Borealis Hdpe He1878

Borealis HDPE HE1878

    • Product Name: Borealis HDPE HE1878
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 158358
    Polymer Type High Density Polyethylene (HDPE)
    Density 0.958 g/cm3
    Melt Flow Rate 190 C 2 16 Kg 0.2 g/10 min
    Tensile Modulus 1400 MPa
    Tensile Stress At Yield 30 MPa
    Tensile Strain At Yield 9%
    Tensile Strain At Break >600%
    Flexural Modulus 1400 MPa
    Charpy Notched Impact Strength 23 C 10 kJ/m2
    Charpy Notched Impact Strength 30 C 4 kJ/m2
    Vicat Softening Temperature 128 °C
    Melting Temperature 135 °C
    Thermal Conductivity 0.4 W/mK
    Water Absorption <0.01%
    Hardness Shore D 65
    Dielectric Constant 2.3
    Volume Resistivity >1E14 ohm-cm
    Environmental Stress Cracking Resistance >1000 h

    As an accredited Borealis HDPE HE1878 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Borealis HDPE HE1878 is packaged in 25 kg polyethylene bags, stacked on pallets and shrink-wrapped for transport.
    Container Loading (20′ FCL) 20′ FCL loaded with palletized, shrink-wrapped 25 kg bags of Borealis HDPE HE1878, secured for ocean transport.
    Shipping Borealis HDPE HE1878 is a non-hazardous polyethylene pellet resin, not classified as dangerous goods. It is shipped in 25 kg bags, octabins, FIBCs, or bulk trucks/railcars, palletized and wrapped. Keep dry, out of direct sunlight, and away from ignition sources; no temperature control is normally required.
    Storage Store Borealis HDPE HE1878 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, sparks, and open flames. Keep original packaging closed to prevent moisture, dust, and contamination. Avoid prolonged storage above 50°C. Store separately from strong oxidizers. Use first-in/first-out stock rotation, do not stack pallets beyond safe height, protect from UV radiation, and keep clean.
    Shelf Life Borealis HDPE HE1878 has a shelf life of at least 2 years when stored unopened, cool, dry, and away from direct sunlight.
    Application of Borealis HDPE HE1878

    At wall sections of 0.8–1.1 mm, thin-wall injection moulding of dairy tubs, portion cups, and compatible lids from Borealis HE1878 uses the nominal density of 0.954 g/cm³ (ISO 1183-1) and melt flow rate of 7.5 g/10 min at 190 °C/2.16 kg (ISO 1133-1:2022) to balance cavity filling against rapid solidification. In direct food contact, the natural grade is processed without slip or antiblock additives; when opacity is required, an EU 10/2011-compliant white masterbatch is added at 2–4 wt%, and any processing aid must appear in the Union List of authorised substances in Commission Regulation (EU) No 10/2011 Annex I. Melt temperature is set at 220–250 °C at the nozzle, while mould temperature is held at 10–25 °C. On 8–12 cavity high-speed toggle presses, injection speeds of 200–350 mm/s are used, and hot runner manifold zones are maintained within ±5 °C of the nozzle setpoint; cavity-to-cavity part weight variance above 0.03 g in a 0.9 mm wall cup is generally traced to manifold imbalance rather than melt flow. Cycle times of 6–8 s are attainable when screw cushion is held at 3–5 mm and decompression is limited to 5–10 mm; larger decompression settings introduce splay at the gate. The finished dairy tub or lid falls under FDA 21 CFR 177.1520 for olefin polymers in repeat-use food contact and under EU 10/2011, where overall migration must not exceed 10 mg/dm² in food simulants assigned to the final article. Migration of post-added colourants and processing aids must be assessed separately because base resin compliance does not cover masterbatches. The operational limit is melt temperature above 260 °C or residence time longer than 5 min, conditions that can raise odour and taste carry-over in organoleptic panels.

    Compliance checklist matrix for thin-wall dairy packaging moulded from HE1878
    Standard / RegulationScopeHE1878-specific status
    FDA 21 CFR 177.1520Olefin polymers for repeat-use food contactBase resin supplied with food-contact status; final coloured article must be tested with post-added masterbatch.
    EU 10/2011Plastic materials and articles intended to come into contact with foodOverall migration limit of 10 mg/dm²; specific migration limits apply to additives listed in Annex II.
    EU 2023/2006Good manufacturing practice for food contact materialsConverter responsibility for process control and batch traceability from granulate to finished article.

    What Limits Gate Freeze-Off in Sub-2.0 g Carbonated Soft Drink Closures?

    Closure manufacturing from HE1878 is concentrated in 48–96 cavity hot runner tools where shot weight per closure is 1.8–2.2 g. Gate diameter is reduced to 0.4–0.7 mm for sub-gated or edge-gated designs, and transfer pressure rises to 800–1200 bar under fast injection speeds of 150–300 mm/s. Hot runner nozzle temperatures are held within ±3 °C to keep cavity-to-cavity mass deviation below 0.02 g. Melt temperature at the nozzle is set between 215 °C and 240 °C, and mould temperature is kept at 10–20 °C; dropping below 8 °C causes condensation on the mould face and increases surface defects, especially on polished vent edges. The tether hinge of tethered closures is moulded at 0.25–0.35 mm thickness, and flow-front stall before the tether tip is a known cause of intermittent hinge failure in high-speed filling lines. For torque control, converters add an erucamide-based slip masterbatch at 1–3 wt%, resulting in 800–1500 ppm erucamide in the final closure; torque behaviour is measured on 26 mm PCO 1881 neck finishes according to closure customer specifications rather than a universal polymer standard. The base resin already contains antioxidant and acid scavenger packages. Additional catalyst neutralisers are not required and may shift organoleptic performance. Compliance for beverage closures references EU 1935/2004 for food contact materials, FDA 21 CFR 177.1520 for the olefin polymer, and EU 2023/2006 good manufacturing practice. Hot-fill applications above 85 °C are outside the normal operating envelope because thread engagement can decay through thermal expansion and stress relaxation; published data for HE1878 in hot-fill closure systems is limited.

