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Borealis HDPE HE6067

    • Product Name: Borealis HDPE HE6067
    • 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 231886
    Density 0.959 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 8.0 g/10 min
    Tensile Stress At Yield 28 MPa
    Tensile Stress At Break 30 MPa
    Tensile Strain At Break >600%
    Flexural Modulus 1400 MPa
    Charpy Notched Impact Strength 23 C 5 kJ/m²
    Shore D Hardness 62
    Vicat Softening Temperature 76°C
    Heat Deflection Temperature 0 46 Mpa 72°C
    Thermal Conductivity 0.4 W/m·K
    Specific Heat 1.8 J/g·°C
    Water Absorption <0.01%
    Moisture Absorption <0.01%

    As an accredited Borealis HDPE HE6067 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Borealis HDPE HE6067 is typically packaged in 25 kg polyethylene bags, with 55 bags per pallet.
    Container Loading (20′ FCL) Container Loading (20′ FCL) for Borealis HDPE HE6067: palletized 25 kg bags, shrink-wrapped, strapped, evenly distributed, and secured to prevent shifting.
    Shipping Borealis HDPE HE6067 is supplied as black high-density polyethylene pellets in 25 kg PE bags or octabins, palletized and shrink-wrapped. It is non-hazardous for transport, has no UN number, and should be shipped in clean, dry, covered trucks or containers, protected from moisture, heat, and direct sunlight.
    Storage Store Borealis HDPE HE6067 in original, tightly closed packaging in a cool, dry, well-ventilated area. Protect from direct sunlight, heat, ignition sources, moisture, dust, and contamination. Keep away from strong oxidizing agents. Use stable pallets, avoid prolonged UV exposure, and maintain clear labels. Recommended storage temperature: ambient, below 50°C. Rotate stock and keep containers sealed until use.
    Shelf Life Borealis HDPE HE6067 has a 2-year shelf life when stored unopened, cool, dry, and away from direct sunlight.
    Application of Borealis HDPE HE6067

    Extrusion Blow Moulding Envelope for Rigid Food-Contact Containers

    HE6067 enters monolayer food-contact blow moulding as a high-density polyethylene with a melt flow rate of 0.7 g/10 min measured at 190°C under 2.16 kg load according to ISO 1133-1:2022 and a density of 0.956 g/cm³ according to ISO 1183-1:2019. The melt rheology provides sufficient parison hang time for shuttle and long-stroke machines producing containers from 0.2 L to 5 L. The die head is set to 195–205°C, the die gap is held at 1.5–2.0 mm for bottle weights between 20 g and 120 g, and the blow-up ratio is limited to 2.2:1–2.8:1. Production equipment for this grade typically includes a single-screw extruder with a 24:1–30:1 L/D barrel, barrier screw, and Maddock mixing element. Head pressure at the breaker plate is monitored below 25 MPa to limit shear heating. Cooling water in the mould circuit is held at 8–12°C, and blow air is introduced at 0.5–0.7 MPa to reduce post-mould neck shrinkage.

    The additive formulation for monolayer food-contact bottles uses 97.5–99.0 wt% HE6067 with 1.0–2.5 wt% LDPE-based white masterbatch. The LDPE carrier must not exceed 2.5 wt% because additional low-molecular-weight polyethylene depresses environmental stress-crack resistance in the shoulder and pinch-off weld. A processing aid may be added at 0.1–0.3 wt% only when the specific grade appears on the positive list of the destination market. Compliance includes FDA 21 CFR §177.1520, EU Regulation (EU) No 10/2011 Annex I with an overall migration limit of 10 mg/dm², and GB 4806.6-2016. Terminal finished product types include refrigerated milk bottles up to 2 L, yogurt bottles, condiment squeeze bottles, and snack-food jars. Hot-fill applications with product temperatures above 80°C are outside the operational boundary for HE6067 because sidewall deformation and neck ovality exceed acceptable limits.

