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LyondellBasell HDPE ALATHON M5372

    • Product Name: LyondellBasell HDPE ALATHON M5372
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 806385
    Density 0.953 g/cm³
    Melt Index 190 C 2 16 Kg 0.35 g/10 min
    Tensile Strength At Yield 26 MPa
    Tensile Strength At Break 32 MPa
    Elongation At Break >600 %
    Flexural Modulus 1200 MPa
    Vicat Softening Point 126 °C
    Melting Point 130 °C
    Brittleness Temperature < -70 °C
    Hardness Shore D 65
    Environmental Stress Crack Resistance 10 Igepal >1000 h
    Notched Izod Impact Strength 5 kJ/m²
    Thermal Conductivity 0.35 W/m·K
    Volume Resistivity >1E15 ohm·cm

    As an accredited LyondellBasell HDPE ALATHON M5372 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing LyondellBasell HDPE ALATHON M5372 is packaged in 55 lb (25 kg) bags, 40 bags per pallet, totaling 1,000 kg.
    Container Loading (20′ FCL) 20′ FCL container loaded with LyondellBasell HDPE ALATHON M5372 in 25 kg bags, palletized, stretch-wrapped, and secured for ocean shipment.
    Shipping LyondellBasell HDPE ALATHON M5372 ships as a non-hazardous polyethylene resin, not regulated for transport. It is typically supplied in 25-kg bags, octabins, or bulk trucks/railcars. Keep containers closed, dry, and away from heat or ignition. No special DOT/IMDG/IATA labeling required.
    Storage Store LyondellBasell HDPE ALATHON M5372 in a cool, dry, well-ventilated warehouse, 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, crushing, and excessive stacking. Do not store outdoors. Maintain cleanliness, avoid odorous materials, inspect containers regularly, and follow first-in, first-out inventory practices.
    Shelf Life Shelf life is typically 24 months from manufacture when stored in original packaging, cool, dry, away from direct sunlight.
    Application of LyondellBasell HDPE ALATHON M5372

    ALATHON M5372 from LyondellBasell is a narrow-molecular-weight-distribution high-density polyethylene injection molding grade with a nominal melt flow rate of 52 g/10 min under ASTM D1238 at 190°C/2.16 kg and a nominal density of 0.954 g/cm³ under ASTM D1505. The application-specific processing windows presented below are compiled for raw material qualification, tooling specification, and supplier evaluation. Published data for non-standard tooling configurations is limited.

    On multi-cavity thin-wall dairy packaging lines, ALATHON M5372 is used when wall sections below 0.60 mm require a longer flow length at reduced injection pressure. Melt flow-rate measurement under ASTM D1238 at 190°C/2.16 kg yields 52 g/10 min, but runner balance and hot-runner tip geometry still control short shots in 32- to 64-cavity stack tools. Direct food-contact compliance rests on 21 CFR 177.1520(c) Items 3.1a and 3.2a, EU Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm², and China GB 4806.7-2016 where national certification applies. At the compounding hopper, virgin resin is processed at 100 wt% or with a food-contact white masterbatch at 2.0 wt% ± 0.5 wt%; slip amide concentrate for lid denesting may be added at 0.1–0.3 wt% of the final compound. The injection molding process on 350–650 t hydraulic or hybrid presses with general-purpose screws of 22:1–25:1 L/D and compression ratio 2.5:1–3.0:1 operates with barrel zones from 220°C to 250°C, mold temperature 8–20°C, fill time 0.25–0.45 s, hold pressure 45–60 MPa, back pressure 2–5 MPa, and total cycle 4.5–6.5 s. In production-scale lines, insufficient cooling-water turbulence is observed as stacking-ledge dimensional variation, while mold temperatures above 20°C increase demolding flash. Pre-drying is unnecessary below 60% relative humidity; exposed resin held above 60% RH should be dried for 2 h at 70°C to reduce surface splay. Terminal finished forms include 8 oz–32 oz dairy tubs, portion cups, and snap lids.

    What Limits Gate Freeze Time in 48- to 96-Cavity Closure Molding?

