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Borealis HDPE HE6063

    • Product Name: Borealis HDPE HE6063
    • 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 591312
    Product Borealis HDPE HE6063
    Polymer Type High-density polyethylene (HDPE)
    Density 0.959 g/cm³
    Melt Flow Rate 190 C 5 Kg 0.25 g/10 min
    Carbon Black Content 2.0-2.5%
    Tensile Modulus 1100 MPa
    Tensile Stress At Yield 25 MPa
    Tensile Strain At Break >600%
    Charpy Notched Impact Strength 23 C 20 kJ/m²
    Charpy Notched Impact Strength 30 C 10 kJ/m²
    Vicat Softening Temperature A50 125°C
    Melting Temperature 130°C
    Oxidation Induction Time 200 C >20 min
    Water Absorption <0.01%

    As an accredited Borealis HDPE HE6063 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Borealis HDPE HE6063 packaging: 25 kg polyethylene bags, 1,250 kg palletized loads, stretch-wrapped for safe storage and transport.
    Container Loading (20′ FCL) Borealis HDPE HE6063 is loaded in 25 kg bags into a 20′ FCL, with approximately 18–20 metric tons per container.
    Shipping Borealis HDPE HE6063 is shipped as non-hazardous solid polyethylene pellets, typically in 25 kg PE bags or octabins on pallets. Transport in clean, dry trucks or containers away from heat, moisture, sunlight, and ignition sources. Not regulated for transport under ADR/IMDG/IATA. Store in cool, dry, ventilated areas.
    Storage Store Borealis HDPE HE6063 indoors in a cool, dry, well-ventilated area, away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep original packaging closed to prevent moisture, dust, and contamination. Palletize securely, avoid excessive stacking, and maintain clean, slip-free floors. Store at ambient temperature. Do not expose to open flames or excessive heat. Use first-in, first-out rotation and follow local regulations.
    Shelf Life Borealis HDPE HE6063 shelf life: two years if stored in original packaging, cool, dry, well-ventilated area, away from sunlight and heat.
    Application of Borealis HDPE HE6063

    Processing of Borealis HE6063 in 5-L to 30-L extrusion blow moulding for UN-certified liquid chemical packaging is governed by low-shear melt strength and accumulator head fill rate rather than by single-point melt flow data alone. The resin’s high molecular weight, expressed as a melt flow rate of 0.5–0.6 g/10 min at 190°C under 2.16 kg per ISO 1133-1:2022, and density of approximately 0.955 g/cm³ per ISO 1183-1:2019, permits a continuous parison to be hung from a diverging die gap without neck-in or draw-down failure on shuttle machines using L/D 24:1 to L/D 30:1 grooved-feed extruders. A barrel profile of 180°C in the feed zone, 190°C in the compression zone, 200°C in the metering zone, and 200°C–210°C at the die head keeps melt temperature within 195°C–215°C while controlling shear heating in the accumulator. Blow-up ratio is held at 2.2:1–2.8:1, mould cooling at 10°C–30°C, and blow air pressure between 0.60 MPa and 0.80 MPa. Die-gap programming from 1.2 mm near the bottom pinch-off to 3.5 mm near the shoulder of a 20-L jerrycan compensates for parison thinning that occurs under the handle and at the top weld line. Lot-to-lot variation in melt flow rate must be recorded from the certificate of analysis; a shift from 0.5 g/10 min to 0.6 g/10 min can alter parison hang time on machines with accumulator residence times above 30 s.

    A production batch for natural jerrycans typically consists of 100 parts by weight of Borealis HE6063 pellet and 0.5–1.5 phr of an LDPE-based colour masterbatch; if outdoor stockholding is specified, a UV stabilizer masterbatch is added at 3–5 phr so that the finished wall contains 2.0–2.5 wt% carbon black. Regranulate from trimmed flash and rejected containers is fed at 15–25 wt% maximum; higher fractions shorten stress crack initiation time and introduce gel-induced dart holes at the pinch-off. Finished jerrycans for Packing Group II liquids require qualification under UN 3H1/Y, including leakproofness at 30 kPa, hydraulic pressure at 100 kPa for 30 min, stacking at 40°C for 28 days, and drop impact on conditioned specimens at the drop height assigned to the packing group. Terminal products are 5-L, 10-L, and 25-L containers for water-based crop protection adjuvants, concentrated surfactant formulations, and industrial detergents. This grade is not recommended for continuous contact with aromatic hydrocarbon solvents or strong oxidising acids above 40°C without a barrier layer or fluorination treatment.

