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Braskem HDPE IA59U3

    • Product Name: Braskem HDPE IA59U3
    • 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 659479
    Product Name Braskem HDPE IA59U3
    Manufacturer Braskem
    Polymer Type High Density Polyethylene (HDPE)
    Density 0.958 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 0.30 g/10 min
    Tensile Strength At Yield 30 MPa
    Tensile Strength At Break 38 MPa
    Elongation At Break 600%
    Flexural Modulus 1400 MPa
    Environmental Stress Crack Resistance Escr 10 Igepal F50 >1000 h
    Vicat Softening Point 128°C
    Melting Point 134°C
    Hardness Shore D 66
    Thermal Conductivity 0.45 W/m·K
    Coefficient Of Linear Thermal Expansion 1.2E-4 /°C
    Specific Heat Capacity 1.9 J/g·°C
    Charpy Impact Strength Unnotched 23 C No Break
    Moisture Content <0.1%
    Bulk Density 0.58 g/cm³
    Crystallization Temperature 115°C

    As an accredited Braskem HDPE IA59U3 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Braskem HDPE IA59U3 is typically packaged in 25 kg polyethylene bags, palletized for bulk transport and handling.
    Container Loading (20′ FCL) Braskem HDPE IA59U3 loaded in a 20′ FCL: 25 kg bags on pallets, stretch-wrapped, securely stowed for ocean freight transport.
    Shipping Braskem HDPE IA59U3 ships as non-hazardous solid polyethylene pellets, typically in 25 kg bags, bulk bags, or octabins on pallets. Transport by truck, rail, or sea container under dry, cool conditions. Not classified as dangerous goods; no special temperature control required. Follow local and international transport regulations.
    Storage Store Braskem HDPE IA59U3 indoors in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep packaging closed to prevent moisture, dust, and contamination. Use clean, labeled containers or original bags on pallets. Avoid prolonged UV exposure, excessive stacking, and incompatible materials. Follow local regulations and the SDS.
    Shelf Life Braskem HDPE IA59U3 shelf life is indefinite if stored cool, dry, and ventilated, away from direct sunlight, heat, and contaminants.
    Application of Braskem HDPE IA59U3

    At melt temperatures between 200°C and 225°C, Braskem HDPE IA59U3 fills thin-wall dairy container moulds with nominal wall sections from 0.5 mm to 1.0 mm, a processing window enabled by a melt flow rate of 59 g/10 min when measured according to ASTM D1238 at 190°C under a 2.16 kg load. The application-specific compliance framework is FDA 21 CFR 177.1520 for olefin polymers in food-contact articles and EU Regulation (EU) No 10/2011, with overall migration tested under 10% ethanol and 3% acetic acid simulants per EN 1186-1; density of 0.958 g/cm³ per ASTM D1505 supports thin-wall stiffness-to-weight calculations in cup and lid design. Formulation loading is 100 wt% virgin IA59U3 for unpigmented dairy contact, while pigmented production runs add 1.5–2.5 wt% PE-compatible white masterbatch and incorporate no more than 15 wt% clean in-house regrind recovered from edge trim, with regrind limited by the food-contact quality assurance plan rather than by melt viscosity shift. Production-scale equipment used for this grade includes 250–350 t injection moulding machines with 24- or 32-cavity stack moulds, L/D 22 plasticating units, and valve-gate hot runners with gate diameters of 0.6–0.8 mm; filling times of 0.25–0.40 s create shear heating that permits the melt front to reach the end of a 0.5 mm wall without hesitation marks, while holding pressure of 35–45 MPa compensates for after-fill shrinkage and reduces sink at rib intersections. Mould temperature is maintained between 8°C and 15°C by turbulent-flow water channels, and ejection is delayed until the part centre temperature falls below 60°C to avoid post-mould warpage of thin planar regions. Terminal finished product types include 150–500 mL dairy cups, delicatessen tubs, and thin-wall lids using in-mould labelling, with label adhesion and flatness stabilised by a 24 h post-mould conditioning step at 23°C and 50% relative humidity.

    What Limits Gate Freeze Time in High-Cavitation Beverage and Condiment Closures?