    Closure and overcap production from ALATHON M5372 is dominated by gate-freeze dynamics in valve-gate and tunnel-gate hot-runner systems, where small gate diameters of 0.5–0.8 mm create the primary pressure-drop boundary. If the gate freezes before hold-pressure transfer is complete, the tamper-evident bridge and knurl diameters drift beyond dimensional tolerance; if the gate remains open too long, hot-runner stringing and additional screw recovery time reduce overall equipment effectiveness. Direct food-contact closures require 21 CFR 177.1520(c), EU Regulation (EU) No 10/2011, and manufacturing hygiene under 21 CFR Part 174.5 and EU Regulation 2023/2006. Formula addition typically includes a 5% erucamide slip masterbatch at 1.5–2.5 wt%, a fluoropolymer-free processing aid at 0.2–0.5 wt%, and a food-contact-compatible silicone release additive at 0.1–0.2 wt%; higher erucamide concentrations reduce coefficient of friction but may plate out on mold vents and hot-runner components. Injection molding on 48- to 96-cavity stack tools with 250–500 t clamp force uses melt temperature 215–245°C, hot-runner manifold temperature 220–240°C, mold temperature 10–15°C, hold pressure 35–50 MPa, back pressure 3–8 MPa, and cycle time 3.8–6.0 s depending on cap weight and bridge thickness. A documented production-scale failure mode is vent erosion at the parting line after extended runs above 250,000 cycles; increased flash and reduced gate sealing result. Finished product types include non-carbonated beverage closures, condiment closures, dairy overcaps, and secondary overcaps for cosmetic or pharmaceutical bottles where food-contact clearance is not required. Published data for carbonated soft-drink pressure-retention closures based on M5372 is limited, and such applications require separate CO₂ retention qualification.

    Industrial open-head pails, locking lids, and packagings for regulated liquids

    When open-head pails are molded for UN-rated transport of viscous liquids, the lower injection pressure requirement of ALATHON M5372 assists in filling thin handle bridges and lid gasket seats without excessive cavity-pressure peaks. Regulatory compliance for dangerous goods packagings is determined by UN Model Regulations Chapter 6.1; removable-head plastic jerricans are commonly classified as packaging code 3H2, while larger open-head plastic drums are 1H2, with performance testing under 49 CFR Part 178 or national equivalents. REACH Regulation (EC) No 1907/2006 Article 33 communication duties apply if SVHC content in the article exceeds 0.1 wt%. The compound addition for outdoor or colored pails includes UV stabilizer masterbatch at 1.0–2.0 wt% and carbon black or color concentrate at 2.0–4.0 wt%; a dual-use food-contact masterbatch is required only for pails marketed into food logistics. Injection molding on 500–900 t presses with accumulator assist or servo pumps uses melt temperature 215–240°C, mold temperature 15–25°C, hold pressure 25–40 MPa, cooling time 18–35 s, and total cycle 35–55 s for a 20 L pail. On production lines, handle bridges are observed as the highest-risk area for sink marks and impact fracture; processors delay gate freeze by enlarging the gate to 7–9 mm and reducing hold-pressure taper. Terminal finished products include 5 L, 10 L, 15 L, and 20 L open-head pails for paints, coatings, chemical concentrates, detergent powders, and water-based emulsions.

    Houseware storage products such as stackable totes, drawer dividers, and modular shelf bins are molded from ALATHON M5372 on medium-tonnage injection presses with clamp force 150–350 t, barrel temperature 200–230°C, and mold temperature 10–25°C. The material addition is typically 0.5–2.0 wt% color concentrate and, for outdoor items, 1.0 wt% UV stabilizer concentrate; general-purpose European distribution is assessed under REACH Regulation (EC) No 1907/2006 Annex XVII restricted substance limits, while RoHS Directive 2011/65/EU applies only to electrical or electronic components integrated into the article. This scenario does not include direct food-contact claims; if the storage article is used in food processing environments, compliance with FDA 21 CFR 177.1520(c) and EU Regulation (EU) No 10/2011 requires migration testing on the finished article. Processing is established on cold sprue or tunnel-gate tooling; no pre-drying is required below 60% relative humidity, and the main production-scale defect is flow-line visibility at high melt temperature. Finished types include stackable totes, storage crates, drawer dividers, modular shelf bins, and desk organizers.

