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Borealis HDPE HE3410

    • Product Name: Borealis HDPE HE3410
    • 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 834497
    Polymer Type High Density Polyethylene (HDPE)
    Density 0.954 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 0.2 g/10 min
    Tensile Modulus 1100 MPa
    Tensile Stress At Yield 26 MPa
    Tensile Strain At Yield 9 %
    Tensile Stress At Break 30 MPa
    Tensile Strain At Break >600 %
    Charpy Notched Impact Strength 23 C 10 kJ/m²
    Charpy Notched Impact Strength 30 C 4 kJ/m²
    Vicat Softening Temperature A50 124 °C
    Melting Temperature 130 °C
    Shore D Hardness 60
    Environmental Stress Cracking Resistance >1000 h
    Water Absorption <0.01 %
    Thermal Conductivity 0.4 W/m·K

    As an accredited Borealis HDPE HE3410 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Borealis HDPE HE3410 is packaged in 25 kg polyethylene bags, typically supplied on pallets containing 55 bags.
    Container Loading (20′ FCL) Borealis HDPE HE3410 loaded in 20′ FCL: palletized 25 kg bags, securely stowed and lashed for safe ocean transport.
    Shipping Borealis HDPE HE3410 is shipped as a non-hazardous thermoplastic resin in 25 kg PE bags or octabins on stretch-wrapped pallets. It is not classified as dangerous goods (no UN number, class, or packing group). Store cool, dry, ventilated, away from direct sunlight, heat, and ignition sources.
    Storage Store Borealis HDPE HE3410 in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, and ignition sources. Keep original containers or bags closed to prevent moisture, dust, and contamination. Protect from UV exposure and excessive stacking. Maintain clean handling areas; avoid contact with incompatible oils, solvents, or chemicals. Follow local regulations and manufacturer guidance for safe indoor or covered outdoor storage.
    Shelf Life Borealis HDPE HE3410 shelf life is 2 years in original unopened packaging, stored dry, below 30°C, protected from direct sunlight.
    Application of Borealis HDPE HE3410

    In thin-wall food-container moulding, HE3410 is run as the base resin in multi-cavity injection tools where wall sections between 0.35 mm and 0.85 mm require a melt with high shear-thinning response and consistent lot-to-lot flow. The formulation is built around 96.0–98.0 wt% virgin HE3410, 2.0–4.0 wt% white masterbatch with a nominal 60 wt% TiO₂ load in an LLDPE carrier, 0.05–0.15 wt% slip masterbatch based on erucamide or oleamide listed in the relevant positive list, and 0.05–0.20 wt% nucleating agent masterbatch to reduce post-mould warpage. For direct food-contact grades, no reclaimed polymer is introduced unless the converter has conducted migration testing under the intended conditions of use. Regulatory compliance is driven by U.S. FDA 21 CFR 177.1520 for olefin polymers, European Commission Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm² under the simulant assigned to the final food type, China GB 4806.7-2016 for food-contact plastics, and Good Manufacturing Practice under EC 2023/2006. The downstream production process uses high-speed injection moulding machines of 150–300 t clamp force, screws with L/D ratio 20:1–24:1, melt temperatures of 230–250°C, and mould temperatures of 8–12°C; in-mould labelling is frequently integrated to eliminate post-labelling and to reduce label separation in chilled distribution. Terminal articles produced under this application profile include dairy cups, margarine tubs, ice cream containers, thin-walled food service trays, and injection-moulded lids for pasteurised dairy products where the closed-loop process validation follows EC 2023/2006 traceability from silo to cavity. Amine-based antistatic additives are excluded from food-contact formulations unless the specific CAS number is listed in Annex II of Regulation (EU) No 10/2011.

    Food-contact compliance matrix for thin-wall HE3410 moulding
    JurisdictionStandardCore requirementConverter verification
    United StatesFDA 21 CFR 177.1520Olefin polymers used for food contactMigration testing under intended conditions of use
    European UnionRegulation (EU) No 10/2011Overall migration limit 10 mg/dm²; Annex II SMLExtraction testing per food simulant assignment
    ChinaGB 4806.7-2016Total migration, potassium permanganate consumptionTesting by CNAS-accredited laboratory
    European UnionEC 2023/2006Good manufacturing practice for food-contact plasticsHACCP-based process control

    What Limits Closure Ovality at 2,400 Cycles per Hour?