    Application scenarioGoverning standard or directiveCritical requirement
    Food-contact blow mouldingFDA 21 CFR §177.1520, EU Regulation (EU) No 10/2011, GB 4806.6-2016Overall migration 10 mg/dm²
    Surfactant-rich household chemicalsASTM D1693-15e1, ISO 22088-3:2010, REACH Annex XVIIESCR F50 retained on actual bottle geometry
    Post-consumer recycled blends94/62/EC, ISO 14021:2016, REACH Annex XVIIRecycled content claim validation
    Sheet and thermoformingFDA 21 CFR §177.1520, EU Regulation (EU) No 10/2011Gauge variation ±0.03 mm
    UN-certified jerricansADR Chapter 6.1, UN Model Regulations Chapter 6.124 h conditioning at −18°C before drop test
    Pharmaceutical and personal careUSP <661.1>, Ph. Eur. 3.1.3, EU Regulation (EU) No 10/2011Extractables and organoleptic neutrality

    Surfactant-rich household cleaning formulations impose a specific environmental stress-cracking load on HDPE sidewalls. Non-ionic ethoxylated surfactants and terpene solvents act as stress-cracking agents; in a 2 L trigger-spray bottle moulded from HE6067, the shoulder/body transition is maintained at 0.6–0.9 mm wall thickness and the main body at 0.5–0.8 mm. A 12-zone parison programmer is required to offset wall-thickness variation greater than ±0.1 mm at the pinch-off weld. Melt temperature at the die is controlled at 195–205°C; excursions above 210°C increase parison sag, while operation below 190°C produces shark-skin melt fracture at the die exit. The critical compliance test is environmental stress-crack resistance under ASTM D1693-15e1 condition B in 10% Igepal CO-630 at 50°C. Retained ESCR must be measured on the actual bottle, not on compression-moulded plaques, because the pinch-off weld and thread area reduce F50 time compared with the resin datasheet value.

    The formulation for this service is constrained to 99.0–99.5 wt% HE6067 with 0.5–1.0 wt% colour masterbatch; higher pigment loadings increase the crack initiation rate. A fluoroelastomer processing aid at 0.03–0.08 wt% is used only on high-output lines where die lip build-up causes streaking. Products made under this envelope include detergent bottles, fabric softener bottles, multi-surface cleaner trigger bottles, and bathroom cleaner bottles. Containers intended for oxidising solutions above 12% sodium hypochlorite are outside the unlined monolayer boundary and require fluorination or an internal barrier layer, because neck-area stress cracking under top-load can cause premature ruptures.

    What Limits ESCR Retention When HE6067 Is Blended with Post-Consumer Resin?

    The incorporation of post-consumer recycled HDPE into HE6067 for non-food blow moulding is operationally permitted but shifts the slow crack growth threshold. Published data for this specific HE6067/PCR configuration is limited; converters must establish lot-specific ESCR on the actual bottle geometry before freezing the formulation. The standard blend band for non-food containers is 70–80 wt% HE6067 with 20–30 wt% washed and ground post-consumer HDPE. For low-risk non-food products the recycled fraction is occasionally extended to 50 wt%, but the drop impact margin at −18°C narrows. A 0.5–1.0 wt% blue masterbatch is added, and antioxidant carry-over from the recycled fraction is compensated by adding 0.05–0.15 wt% of a phosphite antioxidant masterbatch.

    Processing uses a 30:1 L/D single-screw extruder with a continuous melt filter of 120–200 mesh to remove residual gel particles. Melt temperature is held at 195–205°C. The die gap is increased by 0.2–0.3 mm relative to virgin-only operation because the filter raises head pressure by 0.5–1.5 MPa. Compliance is anchored to EU Packaging and Packaging Waste Directive 94/62/EC, REACH Annex XVII, and ISO 14021:2016 for recycled content claims. Terminal products are restricted to non-food household chemical bottles, industrial packaging, and waste containers. Food-contact use is excluded unless the recycled fraction meets a valid EU novel-technology approval or an FDA letter of no objection for the specific recycling process.