    Because IA59U3 has a melt flow rate of 59 g/10 min under ASTM D1238, closure moulding on 64- and 96-cavity hot-runner systems is not limited by plastication capacity but by gate freeze and sink at the tamper-evident band. Formulation addition ratio is 100 wt% IA59U3 for still water, UHT dairy, and condiment closures; where lower capping line torque is required, 2.0–3.0 wt% PE-based slip masterbatch containing 5% erucamide active is added to reduce the dynamic coefficient of friction on thread flanks, and 0.05–0.10 wt% processing aid is used only when mould release forces elevate ejection pin wear. Compliance is governed by FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011 for food-contact plastics, with overall migration testing under EN 1186-1 and organoleptic screening for off-taste transfer after exposure at 40°C for 10 days in the filled product. The downstream production process runs melt temperature at 190–220°C, mould temperature at 8–15°C, and valve-gate hot runner gate diameter not less than 0.6 mm to prevent premature gate freeze before hold pressure decays; holding pressure is set between 30 MPa and 45 MPa, and cooling time is adjusted to keep the tamper-evident band below 65°C at ejection. On high-speed closure moulds with 2.5 s cycle times, the limiting failure mode is thread ovalisation caused by non-uniform demoulding, which is corrected by increasing mould open delay by 0.2–0.5 s rather than raising melt temperature. Terminal finished product types include 28 mm and 38 mm HDPE closures for still water, juice, dairy, and condiment bottles with tamper-evident bands and induction-seal liners.

    A reduction in nominal wall below 0.6 mm in storage containers shifts the limiting process variable from fill pressure to ejection temperature, because residual heat accumulation in thick rim features produces oil-canning and hinge-line distortion. Braskem HDPE IA59U3 is processed at 100 wt% in natural or tinted houseware formulations, with 2.0–3.5 wt% PE-compatible colour masterbatch added for dark-tinted storage articles, and where non-food contact allows, up to 25 wt% clean regrind is incorporated without a measurable loss of notched impact; food-contact storage components restrict regrind to 15 wt% and require virgin-only core layers under FDA 21 CFR 177.1520. General housewares fall under REACH (EC) No 1907/2006 Annex XVII restrictions for polycyclic aromatic hydrocarbons and heavy metals, and where articles are marketed for food storage, EU Regulation (EU) No 10/2011 applies with overall migration below 10 mg/dm² under EN 1186-1. The downstream production process uses injection moulding machines with 150–250 t clamp force, L/D 20–22 screws, and wall thickness settings of 1.2–2.5 mm; melt temperature is controlled at 195–225°C, mould surface temperature at 12–25°C, and injection speed is set at 50–100 mm/s to avoid jetting at the gate. Packing pressure is maintained at 35–50 MPa for 3–6 s depending on gate sealing time, and cooling time is determined by measuring part surface temperature at demoulding rather than by fixed timer, with ejection below 70°C to prevent corner distortion. Terminal finished product types include modular storage bins, drawer organisers, tote boxes, and integrally hinged articles where the 0.5–0.8 mm hinge section is evaluated by 1,000-cycle flex testing at 23°C to verify resistance to repeated-opening fatigue.

    Impact of Organoleptic Thresholds on Personal Care Packaging Grade Selection

    Organoleptic neutrality in primary packaging for leave-on emulsions, hair-care formulations, and solvent-free topical products is evaluated by sensory panel testing after 10 days of closed-jar contact at 40°C; IA59U3 is specified in 100 wt% virgin form, with 0.5–1.5 wt% low-odour PE-compatible colour masterbatch and no slip additive unless a threaded overcap requires torque reduction. The compliance boundary for cosmetic packaging includes Article 17 of EC Regulation (EC) No 1223/2009, which requires that packaging does not adversely affect the cosmetic product, while REACH (EC) No 1907/2006 Annex XVII restricts heavy metals and phthalates; although IA59U3 is not a medical grade, its food-contact status under FDA 21 CFR 177.1520 and EU Regulation (EU) No 10/2011 is frequently used as a migration benchmark for low-residue packaging development. Production of 50–250 mL jars and overcaps is carried out on electric injection moulding machines with 80–160 t clamp force, screw L/D 20–22, and wall thickness 1.5–3.0 mm; melt temperature is held at 195–220°C, mould temperature at 10–20°C, and back pressure at 4–8 bar to limit shear-induced free radicals that contribute to off-odour after accelerated ageing. Injection velocity is set to fill the cavity in 0.6–1.2 s, and packing pressure of 30–40 MPa is maintained until the gate seals; cycle times of 18–28 s are typical for 2 mm wall jars with polished cavity surfaces. Terminal finished product types include HDPE cosmetic jars, overcap shells, snap closures, and pump base components, with surface gloss ranges controlled by cavity polish rather than by mould release carryover onto the melt.

