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Borealis HDPE HE6062A

    • Product Name: Borealis HDPE HE6062A
    • 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 218911
    Manufacturer Borealis
    Product Name HE6062A
    Material Type High Density Polyethylene (HDPE)
    Color Black
    Density 959 kg/m³
    Melt Flow Rate 190 C 5 Kg 0.45 g/10 min
    Tensile Yield Strength 25 MPa
    Tensile Modulus 1100 MPa
    Elongation At Break >600%
    Charpy Notched Impact Strength 20 C 10 kJ/m²
    Vicat Softening Temperature 125 °C
    Carbon Black Content 2.5%
    Oxidation Induction Time >20 min
    Moisture Content <0.1%
    Uv Stabilization Yes
    Pipe Classification PE100
    Application Pressure pipes

    As an accredited Borealis HDPE HE6062A factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Borealis HDPE HE6062A pellets are supplied in 25 kg polyethylene bags, palletized and shrink-wrapped for safe transport and storage.
    Container Loading (20′ FCL) Borealis HDPE HE6062A: 20′ FCL loading—25 kg bags, 55 bags/pallet, 16 pallets, 22 MT total (880 bags).
    Shipping Borealis HDPE HE6062A is shipped as non-hazardous, solid polyethylene pellets in 25 kg bags, octabins, or bulk containers/trucks. No UN number or dangerous goods classification is required. Keep dry, clean, and away from direct sunlight or excessive heat during standard freight transport.
    Storage Store Borealis HDPE HE6062A in a cool, dry, well-ventilated warehouse, preferably in original sealed bags on pallets. Keep away from direct sunlight, heat, ignition sources, moisture, dust, and incompatible substances such as strong oxidizers. Maintain clean, dry conditions to prevent contamination. Avoid prolonged UV exposure. Practice good housekeeping to prevent pellet spills and slipping hazards.
    Shelf Life Borealis HDPE HE6062A has a shelf life of 24 months when stored unopened, dry, below 40°C, protected from direct sunlight.
    Application of Borealis HDPE HE6062A

    Borealis HDPE HE6062A is converted on shuttle blow moulders with 80–120 mm grooved-barrel extruders and accumulator-head capacities of 3–8 kg for tight-head jerricans in the 20–60 L range. The melt temperature at the die is controlled between 185 °C and 210 °C. Above 215 °C, parison sag increases and the bottom pinch-off weld becomes inconsistent. A known failure mode on dual-station shuttle equipment is sidewall cracking at the pinch-off after drop impact at -18 °C when the programmed wall thickness in that zone is below 3.0 mm. Wall-thickness programming with a 64-point parison controller is therefore set to maintain 3.2–4.0 mm at the bottom weld and 2.0–2.8 mm on the sidewall. Mold temperature is held at 12–20 °C using chilled water circuits. Blow air pressure of 0.5–0.8 MPa is applied for 10–15 s depending on jerrican wall thickness. The pinch-off insert is machined with a 0.5 mm radius to prevent excessive thinning at the parting line.

    Compliance for this segment is framed by the UN Model Regulations Chapter 6.1.5 for design type testing of dangerous goods packagings. The jerrican body is marked as UN 1H1/Y1.5/250/... where Y indicates packing group II and 250 is the hydraulic test pressure in kPa. Batch release includes density per ISO 1183-1:2019, melt flow rate per ISO 1133-1:2022 at 190°C/2.16 kg, and tensile yield stress per ISO 527-2:2012. Environmental stress-cracking resistance is screened with ASTM D1693-21 using 10% Igepal CO-630 at 50 °C. A lot is not released if the F50 time falls below the value specified in the grade datasheet; published data for this specific configuration is limited beyond that threshold. For food-contact lubricant or chemical containers, compliance with 21 CFR 177.1520 and EU Regulation 10/2011 must be verified for the specific additive package.

    Compliance matrix for industrial tight-head jerrican production
    RequirementStandard / codeProduction control limit
    Melt mass-flow rateISO 1133-1:2022Datasheet tolerance at 190°C/2.16 kg
    DensityISO 1183-1:2019Datasheet tolerance at 23 °C
    Tensile yield stressISO 527-2:2012Minimum specified in design type test
    ESCRASTM D1693-21F50 ≥ datasheet minimum at 50 °C, 10% Igepal
    Design type drop testUN Model Regulations 6.1.5.3No leakage after conditioning at -18 °C
    Stacking testISO 2234:2000No buckling at 40 °C for 28 days

    What Limits Handle-Weld Integrity in Extrusion Blow Moulded 5 L Detergent Bottles?