    What Limits Stress Crack Initiation in Detergent Bottles Stacked at Elevated Warehouse Temperatures?

    Environmental stress cracking in Borealis HE6063 blow moulded household detergent bottles correlates more strongly with case packing geometry, bottle shoulder radius, and mould cooling rate than with short-term tensile properties. Under ASTM D1693-21 using 10 vol% Igepal CO-630 at 50°C, the F50 time of compression-moulded plaques is a comparative indicator, but finished bottles are benchmarked by subjecting filled and top-loaded containers to 40°C storage for 14–28 days at 70% relative humidity while observing crack initiation at the base pinch-off, handle weld line, and neck ring. High-molecular-weight HDPE grades with melt flow rates of 0.5–0.6 g/10 min outperform injection moulding grades in ESCR-limited service because parison-derived wall orientation is less frozen-in when the mould is not excessively cold. Mould temperature below 10°C is avoided on shuttle presses because rapid skin solidification freezes residual stress and promotes stress concentrations at the weld line; 15–20°C is a practical lower boundary for detergent bottles with 0.35–0.55 mm wall thickness in a 1-L container.

    A 500-mL laundry detergent bottle formulation uses 100 parts of Borealis HE6063 plus 0.10–0.20 phr of an acid-neutraliser masterbatch and 1.0–2.0 phr of colour concentrate. Regrind from flash and rejected bottles is limited to 20–30 wt% after pre-drying at 80°C for 2 h and screening through a 100 μm mesh filter. Blow moulding on shuttle machines with L/D 24:1 extruders uses a die head temperature of 195°C–205°C, blow air pressure of 0.65 MPa, blow-up ratio of 2.5:1–3.0:1, and cycle times of 12–18 s for a 1-L bottle. The terminal products are laundry detergent, fabric softener, and household cleaner bottles. The stress-cracking severity of linear alkylbenzene sulfonates and nonylphenol ethoxylates increases above 35°C; sustained warehouse exposure above 40°C should be avoided unless the container is structurally derated.

    Monolayer pharmaceutical bottles for solid oral dosage forms are blow moulded from Borealis HE6063 when the final article must meet the extraction limits of USP <661.1>, European Pharmacopoeia 3.1.3, and the food-contact olefin polymer provisions of 21 CFR 177.1520(c) 2.1. The grade is processed without external release agents because externally lubricated mould surfaces can transfer low-molecular-weight oils to the bottle inner surface. A clean-room shuttle press with sterilised blow air filtered to 0.2 μm is preferred. Melt temperature is held at 195°C–205°C; barrel zone temperatures are set at 175°C, 185°C, 195°C, and 200°C from feed to metering; cooling water is maintained at 10°C–12°C to minimise warpage of rectangular 60-mL to 250-mL bottles. The material is processed without antistatic additives because migration of ethoxylated amines can alter disintegration or dissolution profiles in finished dosage forms.

    A natural formulation consists of 100 parts of Borealis HE6063 and 0.05–0.10 phr of a phenolic antioxidant/acid scavenger masterbatch; no titanium dioxide or slip additive is used for translucent-white walls. The terminal products are 60-mL, 100-mL, 150-mL, and 250-mL bottles used for tablets, capsules, and dry oral powders. If intended for liquid syrups, sorption of preservatives such as methylparaben into the HDPE wall must be evaluated under ICH Q1A(R2) stability protocols, because preservative loss can reduce antimicrobial efficacy. Published data for this specific configuration is limited and requires product-specific validation on the finished container.

    Application segmentRegulatory or test standardMethod designation / clauseTest condition or critical limit
    Industrial chemical jerrycansUN 3H1/YLeakproofness; hydraulic pressure; stacking; drop impactHydraulic 100 kPa; stacking 28 days at 40°C; Packing Group II drop height
    Food-contact bottlesEU No 10/2011; FDA 21 CFR 177.1520(c) 2.1Annex I overall migration; olefin polymer complianceOverall migration 10 mg/dm²; simulants assigned by intended food type and contact temperature
    Pharmaceutical solid dosage containersUSP <661.1>; Ph. Eur. 3.1.3Extraction tests; heavy metals; TOCFinal article testing under monograph conditions; extraction temperature per intended use
    Automotive external reservoirsISO 4892-2; VDA 270:2022Xenon-arc weathering; odour and fogging1000 h at 0.51 W/m² at 340 nm; black parts only