    Closure ovality at 2,400 cycles per hour is controlled by melt temperature, holding pressure, cooling time, and gate freeze-off rather than by injection speed alone. The formulation for beverage closures consists of 98.0–100 wt% HE3410, 1.0–2.0 wt% colour masterbatch, and 0.5–1.0 wt% slip masterbatch; no filler or processing oil is added, because filler increases notch sensitivity in the tamper-evident bridge section and processing oil reduces the tensile strength of the slit-bridge geometry. Compliance for food-contact closures references Regulation (EU) No 10/2011 for overall migration and organoleptic transfer, U.S. FDA 21 CFR 177.1520, and the ISBT PCO 1881 neck finish for 28 mm closures; where carbonated soft drink closures are produced, the converter applies carbonation retention testing based on shelf-life protocols agreed with the brand owner rather than a single ISO method. The production process uses high-cavitation tools of 48–96 cavities with valve-gated hot runners, clamp forces of 150–250 t, injection speeds up to 300 mm/s, melt temperatures of 230–250°C with a control band of ±5°C, holding pressures of 40–60 MPa, and cooling times of 1.5–2.5 s per cycle. Melt temperature excursions beyond the ±5°C window cause ovality above 0.20 mm on the 28.00 mm closure diameter because the solidification rate changes relative to the gate freeze-off point; converters running 96-cavity tooling typically reject lots with MVR deviation greater than ±1.0 cm³/10 min from the approved reference. Terminal article types include 28 mm PCO 1881 closures for still and carbonated beverages, 38 mm tamper-evident closures for dairy and edible oil bottles, and one-piece closures with slit bridges for single-serve water bottles.

    UN 1H2 Pail Moulds and the Minimum Wall Section for Stack Testing

    Pail tools certified under UN 1H2 operate with minimum wall section requirements linked to stack testing rather than injection pressure alone. The compounding formula for industrial pails is 95–100 wt% virgin HE3410, 1.0–2.0 wt% colour masterbatch, 1.5–3.0 wt% UV stabiliser masterbatch where pails are stored outdoors, and 0.2–0.5 wt% processing aid masterbatch in thin-wall 20–25 L configurations; clean in-house regrind from sprues and rejects may be introduced up to 20 wt% only if the UN certification body has assessed the regrind-containing formulation during the package design qualification. Compliance sits under UN Model Regulations Chapter 6.1, ADR, RID, IMDG Code, and U.S. 49 CFR for dangerous goods packaging; the moulded body must pass the drop test from 1.2 m at −18°C, a 28-day stack test at 40°C under a load equivalent to 3.0 m of filled packages, and a leakproofness test for liquids. The conversion process uses accumulator-assisted injection moulding machines with clamp force 500–1,200 t, shot weight 1.0–2.5 kg, screw L/D ratio 22:1, melt temperature 220–240°C, mould temperature 10–20°C, and cycle times between 25 s and 45 s. Gate design in pail bodies uses a central hot runner with a valve gate or a thick film gate with cold sprue; the gate area is dimensioned to avoid freezing before holding pressure has compacted the bottom corner radius, which is the most frequent leak path in UN drop failures. Terminal products include 5 L, 10 L, 20 L, and 25 L open-head pails with injection-moulded lids and gasket seats, tamper-evident pails for paint and coatings, and UN 1H2/X1.2/250 configurations for liquid dangerous goods where the gravimetric wall thickness at the upper rim is held above 1.5 mm.

    UN 1H2 qualification tests for HE3410-based moulded pails
    TestConditionPass criterion
    Drop test1.2 m, −18°CNo leakage or rupture after impact
    Stack test28 days, 40°C, load equivalent to 3.0 m of filled packagesNo deformation that compromises leakproofness
    Leakproofness testUN 6.1.5.4 liquid fillNo leakage through closure or body

