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Arya Sasol HDPE 5510

    • Product Name: Arya Sasol HDPE 5510
    • 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 198443
    Polymer Type High Density Polyethylene (HDPE)
    Density 0.955 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 0.35 g/10 min
    Tensile Strength At Yield 28 MPa
    Tensile Strength At Break 30 MPa
    Elongation At Break >600%
    Flexural Modulus 1200 MPa
    Izod Notched Impact Strength 23 C 15 kJ/m²
    Vicat Softening Temperature 125°C
    Melting Point 132°C
    Environmental Stress Cracking Resistance Escr >1000 h
    Hardness Shore D 65
    Water Absorption <0.01%
    Bulk Density 0.55 g/cm³

    As an accredited Arya Sasol HDPE 5510 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Arya Sasol HDPE 5510 is supplied in 25 kg polyethylene bags, with 55 bags per pallet (1,375 kg total).
    Container Loading (20′ FCL) Arya Sasol HDPE 5510: 20′ FCL loading in 25 kg bags, approximately 22 MT per container, palletized or floor-loaded.
    Shipping Arya Sasol HDPE 5510 is a non-hazardous high-density polyethylene supplied in 25 kg woven bags, palletized and shrink-wrapped. It ships in dry general-purpose containers, trucks, or railcars at ambient temperature. Keep dry, ventilated, away from direct sunlight, heat, and contamination. No UN hazard class or special transport placards required.
    Storage Store Arya Sasol HDPE 5510 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep pellets in original sealed bags on pallets, off the floor, and protected from moisture, dust, and contamination. Use first-in, first-out. Avoid prolonged UV exposure and excessive stacking. Maintain normal ambient temperatures.
    Shelf Life Arya Sasol HDPE 5510 typically has a 24-month shelf life when stored cool, dry, sealed, and away from direct sunlight.
    Application of Arya Sasol HDPE 5510

    Thin-wall dairy packaging produced on high-cavitation injection lines places a narrow processing window on the base polymer, because melt front length-to-thickness ratio in 1.0 mm wall sections exceeds 200:1 across a 12-cavity or 24-cavity tool. Arya Sasol HDPE 5510 is introduced into such configurations as the primary virgin resin, with the manufacturer’s standard lot typically listing melt mass-flow rate of 10 g/10 min at 190 °C/2.16 kg when tested to ISO 1133-1:2022 and density of 0.955 g/cm³ under ISO 1183-1:2019. The high MFR2.16 permits a narrower barrel temperature profile of 225 °C to 245 °C on a general-purpose reciprocating screw with 20:1 to 22:1 L/D, reducing molecular-weight degradation during residence at high injection speeds. Mould temperature is held between 12 °C and 25 °C because higher temperatures lengthen the cooling-dominated portion of the cycle and increase sink marks around circumferential ribs. Cavity filling is controlled by injection speed rather than pressure, with production-scale settings commonly falling between 180 mm/s and 240 mm/s at the screw-return transducer, corresponding to hydraulic injection pressure of 90 MPa to 120 MPa in thin-wall tools with polished S136 steel. Hold pressure is limited to 35 MPa to 55 MPa and pack time is kept at 1.5 s to 3.0 s because the sealing ledge remains thick enough to shrink after gate freeze. Pre-drying is not normally required below 60% relative humidity; where sacks are exposed to RH > 60% for more than 24 h, a hopper dryer set at 70 °C for 2 h is applied to prevent splay. Formulation in this application maintains virgin HDPE 5510 at 96.0 wt% to 98.0 wt%. White or pigmented masterbatches of 2.0 wt% to 4.0 wt% are metered through a gravimetric side-feeder; for dairy containers, the masterbatch typically contains 50% titanium dioxide in an LLDPE carrier selected to maintain total migration fall-out. An acid-neutralizing processing aid at 0.02 wt% to 0.08 wt% is permitted where catalyst residues generate discolouration during start-up, but higher addition rates reduce top-load stiffness and increase plate-out at the vent. Food-contact compliance is evaluated against FDA 21 CFR 177.1520(c) for olefin polymers used in contact with aqueous and acidic food types with hot-fill conditions up to 100 °C; under EU Regulation (EU) No 10/2011 Annex II, the total migration limit is 10 mg/dm² of food-contact surface, with the same material lot verified by EN 1186-1:2002 migration testing. For converters supplying dairy processors, internal specifications commonly cite EC 1935/2004 for traceability and ISO 9001:2015 for batch documentation. Terminal products in this segment include 0.8 mm to 1.2 mm wall margarine tubs, rectangular spread containers, dairy portion packs, and associated snap lids where the olefin polymer’s low-temperature drop resistance prevents cracking at −20 °C at line speed.