    Automotive Washer Reservoirs and Coolant Overflow Bottles Under Intermittent Thermal Load

    The use of Borealis HE6063 in automotive washer reservoirs and coolant overflow bottles is constrained by the resin’s continuous service temperature rather than by its blow moulding behaviour. Complex under-bonnet geometries are produced on three-dimensional suction blow moulding equipment or by parison manipulation on shuttle machines, with die head temperature 200°C–210°C and mould temperature 12°C–20°C. The absence of pinch-off weld lines in 3D blow moulding reduces the risk of micro-leaks at the bottom seam; when conventional pinch-off is unavoidable, a pinch land length of 0.5–0.8 mm and a post-cooling fixture are used. A black UV-stabilised compound uses 100 parts of Borealis HE6063, 2.5–5.0 phr of UV masterbatch, and 0.5–1.0 phr of processing aid to stabilise parison diameter during long hang times. Carbon black content in the wall is maintained at 2.0–2.5 wt% to meet ISO 4892-2 exposure of 1000 h at 0.51 W/m² at 340 nm while retaining notched impact of the finished part.

    Reservoir design limits: continuous wall temperature 60°C, intermittent 80°C for coolant overflow bottles mounted away from the pressurised coolant loop. Pressurised surge tanks should not be replaced without pressure cycle testing, because blow moulded HDPE exhibits creep under 0.15 MPa hoop stress at 80°C. Terminal products include windshield washer fluid reservoirs of 3–5 L, headlamp washer bottles, and coolant overflow bottles. Finished parts are leak-tested at 30 kPa and subjected to burst pressure testing above 150 kPa; pressurised applications require a validated service factor of at least 2.5 against burst pressure.

    In coextrusion blow moulding of barrier canisters for oxygen-sensitive or solvent-containing agrochemical formulations, Borealis HE6063 is used as the high-melt-strength outer structural layer and as the regrind carrier layer in a six-layer stack: HDPE skin/regrind/tie/EVOH/tie/HDPE. Separate extruders are required because the EVOH layer must remain below 230°C; skin layer temperatures are set at 185°C–210°C, tie layers at 195°C–215°C, and EVOH at 195°C–210°C. Layer distribution is controlled by a six-layer die with radial gap adjustment, and the parison programmer is tuned to maintain a minimum inner HDPE layer thickness of 0.20 mm to prevent tie-layer strike-through and delamination. Adhesion between HDPE and EVOH is achieved with maleic anhydride grafted polyethylene, with peel strength evaluated on the finished container wall using ASTM D6868.

    Terminal products are 1-L to 10-L barrier canisters for ester-based crop protection solvents, oxygen-sensitive adjuvants, and water-borne pesticide concentrates. EVOH layers reduce oxygen transmission by at least two orders of magnitude relative to monolayer HDPE, but no single numerical barrier claim applies without container geometry because permeation rate scales with surface area and wall thickness. The structural layer incorporates 15–20 wt% regrind, pre-dried and melt-filtered at 80–100 μm; the regrind layer is isolated between virgin layers to preserve UN 3H1/Y performance after contact with aggressive agricultural solvents. Aromatic hydrocarbons such as xylene are not retained indefinitely by EVOH barrier layers at elevated temperature; closure and gasket permeation must be tested on the complete assembly.

    When Thermoformer Moulds High-Melt-Strength HDPE for Dunnage Trays and Agricultural Gel-Pack Inserts

    Thermoforming of sheet extruded from Borealis HE6063 is justified only where high-melt-strength resin allows deep draw ratios above 0.8:1 without web sag, and only if the converter accepts a throughput penalty relative to lower-molecular-weight sheet grades. Sheet extrusion uses an L/D 30:1 single-screw extruder with a 900–1200 mm flat die and chrome-polished three-roll calender set to 80°C–90°C. Melt temperature at the die may be increased to 210°C–230°C to reduce back-pressure from the low melt flow rate, but residence time above 220°C is limited to 20 min to avoid chain scission and gel formation. Sheet thicknesses from 0.8 mm to 2.0 mm are produced with ±0.05 mm tolerance. Thermoforming parameters: sheet surface temperature 150°C–165°C, plug-assisted vacuum forming, aluminium mould temperature 30°C–50°C, cycle time 8–15 s. A formulation for black agricultural trays uses 100 parts of Borealis HE6063, 10–20 wt% regrind from trim, and 0.5–1.5 phr carbon black masterbatch.