    A three-roll polishing stack processing HE6067 at 200–230°C melt temperature produces sheet from 0.5 mm to 1.5 mm thickness. Compared with blow moulding, this route demands a lower melt-temperature spread across the die exit. Die bolt adjustment is used to maintain gauge variation within ±0.03 mm. The resin addition ratio is 100 wt% HE6067 for natural translucent sheet or 97.0–98.5 wt% HE6067 with 1.5–3.0 wt% white masterbatch for opaque food trays. For thermoforming, the sheet is heated to 120–130°C surface temperature and formed with plug-assisted tooling at a draw ratio not exceeding 2.5:1. Below that threshold the melt strength of HE6067 minimises corner thinning. Three-roll stack temperatures are held at 70–85°C for the polished roll and 50–65°C for the second roll to control sheet crystallinity.

    Compliance for food-contact sheet falls under FDA 21 CFR §177.1520 and EU Regulation (EU) No 10/2011, with the same overall migration limit of 10 mg/dm². Terminal parts include thermoformed freezer trays, dairy product trays, cosmetic packaging trays, and disposable protective packaging for industrial components. Published data for deep-draw HE6067 sheet beyond a draw ratio of 2.5:1 is limited; converters should evaluate plug material and dual-sheet thermoforming separately before committing to production.

    When UN Certification Requires −18°C Drop Performance in Blow-Moulded Jerricans

    UN-certified jerrican production from HE6067 moves the critical design parameter from ordinary ESCR to low-temperature impact after full-scale drop testing. Accumulator blow moulding machines with clamp forces of 50–150 t are used for 10–30 L containers, with a 2.5–3.5 mm die gap and melt temperature held at 190–205°C. The parison is programmed across 10 points so the sidewall remains at 0.8–1.2 mm and the corners at 1.4–2.0 mm. Wall-thickness deviation greater than ±0.2 mm at the handle juncture causes drop-test failures at the injection pinch line. Mould cooling water at 8–12°C and internal blow air at 0.4–0.7 MPa are used to stabilise neck dimensions.

    The formulation is set at 98.5–99.5 wt% HE6067, 0.5–1.5 wt% carbon black masterbatch for outdoor UV resistance, and 0.05–0.15 wt% hindered amine stabiliser masterbatch. Carbon black loadings above 1.5 wt% reduce the −18°C drop impact margin. Compliance is tested under ADR Chapter 6.1 and UN Model Regulations Chapter 6.1. The container is conditioned for 24 h at −18°C, filled to 98% capacity with water/glycol, and dropped from the packing-group-specified height. Terminal finished products include jerricans for lubricants, agrochemical concentrates, water-treatment chemicals, and automotive fluids. Containers for packing group I liquids are outside the standard HDPE jerrican boundary unless additional outer packaging or supplementary approval is provided.

    Pharmaceutical and personal care packaging lines require organoleptic neutrality and tight lot-to-lot control of odour, taste, and extractables. HE6067 is processed in closed extrusion blow moulding cells with HEPA-filtered blow air at 0.3–0.5 MPa and melt temperature maintained between 195°C and 205°C. The addition ratio for white bottles is 99.0–99.5 wt% HE6067 with 0.5–1.0 wt% white masterbatch pre-approved under USP <661.1> and Ph. Eur. 3.1.3 for polyolefins. Natural bottles are moulded at 100 wt% HE6067. Slip agents and antistatic additives are excluded because migration into the fill product changes the extractable profile and can fail the 10 mg/dm² overall migration limit under EU Regulation (EU) No 10/2011.

    Terminal products are limited to non-sterile oral and topical packaging, such as shampoo bottles, conditioner bottles, body wash containers, vitamin and nutraceutical bottles, and non-sterile topical cream containers. The resin is not intended for parenteral or ophthalmic primary containers. Any clean-room claim must be validated against ISO 14644-1 air cleanliness class and the selected terminal disinfection method. Extractables testing per USP <661.1> and Ph. Eur. 3.1.3 is performed on the finished container, not on the resin alone, because extrusion heat history can generate low-molecular-weight species that affect the result.