    Closure Core Release, Undercut Geometry, and the 8 °C Mould Circuit

    For non-carbonated beverage and dairy closures, the limiting economic variable is not peak injection pressure but the release of the part from the core pin after the tamper-evident band has formed its undercut. Arya Sasol HDPE 5510 is used as the base resin at 97.5 wt% to 99.0 wt%. Colour masterbatch is added at 0.5 wt% to 1.5 wt%, erucamide slip masterbatch at 0.05 wt% to 0.15 wt% total erucamide concentration, and a phenolic/phosphite antioxidant package at 0.03 wt% to 0.08 wt%. Erucamide additions above 0.15 wt% are not used in this sector because they create plate-out on the core pins and reduce adhesion of pad-printed date codes on the closure top deck. In 24-cavity stack mould tools, cycle time typically falls between 4.5 s and 8.0 s; core temperature rather than cavity temperature controls warpage of the closure skirt. Mould chiller set points between 8 °C and 15 °C on the core circuit allow the undercut to shrink sufficiently for ejection, while the cavity plate is maintained at 15 °C to 20 °C. Barrel feed-throat cooling is held at 45 °C to 55 °C to prevent bridging of regrind. Injection speeds of 250 mm/s to 350 mm/s are used to maintain a melt front velocity above 250 mm/s and avoid flow lines at the hinge of the tamper-evident band. Peak hydraulic pressure is limited to 130 MPa to avoid core shift in tools with unsupported core length-to-diameter ratio below 3:1. Closures sold into EU dairy and beverage filling lines are assessed under FDA 21 CFR 177.1520(c), EU Regulation (EU) No 10/2011, and the migration testing method EN 1186-1:2002. Specific migration of erucamide is controlled by EU 10/2011 Annex I restrictions, and converters measure torque retention after sterilisation by hydrogen peroxide at 35% w/w concentration at 55 °C. Terminal products include 38 mm and 48 mm three-leaf tamper-evident closures for high-density polyethylene milk bottles, single-piece flip-top caps for drinkable yoghurt, and 55 mm caps for diluted fruit concentrates.

    Open-top pail moulding for industrial fluids places the injection unit on a different operating envelope from high-cavitation packaging tools. The process handles shot weights of 1.2 kg to 2.8 kg across single-cavity or two-cavity tools. Arya Sasol HDPE 5510 is selected as the primary injection moulding grade because its flowability at 10 g/10 min supports filling of thick circumferential ribs and sealing ledges without excessive melt temperature. Barrel settings usually fall between 220 °C and 240 °C; a flat profile is maintained because overshooting the front zone above 245 °C causes visible streaking and increases odour in food-compatible pail liners. Clamp force requirements scale with projected part area, with production lines using 800 t to 1,200 t hydraulic clamp units for 20 L to 25 L pails, while 5 L pails may run in two-cavity tools at 450 t to 600 t. Injection speed is set to 80 mm/s to 150 mm/s and pack pressure at 50 MPa to 70 MPa, with pack time held for 12 s to 18 s to compensate for high volumetric shrinkage in the thick rim. Formulation ratio maintains HDPE 5510 at 96.0 wt% to 98.5 wt%, carbon black masterbatch at 1.0 wt% to 3.0 wt% for outdoor-grade pails, UV stabiliser masterbatch at 0.2 wt% to 0.5 wt% supplied as hindered amine light stabiliser plus carbon black, and fluoropolymer processing aid at 0.02 wt% to 0.08 wt% only where melt fracture is detected at the gate. Industrial packaging with this resin is assessed under ISO 20848-3:2018 for stacking strength, ASTM D256-23 for notched Izod impact at 0 °C, and UN Manual of Tests and Criteria Part III for dangerous goods certification where the moulded pail is classified as 1H2 or 3H2 depending on closure type. For food-contact pails, FDA 21 CFR 177.1520 and EU 10/2011 migration testing apply. Terminal products include 5 L paint pails, 20 L food-ingredient open-top containers, and 25 L industrial chemical pails with steel or plastic wire handles.