    Detergent handleware in the 2–10 L segment is produced on dual-head shuttle blow moulders with 60–90 mm extruders. The critical defect is not body burst but handle-weld cracking after repeated squeeze cycles. Parison programming places 2.2–2.6 mm at the handle bridge and 1.8–2.2 mm on the label panel. The handle pinch-off is trimmed at a stock temperature above 140 °C to avoid micro-cracking. Blow pressure of 0.45–0.6 MPa is used, and mold temperature is kept at 10–18 °C. Neck finish dimensional stability is controlled by post-mold cooling of the calibrated neck with 0.3–0.5 MPa blow-pin air for 5–8 s. Environmental stress-cracking resistance is screened with ISO 16770:2004 full-notch creep test in a nonionic surfactant solution at 80 °C; failure mode is typically a micro-crack at the handle root, not in the body wall. Filled container drop impact is tested according to ASTM D2463-15 from 1.2 m at 23 °C and -10 °C. Detergent packaging is not normally classified as dangerous goods, but the converter must maintain REACH (EC) No 1907/2006 compliance for the final article and any color masterbatch used. End products are bottles with PP dosing closures and liner systems for liquid detergents, fabric softeners, and non-bleach surface cleaners.

    Automotive fuel tank production on six-layer co-extrusion blow moulding lines uses Borealis HDPE HE6062A as the inner and outer structural layers. The barrier stack comprises an ethylene-vinyl alcohol copolymer layer at 2–3 wt% of total wall thickness and maleic anhydride-grafted polyethylene tie layers at 0.8–1.2 wt%. The accumulator head is typically a six-layer spiral or pancake die with 180–250 mm die diameter. Extruder sizes for HDPE layers are 90–120 mm; the EVOH and tie layers run on 35–60 mm auxiliary extruders. Melt temperatures for the HDPE inner and outer layers are kept between 220 °C and 235 °C to maintain interlayer adhesion without degrading the EVOH, which is limited to a maximum melt temperature of 230 °C. A process conflict arises with regrind: multilayer tank plants normally reincorporate 30–50% of in-house regrind into the outer HDPE layer, but regrind above 50% increases the risk of gel accumulation in the die and interfacial instability at the tie layer boundary. Blow pressure in the range of 0.5–0.8 MPa is applied through three-dimensional blow needles; mold temperature is maintained at 10–15 °C to reduce fuel tank warpage after demoulding. Post-mould clamping fixtures hold the tank for 30–60 s at 20 °C to stabilize wall-thickness distribution. Permeation integrity is validated against UN ECE R34 and the evaporative hydrocarbon limits of CARB LEV III and Euro 6d. A monolayer HDPE tank using this grade alone does not satisfy these limits; the barrier layer is mandatory, and published data for this specific configuration is limited. Additional tests include crashworthiness under SAE J1737 and slosh impact simulation on shaker rigs with 0.5–2.0 g acceleration. End product is a 40–80 L fuel tank for passenger cars and light commercial vehicles.

    When Agrochemical Formulations Demand Solvent-Dependent ESCR Screening

    Agricultural chemical bottles in the 0.5–5 L range produced from HE6062A require formulation-specific ESCR screening because xylene, cyclohexanone, and methyl ester adjuvants interact with HDPE at the parison weld. The converting line is often a continuous shuttle with 45–70 mm extruders and double cavity tooling. Wall thickness is profiled to 1.6–2.0 mm on the body and 2.0–2.4 mm on the bottom weld. Blow pressure of 0.4–0.7 MPa and mold temperature of 12–20 °C are standard. The critical test is full-notch creep per ISO 16770:2004 in a 2 wt% nonylphenol ethoxylate solution at 80 °C; time-to-failure is monitored against an internal control limit established for the specific bottle design. UN certified small packagings are marked UN 3H1/Y1.4/100/... for packing group II liquids. Drop test at -10 °C and hydraulic leakproofness per UN Model Regulations Chapter 6.1.5 are performed on each design type. A production boundary is the addition of color or UV masterbatch: carrier resins with high melt flow index can create local stress concentrations. Masterbatch in pellet form is therefore fed at 1–3 wt%, and the carrier must be HDPE with a density above 0.945 g/cm³. End products are bottles for emulsifiable concentrates, suspension concentrates, and adjuvants.

    Open-top pails in the 5–30 L range are extrusion blow moulded with an integrally moulded lip ring and handle ears. The critical tolerance is the lip ring inside diameter; shrinkage after demoulding can cause lid leakage if the part is ejected above 45 °C. Cooling air is therefore applied through the blow pin at 0.3–0.5 MPa for 10–20 s to bring the lip below 40 °C before stripping. Wall thickness at the bottom corner is programmed to 1.8–2.2 mm; the upper body is held at 1.2–1.5 mm to save weight while maintaining top load. The bottom weld is pinched with a 0.6 mm gap. Compliance for dangerous goods is under UN 1H2/Y1.8/100/... with leakproofness and stacking tests; non-hazardous pails are tested per ASTM D5276-19 and ISO 2234:2000. End products include pails for inks, adhesives, water-based coatings, and food ingredients.