    When Cosmetic Jars and Overcaps Replace Polypropylene for Environmental Stress-Crack Resistance

    Because ester-based solvents and high-pH emulsions generate radial cracking in polypropylene snap fits, cosmetic packaging suppliers evaluate ALATHON M5372 for opaque jars and overcaps that require consistent hoop stress and snap-fit retention. The resin’s narrow molecular-weight distribution supports uniform shrinkage, but it does not provide glass-like clarity; matte and pigmented finishes are the practical design envelope. Regulatory assessment for finished cosmetic packaging in the EU is governed by REACH Regulation (EC) No 1907/2006 Annex XVII restricted substances and the Cosmetic Products Regulation (EC) No 1223/2009 Article 10 safety assessment, which requires packaging interaction to be considered in the product safety report. For dual-use cosmetic food-contact claims, the finished article must also meet 21 CFR 177.1520(c) and EU Regulation (EU) No 10/2011 migration limits. Formulation addition is typically 1.5–2.5 wt% pigmented masterbatch, with matting or pearlescent concentrates added at 1.0–2.0 wt% when specified; migratory slip additives are limited to 0.2–0.5 wt% because exudation can alter cosmetic base texture. Injection molding with polished SPI A-1 cavity surfaces, valve-gate or cold-runner systems, clamp force 150–350 t, melt temperature 220–250°C, mold temperature 15–25°C, and cycle time 20–35 s for wall thickness 1.5–3.0 mm is typical. Production lines using textured cavity surfaces report mold-release inconsistency below 15°C mold temperature; increasing mold temperature to 20–25°C improves snap-fit geometry release. Terminal finished products include opaque jar bodies, secondary overpack shells, compact bases, and overcaps for fragrance pumps.

    Aerosol overcaps are not pressure vessels, but their wall stock must survive drop testing

    In high-speed aerosol filling lines, overcaps and trigger-sprayer shrouds molded from ALATHON M5372 require dimensional stability on vibratory bowl feeders and rotary capping equipment. The relevant regulatory framework is limited to the EU Aerosol Dispensers Directive 75/324/EEC for the filled can assembly and REACH Regulation (EC) No 1907/2006 for article restrictions; product-specific safety requirements apply at the formula level and do not impose direct migration testing on the overcap. The formulation is generally M5372 at 98.0–99.5 wt% with color masterbatch at 1.0–2.0 wt% and slip agent at 0.2–0.5 wt% to maintain nesting and denesting behavior on automated sorting lines. Injection molding uses clamp force 150–300 t, melt temperature 210–240°C, mold temperature 10–20°C, and cycle time 15–25 s; undercut side actions for aerosol can rim snap geometries require consistent ejection temperatures to prevent white stress marks. In high-speed assembly, a common production failure is outer-diameter ovalization due to uneven mold cooling, which increases jamming rates on rotary cap elevators. Finished types include overcaps for air freshener, shaving foam, spray paint, insecticide, and household trigger-sprayer shrouds.

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    Certification & Compliance
    More Introduction

    LyondellBasell HDPE ALATHON M5372 is a high-density polyethylene resin designated for injection molding applications. The product is supplied in pellet form as a high-flow, narrow-molecular-weight-distribution ethylene polymer produced by catalytic polymerization. Routine specification testing is performed according to ASTM D792 for density and ASTM D1238 at 190°C and 2.16 kg for melt flow rate. Because grade-specific nominal values appear on certificates of analysis and are batch-dependent, the following technical description distinguishes class-typical behavior from lot-specific data where published information for this specific configuration is limited. The resin is used in rigid packaging, pails, crates, thin-wall containers, housewares, and industrial parts in which short cycle time, reproducible part mass, and adequate stiffness are primary processing requirements.

    What Distinguishes ALATHON M5372 From Extrusion-Grade HDPE Resins?

