat deflection temperature at 0.455 MPa is typically reported between 70 °C and 80 °C by ASTM D648-18, while Vicat softening point by ASTM D1525-17e1 is commonly in the range of 125 °C to 129 °C.
| Property | Test method | Reported range or nominal value |
|---|---|---|
| Melt flow rate, 190 °C/2.16 kg | ASTM D1238-20 / ISO 1133-1:2022 | 6.2–7.0 g/10 min; nominal 6.6 g/10 min |
| Density | ASTM D1505-10(2018) / ISO 1183-1:2019 | 0.965–0.967 g/cm³; nominal 0.966 g/cm³ |
| Tensile yield stress | ASTM D638-14 / ISO 527-2:2012 | 24–30 MPa |
| Flexural modulus | ASTM D790-17 / ISO 178:2019 | 1,200–1,500 MPa |
| Notched Izod impact, 23 °C | ASTM D256-10e1 | 35–60 J/m or partial/no break |
| Heat deflection temperature, 0.455 MPa | ASTM D648-18 | 70–80 °C |
| Vicat softening point | ASTM D1525-17e1 | 125–129 °C |
| Shore D hardness | ASTM D2240-15(2021) | 66–70 |
Application contexts for M4661 include thin-wall pails, buckets, freezer containers, storage bins, caps and closures requiring moderate flow, toy components, and industrial crates where fast cycle times and high stiffness are required. In thin-wall containers with wall thicknesses of 0.8–1.5 mm, the melt-flow rate of 6.6 g/10 min supports practical fill lengths of 250–400 mm at injection pressures between 60 MPa and 100 MPa, although actual flow length depends on gate diameter, part geometry, mold temperature, and runner balance. The grade is not specified for flexible packaging film, extrusion blow molding of large drums, or rotational molding, because its molecular weight and melt elasticity fall outside the required ranges for those processes.
Injection molding trials on machines with clamp forces from 80 t to 250 t and general-purpose polyolefin screws having L/D ratios of 18:1 to 22:1 indicate that M4661 plastication is stable when barrel temperatures are profiled from 190 °C in the rear zone to 220 °C at the nozzle. Higher melt temperatures up to 230 °C improve flow length in thin-wall tools but increase cooling demand; sustained operation above 260 °C can cause oxidative degradation detectable as yellowing, odor, and reduced impact performance. Mold temperatures between 10 °C and 30 °C are common for high-density polyethylene. Raising mold temperature above 40 °C extends cooling time but can improve surface gloss and slightly increase tensile modulus through higher crystallinity. Injection pressures of 60–100 MPa and hold pressures of 40–70 MPa are typical, while back pressure of 0.5–1.5 MPa is sufficient to homogenize the melt without excessive shear heating or cycle-time penalty.
Pre-drying is not normally required when the material is processed directly from sealed containers at relative humidity below 60%. However, HDPE regrind stored in unheated silos or exposed to condensation may require drying at 70–80 °C for 2–4 h in a desiccant dryer. Avoid purging with PVC or chlorinated polymers at elevated temperature because residual chlorinated material can liberate hydrogen chloride and corrode tool surfaces. Nucleating agents are generally unnecessary because the narrow molecular weight distribution and high density promote rapid crystallization; addition rates above 0.05 wt% of certain nucleators can shift crystallization temperature but may not produce measurable cycle-time reduction in every tool configuration.
When mold temperatures are increased from 15 °C to 35 °C, the solidification front in M4661 advances more slowly, reducing frozen-layer formation at the flow front and permitting improved packing of ribs, bosses, and hinge areas. The trade-off is an increase in cooling time of approximately 8–15% per 10 °C rise in mold temperature, depending on part thickness and cooling-channel design. This condition is relevant to multicavity tools where flow-length imbalance can produce mass variation across cavities; elevated mold temperature alone does not correct runner imbalance, but it can reduce short-shot rates when used with valve-gated hot runners and sequential filling control.
Environmental stress crack resistance for M4661 should be assessed by ASTM D1693 or ISO 22088-3 under the specific stress-cracking fluid and temperature of the intended application. HDPE injection grades with melt flow rates near 6–7 g/10 min typically show lower ESCR than low-melt-flow blow-molding or pipe grades; published data for M4661-specific ESCR are often below 50 h in 10% Igepal CO-630 at 50 °C, but current datasheet values must be verified because formulation variants can shift this response. This limitation restricts use in aggressive detergent, solvent, or surfactant packaging, while the material remains acceptable for dry foods, non-aggressive liquids, and general industrial containers when supported by application-specific testing.
| Regulatory domain | Applicable standard or regulation | Typical requirement |
|---|---|---|
| Food-contact olefin polymer | FDA 21 CFR 177.1520 | Compliance when supported by supplier food-contact certification |
| EU food-contact plastics | Regulation (EU) No 10/2011 | Overall migration limit 10 mg/dm² or 60 mg/kg for relevant simulants |
| REACH registration | Regulation (EC) No 1907/2006 | No substance of very high concern above 0.1% w/w per article |
| RoHS restrictions | Directive 2011/65/EU | Cd 100 mg/kg; Pb 1000 mg/kg; Hg 1000 mg/kg; hexavalent Cr 1000 mg/kg |
| Heavy metals in packaging | EU Packaging Directive 94/62/EC via EN 13432-related protocols | Sum of Cd, Hg, Pb, and Cr(VI) not exceeding 100 mg/kg |
Compliance claims require lot-specific documentation from LyondellBasell or the compounder because additive packages, regrind content, and regional supply sources can alter the regulatory profile. For food-contact use, the final article must be tested under end-use conditions, including time, temperature, and food simulant, according to Regulation (EU) No 10/2011 or the applicable national standard.