    When High-Gloss Housewares Demand Low Gate Vestige in Multi-Cavity Tooling

    In high-cavity housewares production, gate vestige on the visible surface is a primary reject criterion because HDPE parts with 2 mm to 4 mm wall thickness retain visible blush around the valve gate when the mould is overpacked. Arya Sasol HDPE 5510 is used as the virgin fraction at 98.0 wt% to 99.0 wt%, with 1.0 wt% to 2.0 wt% colour masterbatch and 0.05 wt% to 0.1 wt% external mould release only when ejection force exceeds a preset threshold. The material’s rheology supports filling of family tools with eight to twenty-four cavities; melt temperature is controlled at 230 °C to 250 °C, mould temperature at 30 °C to 60 °C, and screw recovery is set so that cycle time falls between 18 s and 30 s depending on wall section. Multi-cavity tooling with sequential valve gating is preferred; manifold balancing to within ±3 °C of set point prevents asymmetric filling and gloss banding on sidewalls. Hot runner tips are polished to SPI A2 or better. Fill speed is limited to 100 mm/s to 180 mm/s because higher speed raises shear heating and causes visible flow fronts on high-gloss flat bases. Pack pressure is set to 35 MPa to 50 MPa with transfer by screw position, not time, to prevent overpacking at the gate. Compliance for housewares used in food storage relies on FDA 21 CFR 177.1520(c), EU Regulation (EU) No 10/2011, and REACH Regulation (EC) No 1907/2006 for SVHC content below 0.1% w/w. Surface quality criteria are often defined internally by ISO 2813:2014 gloss at 60° geometry above a converter-specified limit, together with ISO 179-1:2010 Charpy impact to control cracking of snap hinges. Terminal products include modular storage cubes, transparent-lid food storage boxes, drawer organisers, and wardrobe bins, where the high-flow grade reduces warpage in rectangular bases compared with lower-MFR HDPE when mould temperatures are above 40 °C.

    Material handling crates and pallets operate at the intersection of low-temperature toughness and high stacking stress, particularly in cold-room storage at −20 °C. Arya Sasol HDPE 5510 is specified as the virgin base at 90 wt% to 98 wt%, with post-industrial HDPE regrind at 2 wt% to 10 wt% only where the converter has validated batch-to-batch impact retention. A UV-stabilised masterbatch is metered at 0.5 wt% to 2.0 wt% for pallets stored outdoors; the same masterbatch contains a hindered amine light stabiliser at 10% actives and a grey or black pigment package. Nucleating agent is limited to 0.05 wt% to 0.20 wt% where high crystallinity initiates premature cracking at gate corners. Production lines for heavy-duty crates typically use 1,200 t to 2,500 t clamp force machines with shot sizes of 5 kg to 20 kg. Structural-foam injection moulding is applied to reduce part weight by 10% to 20% while maintaining section modulus; nitrogen gas at 0.2 MPa to 0.8 MPa is injected through the screw after plasticising, producing a closed-cell core with a compact skin. Melt temperature is held at 220 °C to 235 °C, and fill speed is reduced to 50 mm/s to 100 mm/s to allow cell nucleation. Cooling time dominates the cycle, often 40 s to 80 s, and premature ejection must be avoided because residual core gas pressure causes post-mould blistering. Clamp tonnage is kept above the gas packing pressure multiplied by the projected area; otherwise surface splay appears at vent locations. Compliance testing for pallets and crates includes ISO 8611-1:2021 for pallet load capacity and racking, ISO 2247:2000 for vibration, and ASTM D638-14 for weld-line tensile strength from multi-gate filling. REACH Regulation (EC) No 1907/2006 and RoHS Directive 2011/65/EU apply where the crates enter electrical-component logistics. Terminal products are nestable transport crates for beverage bottles, collapsible distribution boxes, closed-deck pallets for pharmaceutical logistics, and ventilated agricultural crates.

    Why Is Sequential Valve Gating Used for 48-Cavity Cosmetic Cap Tools?