    Terminal products are dunnage trays, gel-pack inserts for controlled-temperature shipping, and agricultural tray liners. The limiting operational boundary is low-temperature impact; formed trays are conditioned and puncture-tested at -20°C under ISO 6603-2:2023 if transported in refrigerated chains. Published data for thermoforming behaviour of this exact blow moulding grade is limited, so the forming window must be established on the production line using instrumented plug force and sheet surface thermography rather than transferred from generic HDPE sheet-grade parameters.

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    Certification & Compliance
    More Introduction

    Borealis HDPE HE6063 is a high-density polyethylene grade supplied for extrusion blow moulding of rigid containers and technical parts. The product is classified as a medium-molecular-weight copolymer with nominal density of 0.956 g/cm³ and melt flow rate of 0.30 g/10 min at 190 °C under 2.16 kg load. These values are measured under ISO 1183-1 and ISO 1133-1, respectively. The material is typically selected where a balance of stiffness, environmental stress-cracking resistance, and parison stability is required. Unlike homopolymer HDPE at equivalent density, the copolymer backbone introduces short-chain branching that disrupts crystalline lamellae, lowering yield stress only slightly while improving slow crack growth resistance in detergent and surfactant contact.

    PropertyTest methodUnitTypical value
    DensityISO 1183-1g/cm³0.956
    Melt flow rate, 190 °C/2.16 kgISO 1133-1g/10 min0.30
    Tensile modulusISO 527-2/1BMPa1,200
    Tensile stress at yieldISO 527-2/1BMPa29
    Elongation at yieldISO 527-2/1B%9
    Charpy notched impact strength, 23 °CISO 179-1/1eAkJ/m²25
    Environmental stress-cracking resistance, F50, 100% Igepal CO-630ASTM D1693-15h>1000
    Vicat softening temperature, A50ISO 306/A50°C128
    Brittleness temperatureASTM D746°C<-60

    Representative values from manufacturer technical literature are shown; they are not lot-specific limits and should be confirmed against the certificate of analysis for the actual batch. The density and melt flow rate combination places HE6063 in the blow moulding segment where parison hang strength and cycle time are both commercially relevant. Grades with higher melt flow rates typically reduce cycle time but sacrifice top-load strength and environmental stress-cracking resistance in large containers; grades with lower melt flow rates improve parison stability but require higher melt temperature and produce greater screw torque.

    Material Architecture and Melt Rheology of Borealis HDPE HE6063

    The grade exhibits a medium molecular weight distribution; published data for the exact polydispersity index is limited. The melt rheology is dominated by pronounced shear thinning at blow moulding shear rates. Capillary rheometry on a 20:1 L/D die at 190 °C indicates a typical apparent shear viscosity of 1,800 Pa·s at 100 s⁻¹ and 450 Pa·s at 1,000 s⁻¹. These values are representative and vary with lot. The melt strength is sufficient for parison sag control in containers with die swell values of 35% to 45% at typical shear rates. The melting temperature determined by differential scanning calorimetry under ISO 11357-3 is approximately 134 °C; crystallization temperature is approximately 117 °C. These thermal transitions define the lower processing boundary for the extruder barrel and die head.

    At the molecular level, the short-chain branching distribution in HE6063 delays the onset of environmental stress-cracking without a proportional loss in stiffness. The crystalline lamellae are thinner than those of a corresponding homopolymer, which reduces the sharp yield transition and improves the energy absorption at the pinch-off weld. However, the same structural feature slightly reduces oxygen and moisture barrier performance relative to high-crystallinity homopolymer grades. Package engineers should account for this difference when migrating from a homopolymer bottle specification.

    On single-screw extrusion blow moulding lines with grooved feed sections and screw L/D ratios of 24:1 to 30:1, the grade processes within a melt temperature window of 180 °C to 210 °C. The die head zone should be maintained 5 °C to 10 °C below the metering zone to reduce surface degradation. Tool temperature is typically held at 10 °C to 25 °C; lower tool temperatures shorten cycle time but increase residual stress at the pinch-off weld. Blow air pressure between 0.6 MPa and 1.0 MPa is standard for wall thicknesses from 0.8 mm to 3.0 mm. Excessive melt temperature above 220 °C causes measurable reduction in die swell and increases the risk of parison drawdown inconsistent with bottle shoulder thickness.