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    Certification & Compliance
    More Introduction

    Borealis HDPE HE6067 is a bimodal high-density polyethylene grade produced on a Borstar loop–gas-phase cascade. The product code HE6067 identifies a blow-moulding resin with a nominal density of 0.950 g/cm³ when measured according to ISO 1183-1:2019 and a melt flow rate of 0.7 g/10 min at 190 °C under 2.16 kg load according to ISO 1133-1:2022. The grade is supplied as natural or white pellets and is positioned for extrusion blow moulding of small to medium rigid containers for household chemicals, personal care products, and industrial liquids. The bimodal molecular weight distribution separates the high-molecular-weight fraction, which contributes parison melt strength and environmental stress crack resistance, from the lower-molecular-weight fraction that controls extruder torque and die pressure. On incoming resin release, converters normally measure density, melt flow rate, moisture content, and visual contamination against the supplier lot certificate. The density places HE6067 in a stiffness band typical of rigid HDPE containers, while the MFR value is low enough to restrict its use in high-speed injection moulding of thin-walled caps and closures. The exact lot-to-lot limits for ash, stabiliser content, and ESCR are controlled by the supplier specification and may vary with reactor campaign, additive package, and regrind policy.

    What Limits the Die-Head Temperature Window in Continuous Shuttle Blow Moulding?

    On a 60 mm grooved-feed extruder with a 24:1 L/D barrel and a 2.5 L accumulator shot capacity, HE6067 is typically processed with a feed-zone temperature of 170 °C, a metering-zone temperature of 200 °C, and a die-head temperature between 190 °C and 205 °C. The thermal window is narrow because the high-molecular-weight fraction begins to lose extensional viscosity above 210 °C. A parison length measured over 300 mm shows increased sag when parison programming is delayed by more than 0.5 s; the resulting wall-thickness variation is concentrated in the base and shoulder. Below 180 °C, the melt pressure at the die can exceed 25 MPa on a grooved-feed machine, producing sharkskin and surface melt fracture. The practical operating window around 195 °C is therefore approximately ±5 °C. The parison programmer is set to open the die gap 20–30 % during the first 20 mm of parison extrusion and to close it during the final 10 mm to compensate for gravity-induced thinning. Mould clamp force is maintained between 150 kN and 250 kN for containers up to 5 L, with blow pressure of 0.7–1.0 MPa. Published data specific to HE6067 in this exact configuration is limited, so start-up trials must record melt pressure, parison length variability, and pinch-off flash thickness before rate increases.

    PropertyMethodNominal or acceptance criterion
    DensityISO 1183-1:20190.950 g/cm³
    Melt flow rate (190 °C/2.16 kg)ISO 1133-1:20220.7 g/10 min
    Moisture contentISO 15512:2019< 0.05 % for sealed octabins
    Tensile modulusISO 527-2:2012Supplier certificate of analysis
    Environmental stress crack resistanceASTM D1693 or ISO 16770:2004Supplier certificate of analysis

    Environmental stress crack resistance in HE6067 is related to the bimodal molecular weight distribution rather than to density alone. The high-molecular-weight fraction increases the probability of intercrystalline tie-chain formation, while the lower-molecular-weight fraction retains processability. In slow crack growth testing according to ISO 16770:2004 or ASTM F1473, the crack propagates through the amorphous layer under plane-strain conditions; tie molecules must be physically disentangled or fractured for the crack to advance. A higher tie-molecule density therefore extends the failure time under constant load at a given stress intensity factor. For a 1 L detergent bottle, failure normally initiates at the pinch-off scar, where highly oriented weld-line material contains frozen-in stresses. The high-molecular-weight component in HE6067 strengthens this weld line, but the effect is sensitive to mould temperature. If the mould is maintained below 10 °C, the oriented skin solidifies before sufficient interdiffusion occurs, and the ESCR gain is partially lost. Mould temperatures between 12 °C and 25 °C are commonly used in shuttle machines for this grade; at the upper end, cycle time increases by 2–4 s per additional 5 °C. Published data for the exact ESCR improvement of HE6067 relative to a unimodal reference at a given cooling condition is limited.