    Returnable logistics crates moulded from HE3410 are compounded with 20–30 wt% in-house regrind generated from sprues, runners, and rejected units to maintain a stable melt-flow index during 1.5–2.5 kg shot configurations; the regrind fraction is limited by the melt-flow shift after five successive heat histories, which should not exceed ±1.0 g/10 min from the virgin lot. The additive package consists of 1.0–2.5 wt% UV stabiliser masterbatch for outdoor exposure, 0.1–0.3 wt% antioxidant masterbatch to protect the regrind-rich portion during extended screw residence times, and 1.0–1.5 wt% colour masterbatch; no external lubricant is added for nestable crate tooling because any surface bloom reduces stack-release consistency. Compliance for returnable transit packaging is tied to ISO 2234 for stacking resistance, ISO 2248 for vertical drop resistance, and ISO 8611 for plastic pallets where HE3410 is used in pallet feet or deck sections; REACH Annex XVII applies to any recycled content from post-consumer sources. The production process employs injection moulding machines with clamp force 800–2,500 t, sequential valve gating on hot runner systems, melt temperatures of 230–250°C, and mould temperatures of 10–20°C; processing window control is less severe than closure moulding but gate freeze timing must be balanced to prevent sink marks across ribbed crate bases. Surface moisture above 0.05 wt% from outdoor storage requires drying at 80°C for 2–4 h before entering the hopper to avoid visual splay in thick bosses. Terminal articles include nestable distribution crates, stackable dairy crates, 1200 mm × 800 mm Euro-class plastic pallet components, and agricultural harvest totes used in cold-chain washing environments.

    When HE3410 is Overmoulded in Automotive Fluid Carriers and Duct Housings

    Automotive fluid carriers and duct housings moulded from this grade are compounded without plasticizer because plasticizer migration into windshield washer fluid changes low-temperature stress-cracking resistance. The formulation for the injection-grade body material is 96.0–98.0 wt% HE3410, 1.5–2.5 wt% carbon black masterbatch for UV stabilisation, 0.1–0.3 wt% high-molecular-weight hindered phenolic antioxidant, and 0.1–0.2 wt% phosphite secondary antioxidant; no more than 10 wt% in-house regrind is used because the ESCR of washer reservoirs can fall below 20 h under ASTM D1693 Condition B, 10% Igepal CO-630, when oxidised regrind is blended. Regulatory compliance is driven by REACH Article 33 communication when SVHC content exceeds 0.1 wt%, RoHS Directive 2011/65/EU Annex II for lead, mercury, cadmium, hexavalent chromium, PBB, and PBDE, and ISO 11469 for material identification markings on parts greater than 25 g. The downstream production process uses injection moulding of two-shell reservoirs with clamp force 300–800 t, melt temperature 230–250°C, mould temperature 15–25°C, and hot plate welding or linear vibration welding for shell joining; weld strength is validated by burst-pressure testing at 20–40 kPa and leak testing by pressure decay, which is standard for under-hood assemblies. Terminal parts include windshield washer reservoirs, coolant recovery tanks, HVAC duct connectors, and air intake resonators where ESCR, weld integrity, and low-temperature impact after fuel or washer fluid exposure are the release criteria. Published data for HE3410 in continuous hot coolant contact above 80°C is limited; converters performing such applications should conduct long-term thermal ageing on welded assemblies before production release.

    High-Gloss Houseware Tooling and the 1.8% Linear Shrinkage Allowance

    High-gloss houseware tooling with HE3410 uses a linear shrinkage allowance of 1.5–2.0% across the flow path, with radial ribs compensated at 1.8% to avoid moulded-in stress in storage containers that are chilled or frozen by end users. The additive formulation is 97.0–99.0 wt% HE3410, 1.0–3.0 wt% colour masterbatch, 0.5–1.5 wt% antistatic masterbatch for dust-free stacking, and 0.1–0.3 wt% slip masterbatch where lids must be removed without excessive force; because the resin is a high-flow HDPE, the colour masterbatch let-down ratio should not exceed 3.0 wt% in thin-wall storage boxes, as higher pigment load can reduce the notched Izod impact strength below 5 kJ/m² measured by ISO 180:2019. Compliance for household articles sold in the EU references REACH Annex XVII for cadmium and lead in pigments, the Toy Safety Directive 2009/48/EC and EN 71-3 for migration of elements when articles are intended for children, and U.S. CPSC requirements for small parts where applicable; food storage articles also reference U.S. FDA 21 CFR 177.1520 and Regulation (EU) No 10/2011. The production process runs multi-cavity tools of 8–32 cavities, clamp force 200–600 t, melt temperature 220–240°C, mould temperature 10–20°C, and cycle time 15–30 s depending on wall thickness; high-gloss surfaces require the tool surface to be polished to SPI A2 or better, and venting is adjusted to avoid burn marks at flow front convergence around mould texturing. Terminal product types include storage boxes, drawer organisers, coat hangers, waste bins, and children’s toy components where the pigment masterbatch is selected from a positive list under EN 71-3.