    Compared with blow molding, film, and pipe extrusion grades, ALATHON M5372 occupies a higher-melt-flow segment of the high-density polyethylene family. Blow molding grades typically maintain lower melt flow rates to provide parison hang strength and melt stability, while bimodal pipe grades retain a high-molecular-weight fraction for environmental stress crack resistance and slow crack growth resistance. The injection molding position of ALATHON M5372 reduces fill pressure in long flow-length, multi-cavity tools and permits thinner walls. The narrower molecular weight distribution also limits die swell and enhances shot-to-shot consistency, but it reduces melt strength relative to extrusion grades. Thus, the product is not intended for blown film lines that require bubble stability or for extruded pipe service where long-term hydrostatic performance is governed by ISO 9080 and related pressure-life evaluations. In these applications, a fractional-melt or bimodal high-density polyethylene is generally specified instead. Comparative rheological data are obtained by ASTM D1238, ISO 1133-1:2022, and capillary viscosity testing under ASTM D3835.

    Standard Characterization Matrix for ALATHON M5372 Injection Molding Evaluations
    Test methodProperty measuredProcessing or design relevance
    ASTM D1238Melt flow rate at 190°C/2.16 kgControls injection pressure, fill capacity, and thin-wall capability
    ASTM D792DensityDetermines stiffness, shrinkage level, and barrier contribution
    ASTM D638Tensile yield strength and elongation at breakShort-term load performance under assembly and service stress
    ASTM D790Flexural modulusStacking rigidity of containers, crates, and pails
    ASTM D256Notched Izod impactImpact resistance at room and low temperature
    ASTM D1693Environmental stress crack resistanceService life under chemical and residual stress
    ASTM D955Mold shrinkageDimensional stability and warpage control
    ASTM D2240Shore D hardnessSurface indentation and scratch response

    On high-speed injection molding lines, ALATHON M5372 is processed in conventional reciprocating-screw machines. Production-scale trials commonly use screws with 20:1 to 25:1 L/D ratios and compression ratios between 2.5:1 and 3.5:1. Barrel zone settings from 210°C to 260°C are typical, with nozzle temperatures held below 270°C to reduce molecular weight loss and degradation. Mold temperatures between 10°C and 50°C are used in rigid packaging; lower mold temperatures shorten cycle time but increase residual stress and warpage sensitivity. Back pressure in the range of 0.3 MPa to 1.0 MPa and screw surface speed below 0.5 m/s maintain melt homogeneity without excessive shear heating. The shot size should remain between 50% and 70% of barrel capacity, with a consistent cushion of 3 mm to 6 mm to allow adequate pack and hold pressure transfer. Gate freeze time, not plastication rate, often limits cycle time in thin-wall packaging tools.

    Melt Rheology and Gate Freeze-Off in Multi-Cavity Tools

    Melt viscosity of ALATHON M5372 is best characterized by capillary rheometry under ASTM D3835 at 190°C and 210°C, with shear rate sweeps from 100 s⁻¹ to 10,000 s⁻¹. The narrow-molecular-weight-distribution structure yields pronounced shear thinning at typical injection shear rates. A power-law flow behavior index below 0.5 is common for this class of high-density polyethylene, indicating a strong reduction in apparent viscosity as shear rate rises. In multi-cavity tools, this shear thinning improves filling of long flow paths but does not eliminate cavity imbalance caused by runner geometry. Gate freeze-off is controlled by cavity pressure decay after switchover from velocity to pressure control. If gate freeze occurs too early, pack pressure cannot compensate volumetric shrinkage and the part may show sink marks, voids, or dimensional shortfall. If gate freeze occurs too late, cycle time increases and the gate region may remain soft during ejection. Mold-filling simulation should use pressure-dependent viscosity and pvT data for this specific resin rather than single-point melt index values. Production nozzles commonly see filling pressures from 60 MPa to 120 MPa, depending on wall thickness and flow length.