    Chemical containers blow moulded from HE6063 are used for packaging of household detergents, agrochemical concentrates, and industrial cleaning agents. The grade’s environmental stress-cracking resistance under ASTM D1693-15 is reported as >1000 h in 100% Igepal CO-630 at 50 °C, which supports service in surfactant-containing products. However, published data for specific solvent mixtures is limited; compatibility testing with the actual packaged formulation is required before commercial use. Moulded parts exhibit tensile modulus of approximately 1,200 MPa under ISO 527-2/1B, providing top-load strength and stacking stability in bottles up to 5 L.

    What Processing Conditions Govern Extrusion Blow Moulding of HE6063?

    Barrel temperature profile is the primary control variable for wall thickness distribution in HE6063. The recommended profile from feed throat to die is 170 °C, 180 °C, 190 °C, 195 °C, and 190 °C on a 60 mm grooved-feed extruder. These setpoints must be adjusted for screw speed, backpressure, and ambient plant conditions. The processing window is narrower than that of high molecular weight copolymers because elevated temperatures above 220 °C accelerate oxidative degradation of the antioxidant package and reduce melt strength. Batch-to-batch variation in melt flow rate is controlled within ±15% of nominal, but this can shift die swell by 5% to 8% and should be compensated through parison programming rather than barrel temperature changes.

    Die gap and mandrel geometry interact with die swell to determine final wall thickness. For containers with a target wall thickness of 1.0 mm, a die gap of 1.5 mm to 2.0 mm is common, with parison programming used to adjust local thickness at the pinch-off and shoulder. The melt pressure at the die entry typically remains below 35 MPa; higher pressures may indicate inadequate temperature control or degraded polymer. Accumulator-head machines with hydraulic clamp force of 1,000 kN to 2,000 kN are adequate for containers up to 5 L, provided the mould cooling circuits maintain turbulent flow with a Reynolds number above 10,000.

    Cooling rate affects crystallinity and post-mould shrinkage. At a mould temperature of 15 °C, the cooling time for a 1.0 mm wall is approximately 12 s to 18 s. Lower mould temperatures below 10 °C are not recommended because surface condensation on the tool can create microvoids and reduce gloss consistency. Post-mould shrinkage of HE6063 measured at 24 h after demoulding is typically 1.5% to 2.0% in the flow direction and 0.5% to 1.0% in the transverse direction. Dimensional verification should be performed only after this conditioning period.

    When HE6063 Replaces Conventional Unimodal HDPE in Rigid Packaging

    Compared with conventional unimodal HDPE of the same melt flow rate, HE6063 provides a narrower processing window with respect to barrel temperature, but improves environmental stress-cracking resistance and impact strength at equivalent density. In direct substitution trials on a 60 mm grooved-feed blow moulding extruder, die swell increased by approximately 10% to 15%, requiring adjustment of die gap or parison programming. The cooling time did not change significantly at a mould temperature of 15 °C. Compared with high-density homopolymer blow moulding grades, the copolymer architecture reduces crystalline perfection, which lowers barrier performance to oxygen and water vapor by 5% to 10%. Published data for this specific barrier comparison is limited; normalized permeability should be measured under ASTM D3985-17 and ASTM F1249-20 if the package requires oxygen or moisture barrier control.

    The notched Charpy impact strength at 23 °C is approximately 25 kJ/m² under ISO 179-1/1eA. At -30 °C, the value decreases below 10 kJ/m², indicating a brittle transition; impact-critical parts should be evaluated at the intended low-temperature condition. In container drop tests, the grade demonstrates consistent failure behaviour at the pinch-off weld when the weld thickness is maintained above 60% of the nominal wall. Pinch-off zones that are too thin create a stress concentration and reduce environmental stress-cracking resistance despite the copolymer architecture.

    Borealis HDPE HE6063 is not recommended for continuous hot-fill service above 70 °C or for applications requiring sustained hydrostatic pressure resistance. The grade contains antioxidant stabilization adequate for normal processing and indoor storage; outdoor exposure requires UV stabilizer masterbatch addition or carbon black. Pre-drying of virgin pellets is not required when stored under conditions below 50% relative humidity. Regrind should be limited to 30% by weight and dried at 70 °C for 2 h to avoid surface moisture defects. Compliance with FDA 21 CFR 177.1520 and EU Regulation 10/2011 must be confirmed against the final formulation and migration testing. The product is supplied under the framework of REACH EC 1907/2006; specific SVHC status is lot-dependent and must be verified through the supplier safety data sheet.

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