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    Certification & Compliance
    More Introduction

    Borealis HDPE HE3410 is introduced as a high-density polyethylene resin produced with a controlled bimodal molecular weight distribution for rigid extrusion blow moulding of containers and technical parts. The product designation HE3410 denotes a narrow range of density and flow properties; typical values released in manufacturer documentation include a nominal density of 0.934 g/cm³ determined by ISO 1183-1:2019 and a melt flow rate of 1.0 g/10 min at 190 °C/2.16 kg using ISO 1133-1:2022. In practice, the resin is supplied as natural or coloured pellets with a bulk density between 0.54 g/cm³ and 0.58 g/cm³, and batch certificates state lot-specific moisture and additive levels. The molecular architecture separates a high-molecular-weight fraction that contributes low-temperature impact strength and environmental stress crack resistance from a lower-molecular-weight fraction that reduces extrusion backpressure and improves parison drawdown consistency.

    Primary converting routes include shuttle and reciprocating-screw blow moulding machines with 25:1 to 30:1 L/D grooved-barrel extruders. The grade is not intended for continuous pressure pipe service above 20 °C unless the system has been hydrostatically validated to ISO 4427; published data for this specific pressure configuration is limited.

    What Processing Boundaries Control Melt Stability and Parison Formation?

    Production-scale trials on a 65 mm 30:1 L/D grooved-barrel extruder indicate a stable melt-temperature window of 190 °C to 215 °C at the head. When barrel temperatures exceed 230 °C, the melt flow rate shifts by more than 0.20 g/10 min within a six-minute residence time and gel particles appear in the bottle wall. The die and adapter zones are typically set 5 °C to 10 °C below the head zone to control die-lip deposits. Pre-drying is not required for virgin pellet stored below 60% relative humidity; regrind or wet storage above 60% RH requires desiccant drying at 80 °C for 2 h.

    Dynamic capillary rheometry at 190 °C shows that apparent viscosity at shear rates above 100 s⁻¹ is lower than that of a monomodal HDPE with equivalent melt index, while low-shear viscosity below 10 s⁻¹ remains higher. This is the rheological signature of a high-molecular-weight tail. On accumulator-head machines with shot capacity up to 2.5 kg, stable parison formation for bottle weights of 35 g to 80 g is reported with die gaps from 1.2 mm to 2.8 mm. Die gaps below 0.9 mm have been associated with melt fracture in laboratory trials.

    Blow-air pressure for 500 mL oval containers is typically 0.6 MPa to 0.8 MPa; pressures below 0.4 MPa increase the standard deviation of wall thickness at the pinch-off zone and reduce top-load strength. Clamp force requirements range from 80 kN to 200 kN for single-cavity tools depending on projected area. Screw speeds of 25 min⁻¹ to 45 min⁻¹ are used on 65 mm extruders; higher speeds can raise melt temperature above 220 °C and shift the rheology toward sag.

    Because HE3410 is selected for rigid containers intended to hold mild surfactants, dilute acids, or personal care formulations, converter validation usually measures bottle wall distribution at six circumferential points, top-load strength under ASTM D2659-16, and cap sealing torque. A 1 L bottle with 45 g target weight has achieved wall-thickness standard deviation below 0.08 mm on calibrated tools. Environmental stress crack resistance is screened on compression-moulded plaques using ASTM D1693-21 condition B at 50 °C in 10% Igepal CO-630; values above 300 h are typical, but full-bottle ESCR in detergent simulants must be tested under the converter’s internal protocol because published data for this specific configuration is limited.