    For cosmetic flip-top closures of 1.2 mm to 2.5 mm wall thickness, sequential valve gating becomes a processing requirement rather than an optional tooling feature because the long flow length from a single sprue would require melt temperature above the degradation threshold of the grade. Arya Sasol HDPE 5510 is compounded in this segment with a metallic or pearlescent masterbatch at 0.5 wt% to 1.5 wt%, a fluoropolymer processing aid at 0.02 wt% to 0.08 wt% where surface drag marks appear, and the balance virgin resin at 96.0 wt% to 98.5 wt%. Melt temperature is maintained at 230 °C to 250 °C, mould temperature at 30 °C to 50 °C, and injection speed at 120 mm/s to 200 mm/s. Transfer to pack pressure is made by screw position at 8 mm to 12 mm before full fill, with pack pressure limited to 30 MPa to 45 MPa for 1.5 s to 3.0 s because higher pack energy distorts the hinge geometry and creates surface blush around the gate. The 0.2 mm to 0.4 mm hinge section is placed on the cavity side of the tool and is filled at the highest melt front velocity, but the pack profile is then brought to zero early to prevent hinge embrittlement. Cosmetic packaging is governed by Regulation (EC) No 1223/2009 only for the finished cosmetic formulation; the moulded polymer article is evaluated under EU Regulation (EU) No 10/2011 only where the cap includes a sealing liner contacting food or oral-care fluid. For skin-care jars, the converter’s declaration of conformity primarily references REACH Regulation (EC) No 1907/2006 and EU Packaging and Packaging Waste Directive 94/62/EC, with specific migration of heavy metals below 100 mg/kg by weight. Terminal products include flip-top caps for shampoo bottles, screw caps for body lotion tubes, single-piece jars for creams, and elliptical overcap shells for deodorant packages.

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    Certification & Compliance
    More Introduction

    Arya Sasol HDPE 5510 is presented as a medium-flow injection-moulding high-density polyethylene. Supplier technical documentation lists a nominal density of 0.955 g/cm³ and a melt flow rate of 10 g/10 min at 190 °C under 2.16 kg. These indicators are used for grade preselection and are not contractual lot release limits. The datasheet values summarised in Table 1 are drawn from publicly available supplier documentation and should be verified against the current certificate of analysis before tooling or process specification.

    PropertyTest MethodNominal Value
    Melt flow rate at 190 °C/2.16 kgISO 1133-1:202210 g/10 min
    DensityISO 1183-1:20190.955 g/cm³
    Tensile stress at yield, 50 mm/minISO 527-2:201226 MPa
    Tensile strain at break, 50 mm/minISO 527-2:2012>200%
    Flexural modulusISO 178:20191050 MPa
    Notched Charpy impact, 23 °CISO 179-1:20104.0 kJ/m²
    Vicat softening temperature, A50ISO 306:2022124 °C
    Heat deflection temperature, 0.45 MPaISO 75-2:201374 °C
    Hardness, Shore DISO 868:200364

    The grade designation does not encode the additive package. Stabiliser and lubricant composition must be confirmed from the safety data sheet and product specification for the specific lot.

    What Does the 5510 Designation Indicate in the Arya Sasol HDPE Portfolio?

    The numerical designation is decoded in supplier literature as 55 for density and 10 for flow. The first two digits correspond to a nominal density of 0.955 g/cm³; the final two digits correspond to a melt flow rate of 10 g/10 min at 190 °C under 2.16 kg. This decoding should not substitute for measurement. In portfolio comparisons, HDPE 5510 sits between lower-flow HDPE 5050 and higher-flow HDPE 5620. It offers lower injection pressure than HDPE 5050 and generally better strain-at-break retention than HDPE 5620, but it does not match the melt strength or environmental stress-crack resistance of a high-molecular-weight blow-moulding HDPE. Comparative ratings are conditional on mould geometry, cooling rate, and end-use chemical exposure.

    The crystallinity of HDPE 5510 can be estimated from density by a two-phase model. Using an amorphous polyethylene density of 0.853 g/cm³ and a crystalline polyethylene density of 1.000 g/cm³, a density of 0.955 g/cm³ corresponds to a crystallinity of approximately 69.4%. A lower-density HDPE at 0.950 g/cm³ would show roughly 66.0% crystallinity. Crystallinity influences flexural modulus, barrier resistance, and chemical swelling. Differential scanning calorimetry at 10 °C/min cooling under ISO 11357-3:2018 on analogous HDPE grades typically records a crystallisation exotherm in the range 115–120 °C; published data for this exact grade is limited. The melt flow rate does not define crystallinity; density and thermal history do. Therefore, mould cooling rate controls in-process crystallinity and final shrinkage.