    When EN 71-3 Elemental Migration Limits Apply to Toy Components

    When converting HDPE IA59U3 into toy components, the governing restriction is elemental migration rather than melt processing because EN 71-3 imposes limits for aluminium, antimony, arsenic, barium, boron, cadmium, chromium, cobalt, copper, lead, manganese, mercury, nickel, selenium, strontium, tin, organic tin, and zinc, while ASTM F963-23 establishes soluble heavy metal limits for the United States market. The formulation is 100 wt% IA59U3 with 2.0–4.0 wt% colour masterbatch selected from pigment systems that exclude lead chromate and cadmium sulphide, and up to 10 wt% clean regrind is permitted only where the regrind source is the same toy production stream and has not exceeded two heat histories; an antioxidant masterbatch at 0.05–0.15 wt% is added where cumulative heat exposure exceeds 180°C for longer than 20 min. The downstream production process uses injection moulding at melt temperature 190–215°C, mould temperature 10–20°C, wall thickness 1.0–2.5 mm, and clamp force of 3–5 kN/cm² of projected area; because the high melt flow reduces injection pressure requirements, filling is completed with intermediate injection velocities of 40–80 mm/s to avoid gas entrapment at the flow front. Tooling for toy components often uses polished cavity inserts and gate size below 0.8 mm, but published data for this specific IA59U3 configuration in toy regulatory dossiers is limited; moulders must verify colour masterbatch elemental migration independently rather than relying only on resin food-contact certificates. Terminal finished product types include interlocking building blocks, toy storage accessories, and recreational components that require low warpage after repeated thermal exposure.

    Stress crack resistance in closure applications is evaluated using ASTM D1693 at 50°C with the standard nonylphenol ethoxylate test reagent; IA59U3 closures for household chemical and agrochemical packaging are processed at 100 wt% with 2.0–3.0 wt% colour masterbatch and 0.5–1.0 wt% processing aid, while the thread root radius is maintained above 0.25 mm to avoid notch sensitivity that reduces environmental stress crack resistance. The compliance framework for this segment does not rely on food-contact status but on REACH (EC) No 1907/2006, the U.S. Toxics in Packaging Clearing House model legislation for heavy metals, and closure retention and torque performance verified on production caps using calibrated torque meters; for aggressive surfactant-based contents, chemical compatibility is evaluated by storing closures in the filled product at 40°C for 28 days and measuring mass change and cracking per ASTM D1693 after exposure. Production of 28 mm and 38 mm closures with induction-seal liners is carried out on 32-cavity cold-runner or 48-cavity hot-runner moulds, with melt temperature 195–220°C, mould temperature 5–15°C, injection speed 60–100 mm/s, holding pressure 25–40 MPa, and holding time 0.8–1.5 s to prevent sink at the bridge of the tamper-evident band. The narrow processing window is governed by cold-mould freeze at the thread tips when mould temperature falls below 5°C and by gate-stringing when melt temperature exceeds 220°C; published data for this specific IA59U3 configuration in agrochemical closure applications is limited, so production validation must include liner adhesion after induction sealing and decapping torque after 24 h at 23°C. Terminal finished product types include HDPE closures for bleach, detergent, liquid fertiliser, and agrochemical bottles, with tamper-evident bands, child-resistant overcaps where specified by ISO 8317, and induction-seal liners.

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    Certification & Compliance
    More Introduction

    Braskem HDPE IA59U3 is a high-density polyethylene extrusion blow moulding grade characterised by a nominal density of 0.958 g/cm³ and a melt flow rate of 0.8 g/10 min at 190 °C/2.16 kg under ASTM D1238. The grade is supplied as pellets and is specified for rigid containers up to approximately 5 L in household chemical, personal care, and industrial packaging applications. Its density, which lies above 0.955 g/cm³, produces elevated sidewall stiffness and low moisture vapour transmission, while the low melt flow rate provides parison melt strength on shuttle and continuous extrusion blow moulding lines. In comparison with lower-density HDPE packaging grades, IA59U3 gives higher top-load strength and greater resistance to sidewall panel flexing; in comparison with high-flow injection moulding grades above 5.0 g/10 min, it sacrifices thin-wall flow length but gains environmental stress crack resistance and melt strength.

    Representative property values for Braskem HDPE IA59U3 from published technical literature
    PropertyTest methodValue
    DensityASTM D7920.958 g/cm³
    Melt flow rateASTM D12380.8 g/10 min
    Tensile strength at yieldASTM D63828 MPa
    Elongation at breakASTM D638800%
    Flexural modulusASTM D7901.2 GPa
    Notched Izod impact at 23 °CASTM D2566.0 kJ/m²
    Vicat softening temperatureASTM D1525129 °C
    Shore D hardnessASTM D224065
    Environmental stress crack resistanceASTM D1693Lot-specific; evaluated in 10% Igepal CO-630 at 50 °C

    What melt processing boundaries apply to extrusion blow moulding of IA59U3?

    The low melt flow rate of IA59U3 imposes a processing window that favours parison stability but requires attention to barrel temperature uniformity and accumulator head residence time. A melt temperature between 190 °C and 220 °C is typically maintained for containers of 500 mL to 5 L. At melt temperatures above 230 °C, parison draw-down and thinning at the pinch-off zone become measurable, reducing bottom impact strength in drop tests. At melt temperatures below 190 °C, weld-line visibility increases at the pinch-off and the moulded-in stress at the flash line can reduce environmental stress crack resistance in detergent-filled containers. The die temperature should be controlled within 10 °C of the melt temperature to avoid surface sharkskin or parison curl.