    Because injection-molded containers are subject to top-load, drop impact, and stacking, the resin is evaluated by short-term and long-term mechanical tests. In high-density polyethylene of this class, tensile yield strength is typically measured by ASTM D638 with a Type IV specimen and crosshead speed of 50 mm/min. Class-typical tensile yield strength values reported in industrial literature fall between 22 MPa and 32 MPa, while flexural modulus measured by ASTM D790 commonly ranges from 900 MPa to 1,450 MPa. Notched Izod impact by ASTM D256 is generally lower for injection-grade HDPE than for high-molecular-weight extrusion grades because of lower molecular weight and narrower molecular weight distribution. Environmental stress crack resistance measured by ASTM D1693 condition B is also lower than that of bimodal pipe grades. In aggressive detergent, surfactant, or oil-contaminated environments, long-term stress crack performance should be evaluated on the final molded part rather than assumed from resin class alone. Published data for ALATHON M5372 in aggressive environments is limited; lot-specific testing is required where ESCR is acceptance-critical.

    When Narrow Molecular Weight Distribution Alters Shrinkage and Warpage

    Shrinkage of injection-molded high-density polyethylene is anisotropic and is measured by ASTM D955. Typical linear mold shrinkage for this class is between 0.015 mm/mm and 0.035 mm/mm, with differences between flow direction and cross-flow direction. A narrower molecular weight distribution can improve part-to-part dimensional reproducibility but may also increase differential shrinkage when packing is nonuniform. Gate location, wall thickness, melt temperature, mold temperature, cooling time, and pack pressure are the controlling variables. Warpage results from nonuniform volumetric contraction, especially at abrupt wall thickness transitions, rib bases, and corner sections. In thin-wall containers with wall thickness below 1.0 mm, rapid gate freeze limits the transfer of pack pressure, making shrinkage control more sensitive to mold temperature consistency. Multi-cavity tools with unbalanced runner systems can produce systematic cavity-to-cavity mass variation even when the resin itself is consistent. Dimensional acceptance should therefore be based on capability studies using production-scale tooling rather than laboratory plaques.

    Substitution of ALATHON M5372 for a general-purpose fractional-melt high-density polyethylene in an injection-molded cap, closure, or thin-wall container can reduce peak injection pressure and shorten cycle time, but may lower environmental stress crack resistance and impact performance. Conversely, replacement of a polypropylene random copolymer with this HDPE grade may improve low-temperature impact and stress crack resistance in many detergent contact applications, while reducing continuous-use temperature and surface hardness. Crystalline melting point for HDPE of this class is typically observed from 130°C to 137°C by ASTM D3418. Heat deflection temperature under 0.455 MPa by ASTM D648 is commonly between 70°C and 85°C. These trade-offs should be evaluated using the same standard methods on the intended production tooling.

    Regulatory compliance for ALATHON M5372 is targeted to the intended application. For food-contact uses in the United States, the resin is assessed under 21 CFR 177.1520 for olefin polymers, including composition and extractables requirements for the relevant food type and temperature. In the European Union, compliance is evaluated under Regulation (EU) No 10/2011 on plastic materials intended to come into contact with food. Overall migration testing is carried out using the EN 1186 series, and specific migration testing is applied where relevant. Chemical registration obligations are addressed through REACH under Regulation (EC) No 1907/2006. For electrical and electronic equipment components, RoHS compliance is assessed under Directive 2011/65/EU. Final statements of compliance should be obtained from the supplier for the specific lot and end-use condition.

    Which Processing Boundaries Limit Use in High-Speed Packaging Lines?

    The product is not hygroscopic and does not routinely require pre-drying. If condensation or surface moisture is present, a hopper dryer at 80°C for 2 h is sufficient; higher drying temperatures above 90°C may cause pellet sticking and bridging. The melt should not be held above 280°C for extended residence time because thermal oxidation reduces molecular weight and discolors the part. Continuous-use temperature for molded HDPE parts is generally in the range of 60°C to 80°C, with short-term intermittent exposure below 90°C where load is limited. The resin has limited resistance to strong oxidizing acids, chlorinated solvents, and certain aromatic hydrocarbons; chemical compatibility should be verified for each contact fluid. Avoid combination with strong oxidizing agents at processing temperatures because exothermic decomposition may occur. Storage should be in a dry area away from direct sunlight and ultraviolet exposure. Molded parts under sustained stress may fail by environmental stress cracking when exposed to detergents, alcohols, or unsaturated oils; the use of a higher-molecular-weight or bimodal polyethylene is required where this failure mode is unacceptable.

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