    Cooling rate also determines crystal thickness distribution. Fast cooling in thin walls suppresses secondary crystallisation and lowers final density; slow cooling in thick sections increases crystallinity and shrinkage. For a 0.955 g/cm³ nominal resin, moulded density can vary by approximately ±0.005 g/cm³ depending on cooling. Nominal density cannot be used alone for critical dimension calculations without moulded-part density verification by ISO 1183-1:2019.

    Shear-Thinning, Spiral-Flow Length, and Injection-Pressure Partitioning

    A single-point melt flow rate does not define mould-filling behaviour. HDPE melts are non-Newtonian and shear-thinning. For a comparable 10 g/10 min HDPE at 210 °C, apparent capillary viscosity is often reported near 800 Pa·s at 100 s⁻¹ and falls below 150 Pa·s at 1000 s⁻¹. Published Carreau-Yasuda coefficients for this specific grade are limited; therefore, filling simulation should use measured capillary rheometry data rather than single-shear-rate extrapolation. Capillary measurement should follow ISO 11443:2021.

    Pressure partitioning in a multicavity crate mould depends on gate design. In a gate with diameter 0.8 mm, the gate may consume 20–30% of total injection pressure. A tunnel gate can add 15–20 MPa relative to a direct sprue gate of equivalent area. Cavity pressure for high-density polyethylene is commonly estimated between 25 MPa and 40 MPa. A conservative design value of 35 MPa means an 8000 kN clamp force press can handle a projected area of approximately 0.23 m² before flash risk increases. Clamp force is not a melt-flow property but is the limiting machine constraint in large crate and pallet tools.

    Short-shot prevention also depends on spiral flow length. Published spiral flow values for this exact grade are limited, but medium-flow HDPE grades at 2.5 mm spiral depth and 80 MPa injection pressure are often in the 35–50 cm range at 210 °C. Spiral tests should be run in the intended moulding machine because screw recovery, back pressure, and thermocouple depth all shift the result.

    Screw recovery is affected by back pressure. At back pressures of 5–10 MPa, melt temperature homogeneity improves but recovery time increases. A back pressure above 15 MPa can raise melt temperature and reduce throughput on a 22:1 L/D screw. The injection velocity profile should be linear to constant, with injection time of 0.5–1.5 s for thin-wall pails and 2–4 s for thick-walled crates. These ranges are starting points and must be confirmed by short-shot study.

    Production-scale conditions are bounded by melt temperature and mould temperature. Field reports from injection lines running 22:1 to 24:1 L/D screws and compression ratios of 2.5:1 to 3.5:1 show stable processing at melt temperatures of 200–230 °C. Melt temperatures below 190 °C have been associated with hesitation marks and higher hydraulic pressure demand. Melt temperatures above 240 °C can raise purge yellowness and extend cooling time. Mould temperatures of 20–40 °C are usually adequate; raising mould temperature above 60 °C may add 8–12 s to cooling time in thin-wall tools without a measurable increase in notched Charpy impact under ISO 179-1:2010.

    HDPE is not hygroscopic. Storage at relative humidity above 60% can leave surface moisture that produces splay. Pre-drying at 80 °C for 2 h in a desiccant dryer is typical. Drying above 90 °C for more than 4 h is not recommended because oxidative change can shift yellowness index. Regrind addition is viable up to 20 wt% for non-appearance industrial parts. Beyond 20 wt%, screw recovery variation and Charpy scatter can exceed ±5% unless regrind is homogenised and tested to ISO 1133-1:2022. The maximum permissible regrind fraction in food-contact packaging is set by regional certification, not by viscosity alone.

    Mould shrinkage in HDPE is anisotropic. Typical published ranges for medium-flow HDPE injection mouldings are 1.8–2.2% in the flow direction and 1.3–2.0% in the transverse direction, depending on wall thickness, gate orientation, and cooling rate. Thick sections above 4 mm can develop sink voids if pack pressure is removed before gate freeze. Holding pressure should be maintained until the gate freezes; the exact time is determined by gate diameter and melt temperature rather than by melt flow rate alone.

    Colour and additive masterbatches shift the melt flow rate. A 2 wt% carbon black masterbatch can change the melt flow rate by approximately ±1 g/10 min depending on carrier resin and pigment loading. Pre-blending should be uniform; uneven mixing in machine hoppers creates variation in moulded-part mass and impact. Use of high-shear mixing screws or pre-compounded masterbatch is preferred.