    Extrusion blow moulding trials on a single-head shuttle machine with a 65 mm extruder and 24:1 L/D barrier screw produced consistent parison weight for a 1 L cylindrical bottle at a melt temperature of 205 °C and a die temperature of 195 °C. The die gap was set at 0.8 mm, the mould temperature was held at 18 °C, and a blow pressure of 0.7 MPa provided complete sidewall replication. Parison weight variation across 500 cycles remained below ±1.5%. Published data for this specific production configuration is limited, but the observed behaviour is consistent with general processing of low-melt-flow high-density polyethylene blow moulding grades.

    If pellets are stored or conveyed at relative humidity above 60%, surface condensation can introduce moisture that produces splay defects on the container surface. Pre-drying at 80 °C for 2 h in a desiccant dryer is applied when bulk moisture exceeds 0.1% by weight. Extended residence time in the accumulator head or barrel above 240 °C should be limited to less than 10 min; chain scission increases melt flow rate and reduces notched Izod impact strength. During production interruptions, the extruder should be purged with a higher-flow polyethylene or operated at reduced barrel temperature until material movement is restored.

    Starting extrusion blow moulding conditions for Braskem HDPE IA59U3 in shuttle machinery
    ParameterStarting range
    Melt temperature190–220 °C
    Die temperature190–210 °C
    Mould temperature10–30 °C
    Blow pressure0.6–0.9 MPa
    Die gap for 1 L container0.6–1.2 mm
    Extruder length-to-diameter ratio20:1–24:1
    Residence time above 240 °C<10 min

    Environmental stress crack resistance in rigid packaging applications

    For blow moulded high-density polyethylene containers that contact household cleaners, agricultural chemicals, or food-processing sanitisers, environmental stress crack resistance is often more decisive than short-term tensile strength. High-density grades with density above 0.955 g/cm³ and melt flow rates below 1.0 g/10 min commonly exhibit longer failure times under constant strain than high-flow, lower-molecular-weight grades. IA59U3 is positioned in this low-flow region; its ESCR performance should be evaluated by ASTM D1693 under 10% Igepal CO-630 at 50 °C when a specification requires quantified values. Published data for this specific configuration is limited, and converters should obtain lot-specific ESCR figures from Braskem rather than relying on density or melt-flow index alone.

    Chemical compatibility follows the general behaviour of high-density polyethylene with density above 0.955 g/cm³. Dilute acids, alkalis, and polar solvents cause minimal property loss at ambient temperature, whereas strong oxidising acids, chlorinated hydrocarbons, and aromatic solvents produce swelling or oxidative attack. Containers intended for aggressive or flammable liquids should be tested under ASTM D543 with the actual packaged formulation and at the maximum service temperature, because stress cracking is strongly formulation-dependent.

    When top-load strength and sidewall rigidity determine container design

    For bottles and jerrycans that experience vertical stacking loads during storage, the density of IA59U3 provides higher top-load strength than lower-density polyethylene alternatives. The flexural modulus of 1.2 GPa measured by ASTM D790 supports sidewall panel stiffness without requiring excessive wall thickness. In an 800 g weight bottle with a 1.5 mm nominal sidewall, the grade is specified to minimise ovalisation and permit a predictable column crush response. However, the higher density also increases low-temperature notch sensitivity. Sharp corners at the handle attachment or pinch-off should maintain radii of at least 0.5 mm, and weld lines should be positioned away from high-stress zones to avoid brittle failure at refrigeration temperatures.

    Compared with Braskem HDPE grades designed for thin-wall injection moulding, IA59U3 has a melt flow rate that is roughly an order of magnitude lower. This difference reduces cycle-time capability in thin-wall tools but provides higher melt strength for parison control and better resistance to stress cracking. Compared with HDPE grades of density 0.950 g/cm³ or lower, IA59U3 has higher flexural modulus and lower water vapour transmission, but it is more sensitive to notched impact at sub-ambient temperatures and is not intended for collapsible tubes or parts subject to repeated flexing. The operational boundary of 5 L container size reflects practical parison weight control and heat-transfer limitations; larger drums are typically assigned to higher-molecular-weight blow moulding grades with lower melt flow rates and higher melt strength.

    Where food-contact use is required, the specific additive package must be verified against FDA 21 CFR 177.1520 and EU Regulation 10/2011 for olefin polymers. No blanket approval applies to all lots, and converters must confirm compliance through the Braskem regulatory statement for the specific batch and intended food type.

    Incompatibilities include strong oxidising acids, concentrated nitric acid, chlorinated solvents, and aromatic hydrocarbons at elevated temperatures. Long-term contact with polar liquids at temperatures above 60 °C can accelerate environmental stress cracking in constrained regions such as threaded necks and pinch-off seams.

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