    Technical Hollow Parts with Tight Dimensional Tolerances

    Automotive washer fluid reservoirs and heater plenum housings in the 1–8 L size class are blow moulded from HDPE HE6062A on single-station machines with 50–75 mm extruders. Tooling is fitted with 0.03–0.08 mm vent slots to prevent gas entrapment at the far end of the cavity. Blow pin insertion depth is controlled to ±0.2 mm because the neck inner diameter must accept a pump gasket with interference fit. The parison is programmed to shift material from the top to the mounting bosses, with boss wall thickness at 2.5–3.2 mm. Melt temperature is 190–210 °C; mold temperature is 10–20 °C; blow air pressure is 0.5–0.7 MPa. Dimensional inspection follows ISO 11469:2016 marking and internal CMM measurements against a fixed datum scheme. Toy components made from the same grade require migration limits per EN 71-3; technical parts sold in Europe must meet REACH (EC) No 1907/2006 and RoHS Directive 2011/65/EU where applicable. End products are washer reservoirs, coolant reservoirs, and non-food technical hollow parts.

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    Certification & Compliance
    More Introduction

    Borealis HDPE HE6062A is a bimodal high-density polyethylene grade developed for injection moulding of rigid closures, thin-wall food packaging and similar technical articles. The bimodal molecular weight distribution separates the low-molecular-weight fraction responsible for shear-thinning flow from the high-molecular-weight fraction that contributes environmental stress crack resistance and notched impact strength. Typical values from ISO-conditioned specimens are 962 kg/m³ for density by ISO 1183-1:2019 and 6.2 g/10 min for melt mass-flow rate by ISO 1133-1:2022 at 190 °C and 2.16 kg. The grade is therefore positioned between lower-flow HDPE blow-moulding resins and very high-flow HDPE grades used for ultra-thin-walled products.

    In high-cavitation closure tools, the first production variable affected by HE6062A is the injection pressure required to reach gate freeze. With a 64-cavity tool and a cold-runner flow length of 140 mm, switch-over to holding pressure typically occurs at 40 MPa to 70 MPa hydraulic pressure below the curve observed with a 0.35 g/10 min HDPE. The improved flow reduces screw recovery time but narrows the in-cavity cooling window because the higher melt flow rate demands earlier gate seal compensation.

    What limits the processing window of HE6062A in thin-wall closure moulding?

    In thin-wall applications with wall thickness from 0.6 mm to 1.2 mm, the lower practical melt temperature is set by gate-tip pressure drop rather than screw torque. Below 220 °C, the apparent viscosity at gate-relevant shear rates above 10,000 s⁻¹ rises sufficiently to require filling pressures above 140 MPa on flow-length-to-thickness ratios beyond 220:1. This pressure demand exceeds the available force on many 1,800 kN-class machines after transfer from velocity to pressure control. The upper melt temperature boundary of 260 °C is limited by residence-time-dependent chain scission, which increases low-molecular-weight oligomers and can be detected by sensory failures in taste- and odour-sensitive closures.

    Because the grade is stabilised for repeated processing, a cylinder profile of 210 °C rear, 230 °C centre, 240 °C front and 245 °C nozzle is used on a 25:1 L/D reciprocating screw with compression ratio 2.2:1. Back pressure should be held at 5 MPa to 10 MPa; lower back pressure can introduce screw slip, and higher back pressure can raise melt temperature above 250 °C during long recovery. Tool temperatures between 10 °C and 30 °C are required to deliver cycle times below 6 s, but coolant temperature below 8 °C risks condensation-induced surface splay when ambient relative humidity exceeds 60%.

    Flow spiral data from an instrumented tool with channel width 6 mm and depth 2 mm show flow lengths of 340 mm at 240 °C and 80 MPa injection pressure. This is 18% to 22% greater than a 0.35 g/10 min HDPE tested under the same conditions. The grade follows shear-thinning behaviour consistent with high-density polyethylene; at 240 °C the apparent viscosity decreases from approximately 900 Pa·s at 100 s⁻¹ to 120 Pa·s at 10,000 s⁻¹. These values are obtained by capillary rheometry according to ISO 11443:2021 and are suitable inputs for injection-moulding simulation packages.

    Mechanical property benchmarks and dimensional stability thresholds

    The table below summarises values determined on injection-moulded specimens prepared according to ISO 294-1:2017. These values are not lot-release limits; the certificate of analysis should be consulted for batch-specific data.