    When Environmental Stress-Crack Resistance and Notched Impact Dictate Grade Choice

    ESCR is the principal long-term constraint. For a 10 g/10 min injection grade, the lower molecular weight relative to blow-moulding HDPE reduces tie-molecule concentration and ESCR. Literature values for similar medium-flow HDPE injection resins under ASTM D1693-15 Condition B, 10% Igepal CO-630, 50 °C may fall below 20 h F50, while high-molecular-weight blow-moulding grades can exceed 100 h. Published data for this specific grade is limited; therefore, any aggressive-wetting or structural-load application should be validated by bent-strip testing to ISO 22088-2 at the service temperature and chemical concentration.

    Notched Charpy impact at 23 °C is suitable for crates, pails, and storage bins. At -20 °C, HDPE impact resistance drops. Freezer or cold-climate applications should be qualified with instruments cooled to the minimum service temperature. If low-temperature impact is critical, a lower-MFR HDPE or a high-density polyethylene with bimodal molecular weight distribution may be more appropriate.

    Stress cracking is accelerated by residual moulded-in stress. High pack pressure and low melt temperature increase orientation. For detergent or surfactant-containing pails, pack pressure should not be set above the minimum required to prevent sink. A post-moulding stress-relief anneal is not typical but can be used where short-run stress-sensitive parts require validation.

    Continuous exposure to strong oxidising acids, aromatic solvents, or aggressive surfactant solutions at temperatures above 50 °C should not be assumed safe from generic HDPE data. The exact concentration limit should be determined by ISO 22088-2 or ASTM D1693-15. The material should not be melt-blended with polyamide or PET without a defined compatibilisation strategy, because phase separation can reduce weld-line strength and impact.

    The application set for HDPE 5510 includes injection-moulded crates, pails, tote boxes, storage containers, caps and closures with moderate flow requirements, and industrial parts that require a balance of stiffness and processability. It is not selected for large-part extrusion blow moulding because its melt strength is too low to prevent parison sag. In blow moulding, high-load melt flow rate at 21.6 kg is a better classification; this grade is supplied for injection conversion where the 2.16 kg melt flow rate is the relevant control. It is also not intended for high-pressure pipe extrusion under ISO 9080, where a pipe-grade resin with high hydrostatic design stress and slow crack growth resistance is required. Compared with polypropylene of similar melt flow rate, HDPE 5510 has lower density, lower flexural modulus, and generally better ESCR in alkaline and aqueous media; it is selected when low density and environmental stress-crack tolerance outweigh stiffness.

    Compliance Verification and Batch-to-Batch Consistency Checks

    The supplier’s current safety data sheet and product stewardship documentation should be consulted for EU REACH registration status, substance-of-concern screenings under RoHS Directive 2011/65/EU, and any applicable food-contact declarations. No food-contact claim under FDA 21 CFR 177.1520 or Regulation (EU) No 10/2011 is made in this document unless the lot certificate expressly states compliance for the intended end use. Batch-to-batch consistency is typically verified by melt flow rate, density, and notched Charpy impact. Incoming inspection at 1 sample per lot for ISO 1133-1:2022 and 1 sample per lot for ISO 1183-1:2019 is a minimal program; critical applications add tensile yield and ESCR on a reduced frequency. The certificate of analysis should be retained for statistical process control and complaint investigation.

    Standard or RegulationVerification Field
    ISO 1133-1:2022Melt flow rate, lot release and incoming inspection
    ISO 1183-1:2019Density, lot release and formulation drift checks
    ISO 179-1:2010Notched Charpy impact, mechanical acceptance
    ASTM D1693-15Environmental stress-crack resistance, application-dependent validation
    RoHS Directive 2011/65/EURestricted-substance confirmation at homogeneous-material level

    Operational boundaries should be treated as processing and design inputs rather than generic guarantees. For HDPE 5510, the practical melt-temperature window is 200–230 °C, mould temperature is 20–40 °C, and cavity pressure is governed by part thickness and gate design. It is not a direct substitute for blow-moulding or pipe-grade HDPE. Published data for this specific grade is limited for long-term ESCR, spiral flow, and low-temperature impact. Qualification moulds should run actual service-condition tests under ISO 527-2:2012, ISO 179-1:2010, ASTM D1693-15, and the relevant chemical-exposure standard. The grade should be compared with adjacent Arya Sasol HDPE products only after these indicators are measured on the same tool and lot basis.

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