    Tensile properties are not the primary selection criterion for HE6067. Specimens prepared by injection moulding or compression moulding and tested according to ISO 527-2:2012 usually show a yield stress between 22 MPa and 26 MPa and an elongation at yield between 8 % and 10 % for a 0.950 g/cm³ HDPE. Tensile modulus is commonly reported near 1000 MPa, but the exact value depends on specimen preparation, cooling rate, and testing speed. The relevant property for a blow-moulded container is slow crack growth resistance under hoop stress, not short-term tensile yield. In a 1 L detergent bottle with a 1 mm nominal sidewall, top-load resistance is governed by wall thickness distribution in the shoulder and base and by pinch-off integrity. A correctly programmed parison can produce a top-load failure load of 200–300 N; the same geometry with poor parison programming can fall below 150 N even though the resin modulus is unchanged. This sensitivity is observed across shuttle moulding lines and is a primary source of lot-to-lot performance complaints that are later resolved by process adjustment rather than resin change.

    Regulatory Status, Pre-Drying Boundaries, and Additive Incompatibilities

    For food-contact and pharmaceutical packaging, HE6067 must be evaluated under Commission Regulation (EU) No 10/2011 and FDA 21 CFR 177.1520 using the complete final article formulation. The base resin compliance does not automatically extend to masterbatches, regrind, or processing aids added at the converter. The grade is protected by a standard phenolic/phosphite antioxidant package. Combinations with certain amine-based additives or heavy-metal stearates can shift the organoleptic profile and accelerate yellowing at elevated melt temperatures. Pre-drying is not normally required for pellets stored in sealed octabins at relative humidity below 60 %. If the resin is exposed to air at relative humidity above 60 % for more than 4 h, surface moisture can produce splay and surface bubbles in the parison. In such cases a desiccant dryer is set to 75 °C for 2–3 h with a dew point below −20 °C. The drying temperature must not exceed 85 °C because pellet agglomeration can form in the hopper throat. Grade-specific moisture uptake data is not published, so converters with humid ambient conditions should install hopper-mounted dew point sensors and closed-loop material feed.

    When HE6067 Replaces a Higher-MFR Unimodal HDPE in Extrusion Blow Moulding

    The first measurable difference is melt pressure. A unimodal blow-moulding HDPE with an MFR of 1.5 g/10 min produces lower die-head pressure than HE6067 at the same screw speed and temperature; on a 60 mm grooved-feed extruder, the pressure increase can be 10–20 % depending on die gap and tooling. Die swell is also higher, requiring a die gap reduction of 10–15 % to maintain target wall thickness. Because the molecular weight distribution is broader, the shear-thinning index is larger; apparent viscosity at high die shear rates is lower than the MFR comparison alone would suggest, while melt strength at parison sag rates is higher. The practical effect is a longer parison hang time, which allows larger container diameters but reduces output on high-cadence shuttle lines. A line producing 1 L bottles at 1,200 bottles/h with a 0.9 g/10 min unimodal grade may need to reduce production rate by 5–10 % when HE6067 is introduced because the parison formation time is longer and the melt pressure is higher. Complete colour change on a 60 mm screw may require 20–30 min of purging with a low-viscosity LDPE or a commercial purging compound at 200–220 °C; the high-molecular-weight fraction retains boundary-layer material near the screw root and die lands. The difference is most visible at the pinch-off and weld line, where streaks persist if the purge is not run at full production speed. Attempts to compensate for the higher viscosity by raising die temperature above 220 °C degrade the high-MW fraction and reduce ESCR.

    Cooling time in HDPE blow moulding is controlled by part wall thickness and mould temperature. For a 1 L bottle with 1 mm nominal wall thickness, cycle time on a single-station shuttle machine is typically 10–14 s when the mould is held at 15 °C. Raising the mould temperature to 25 °C adds 2–4 s but improves interdiffusion at the pinch-off weld and raises resistance to stress cracking. Chilled water circuits are normally operated with a supply temperature of 8–12 °C; lower temperatures produce condensation on the mould surface and can create surface defects. The cooling time must be balanced against the parison hang time advantage of HE6067. If the mould is too cold, the oriented skin freezes before the high-molecular-weight chains have fully interdiffused across the weld line, reducing the ESCR benefit. Published data for HE6067-specific cooling curves is limited, but the relationship between mould temperature and weld-line interdiffusion in high-density polyethylene blow moulding is a known production variable.

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