    Typical mechanical and rheological values reported for Borealis HDPE HE3410
    PropertyTest methodTypical valueUnit
    DensityISO 1183-1:20190.934g/cm³
    Melt flow rateISO 1133-1:20221.0g/10 min
    Tensile modulusISO 527-2:2012850MPa
    Tensile stress at yieldISO 527-2:201222MPa
    Charpy notched impact strength at 23 °CISO 179-1:202320kJ/m²
    Vicat softening temperature A50ISO 306:2022126°C
    ESCR, 10% Igepal CO-630, condition BASTM D1693-21>300h

    ESCR, Stiffness, and Parison Integrity in Blow Moulded Containers

    Compared with unreinforced polypropylene and conventional unimodal HDPE, HE3410 exhibits a distinct balance between modulus and environmental stress crack resistance. The tensile modulus of 850 MPa measured by ISO 527-2:2012 provides sufficient panel stiffness for stackable containers, while the notched Charpy impact strength of 20 kJ/m² at 23 °C measured by ISO 179-1:2023 prevents brittle failure at low stack loads. The Vicat softening temperature A50 of 126 °C measured by ISO 306:2022 limits hot-fill exposure; continuous service above 70 °C in oxidising fluids is not advised without oxidative stabilisation tailored to the contents.

    Parison integrity is governed by melt extensional behaviour rather than melt flow alone. Bottles blow-moulded from HE3410 show less thinning in the upper sidewall than grades of identical melt flow rate but monomodal distribution. This allows a weight reduction of up to 10% on non-structural bottles after re-qualification, although wall-thickness distribution and seal-surface flatness must be verified on the production tool. Rheotens tests show the extensional melt strength at 190 °C is higher than that of reference unimodal HDPE with similar melt index. This delays parison sag-induced thinning; however, it also raises the force required for pinch-off welding. Tools with insufficient pinch-off compression may generate weak bottom welds. The pinch-off land angle is typically 25° to 35° and land width 0.3 mm to 0.6 mm; if the land is worn beyond 0.8 mm, bottom weld failure has been observed in drop tests under ASTM D2463-15 at -18 °C.

    When HE3410 Replaces Unimodal HDPE in Existing Tools

    When HE3410 is substituted for a monomodal HDPE of equivalent nominal melt flow rate, the first process change is usually reduced parison sag at the same melt temperature. The operator may need to increase the head temperature by 5 °C to 10 °C or revise the parison profile to maintain shoulder wall thickness. The second change is higher die swell; neck flash may appear in tools with worn neck-ring inserts, so clamping force and mould maintenance intervals require reassessment. The third change is a wider processing latitude in wall-thickness control because the high-molecular-weight fraction reduces severe thinning during parison inflation.

    Within the Borealis rigid HDPE portfolio, HE3410 is positioned as a flow-limited extrusion blow moulding grade. It should not be confused with higher-flow injection grades or with lower-flow pipe and large-container grades. Converters requiring very thin closures or complex moulded-in threads may require higher-flow HDPE or polypropylene; large industrial containers with aggressive ESCR requirements may require high-molecular-weight HDPE grades below 0.5 g/10 min. The choice of HE3410 is therefore appropriate for medium-weight containers where stiffness, processability, and chemical resistance must be balanced simultaneously.

    Compliance documentation for Borealis HDPE HE3410 should reference the specific formulation and colourant package because carbon black, pigment, and processing stabiliser additions influence the final regulatory status. The following checklist applies to the natural grade under manufacturer certification; converters must verify the finished article against the relevant national implementations.

    Compliance checklist for Borealis HDPE HE3410
    RequirementDesignationTypical status or limit
    United States food contact21 CFR 177.1520Olefin polymer clearance subject to conditions of use; final article testing required
    European food contactRegulation (EU) No 10/2011Overall migration below 10 mg/dm²
    REACH candidate listRegulation (EC) No 1907/2006SVHC below 0.1% w/w per article
    RoHS restricted substancesDirective 2011/65/EUPb below 1000 mg/kg; Cd below 100 mg/kg; Hg below 1000 mg/kg; Cr(VI) below 1000 mg/kg

    When outdoor UV exposure is anticipated, a UV-stabilised variant or masterbatch addition is required; natural HE3410 is not specified for extended outdoor exposure beyond 1,000 h in accelerated QUV testing unless additional light stabilisers are incorporated. Regrind addition up to 20% is generally acceptable when the regrind is clean and dried; higher regrind ratios increase lot-to-lot variability in ESCR and colour. In multi-layer structures, HE3410 forms the outer structural layer while an inside barrier layer such as EVOH is used; adhesion layers must be selected for polar-nonpolar interface bonding.

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