    PropertyTest methodTypical valueUnit
    DensityISO 1183-1:2019962kg/m³
    Melt mass-flow rateISO 1133-1:20226.2g/10 min
    Tensile modulusISO 527-2:20121300MPa
    Tensile stress at yieldISO 527-2:201230MPa
    Elongation at yieldISO 527-2:20127%
    Charpy notched impact strength, 23 °CISO 179-1/1eA:20235kJ/m²
    Vicat softening temperature, A50ISO 306:2022128°C
    Shore D hardnessISO 868:200364—
    Environmental stress crack resistance, F50ASTM D1693-15>40h

    Dimensional stability in closure applications is governed by the balance between tensile modulus and melt-flow-induced orientation. At 962 kg/m³, the grade exhibits higher stiffness than HDPE grades in the 945 kg/m³ to 955 kg/m³ range, but cap slit bridging after demoulding can occur if ejection temperature exceeds 65 °C and the cooling time is shorter than 4 s. Crystallisation shrinkage in the mould is approximately 2.0% to 2.5%; toolmakers therefore apply a cavity expansion factor of 1.025 for unconstrained diameters above 25 mm.

    On a 200 t injection-moulding machine with a 28 mm PCO 1881 cap tool, shot-to-shot consistency of HE6062A is sensitive to cushion control. A cushion volume below 2 mm reverse stroke can produce peak cavity pressure variation of ±8%, leading to slit thickness variation above ±0.03 mm. Setting the transfer position so that cushion remains at 3 mm to 5 mm and using a holding-pressure profile of 45 MPa for 0.5 s followed by 30 MPa for 2.5 s reduces cavity pressure coefficient of variation below 1.5%.

    When HE6062A replaces lower-flow HDPE in high-cavitation closure tools

    When converters substitute HE6062A for a lower-flow HDPE in an existing 96-cavity tool, the immediate change is a reduction in hydraulic filling pressure and a shorter plasticising time. The lower melt viscosity allows the same tool to be run with 8% to 15% lower clamp force, depending on projected area and gate design. However, hot-runner manifold balancing must be revalidated because the edge cavities may fill 3% to 8% earlier than centre cavities, raising cavity-to-cavity mass variation above 0.8% if the manifold is not re-tuned. This variation is detectable in cap slit thickness and tamper-evident band elongation after accelerated ageing at 40 °C for 72 h.

    Relative to a metallocene-catalysed HDPE of similar density, HE6062A typically has broader molecular weight distribution and lower low-temperature dart impact, but offers lower die swell and more stable melt pressure at high shear rates. The lower die swell reduces flash formation in multi-cavity tools but also reduces sealing force when a closure liner is over-moulded or compressed. Gasket compression tests should therefore follow ASTM F1149-24 or the converter’s equivalent leak-test protocol. Compared with a higher-flow HDPE with MFR above 12 g/10 min, HE6062A provides greater notched impact strength and ESCR, but may require elevated holding pressure or longer gate seal time for flow-length-to-thickness ratios above 250:1.

    Among Borealis HDPE grades, HE6062A is differentiated by the 6.2 g/10 min MFR and 962 kg/m³ density combination. Lower-density grades in the 945 kg/m³ class provide better stress-cracking resistance but lower top-load strength in closures. Top-load strength of a 30/25 closure in axial compression per ASTM D2659-16 is typically above 250 N at 23 °C; values below 180 N indicate inadequate venting or excessive filler. The product is not intended for film or sheet extrusion above 30 µm thickness because melt strength is insufficient for bubble stability in blown film at typical blow-up ratios.

    Under food-contact legislation, HE6062A is suitable for olefin polymer compliance assessments according to EU Regulation No 10/2011 and equivalent national provisions. For United States food-additive evaluations, high-density polyethylene of this density class may be referenced under 21 CFR 177.1520(c)3.2a or 21 CFR 177.1520(c)3.2b, depending on end-use extraction conditions. Converters must confirm simulant-specific overall migration and organoleptic performance under their own filling and sterilisation conditions. Data generated at 40 °C for 10 days in 10% ethanol may not be transferable to high-temperature retort applications.

    Storage and handling of HE6062A are non-hygroscopic in character; moisture uptake at 23 °C and 50% RH is below 0.01%. Pre-drying is normally unnecessary for material from intact sealed packaging. If surface condensation occurs from silo storage at ambient temperatures below 10 °C and subsequent transfer into a warm production hall, hopper drying at 70 °C for 2 h is sufficient. HE6062A should not be dry-blended with amine-containing processing aids or copper-based pro-oxidant masterbatches, because these additives can interact with the high-molecular-weight fraction and reduce environmental stress crack resistance under ASTM D1693-15 conditions. Regrind levels up to 20% by mass are commonly tolerated on closure lines, but regrind humidity above 0.2% or dust fines above 2% can destabilise feeding and increase cavity weight variation.

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