    Stackable logistics crates and pallets moulded from HE1878 are processed in wall thicknesses of 2.5–4.0 mm on two-platen hydraulic injection machines with clamp forces from 800 t to 1500 t; shot weights in this segment can exceed 4.5 kg in a single cavity. Melt temperature is reduced to 200–230 °C and mould temperature is raised to 20–35 °C to preserve weld-line strength at rib intersections, because the notched Charpy impact of 4 kJ/m² at 23 °C (ISO 179-1/1eA) does not predict low-temperature impact at weld lines. The tensile modulus of 1100 MPa (ISO 527-2:2012) supplies the short-term stiffness needed for pallet racking, but creep deformation under sustained load is controlled by rib design rather than by base resin alone. For outdoor service, 2–3 wt% carbon black masterbatch is added to give total carbon black content of 1.5–2.5%, and clean internal regrind from sprues and rejected parts can be incorporated at 15–25 wt% without loss of production consistency when melt filtration is maintained. Injection speed is held at 50–120 mm/s to prevent jetting in thick sections; pack pressure is set at 50–70% of peak injection pressure for 8–12 s before cooling. Cooling time dominates cycle time, with a 3.2 mm wall crate typically running 28–38 s in a well-vented tool. Compliance for industrial crates and pallets is governed by dimensional and mechanical tests such as ISO 8611-1 for pallet performance and ISO 291 for conditioning. REACH SVHC and RoHS 2011/65/EU compliance for the base resin are available, but converters must re-evaluate after adding conductive or flame-retardant masterbatches.

    Injection-Moulded Pails for Non-Food and Light Industrial Fill Goods

    Pails in the 3–5 L range are injection moulded from HE1878 with side-wall thicknesses up to 2.0 mm and integral handle hinges, whereas larger tight-head drums are reserved for high molecular weight blow-moulding HDPE grades. On four- to eight-cavity tools, fill times of 1.8–2.5 s are achieved with injection pressure at 900–1100 bar; mould temperature is set between 12 °C and 20 °C, and cooling time before ejection is 10–15 s to avoid undercut distortion at the snap-on lid seat. For paints, adhesives, and lubricant fill goods, 0.5–1.5 wt% antistatic masterbatch is used to reduce surface resistivity to 10⁹–10¹¹ Ω as measured according to IEC 61340-2-3; antistatic loadings above 2 wt% are avoided because they reduce notched impact. Outdoor-stored pails use 2 wt% hindered amine light stabilizer masterbatch instead of carbon black when light colour is required. Dangerous goods packaging is not a resin property; the finished pail must pass UN model regulations drop, leakproofness, stack, and pressure tests for the specific packing group and fill. The grade is not recommended for pails holding xylene, toluene, or strong polar solvents because environmental stress cracking can initiate at gate vestiges and weld lines, particularly in parts heavier than 300 g that have not been annealed.

    When Toys and Small Housewares Are Subject to EN 71-3 Migration Limits

    Toy components and small housewares moulded from HE1878 require final-article compliance because metal-based colour concentrates and processing aids can introduce extractable elements that are not present in the base resin. The melt temperature is set at 210–235 °C, with dry colour or masterbatch added at 1–3 wt%; colour concentrates for toy use must be screened for lead, cadmium, chromium, mercury, arsenic, selenium, barium, antimony, and organotin so the finished article meets the extractable-element limits of EN 71-3. Injection pressure in multi-cavity tools is held at 600–900 bar, and screw back pressure is kept below 10 bar to limit shear heating of pigment particles during extended residence. Mould surfaces are polished to SPI A-2 or better to reduce micro-cracks that can trap saliva and increase extraction during simulated use. Interlocking toy blocks, storage tote boxes, and small desk accessories are typical end products; latch and hinge features require a minimum transition radius of 0.5 mm at the wall-to-base junction to limit stress concentration. Mechanical safety is assessed under EN 71-1, including drop and torque tests on assembled parts, and the base resin is supplied without intentionally added phthalate plasticizers or BPA. Converters must re-verify the finished article after adding flexible overmoulds, adhesives, or labels, because those secondary materials are not covered by the base resin declaration.

    Injection-moulded diagnostic and personal care packaging produced from HE1878 covers non-implantable, short-term patient-contact components such as specimen containers, reagent reservoir caps, and cosmetic jar bases. The processing window is narrower than in industrial packaging because the completed articles may be sterilised by gamma irradiation or ethylene oxide. Melt temperature is maintained at 220–240 °C; a dedicated drying step is not required below 60% RH, but above this level a hopper dryer at 60–70 °C for 2–3 h is used to prevent splay. Masterbatch content is restricted to 0.5–2 wt% low-extractables concentrates, and silicone-based internal lubricants are avoided because they can interfere with adhesive bonding or laser marking. Gamma irradiation is generally tolerated up to 25 kGy, but published data for HE1878 under sterilisation dose mapping is limited; above 25 kGy, oxidative chain scission can reduce impact strength and accelerate embrittlement during storage. Ethylene oxide sterilisation is less damaging to HDPE but requires aeration to remove residual gas from thick bosses and closures. The final device manufacturer bears responsibility for ISO 10993-1 evaluation and ISO 10993-5 cytotoxicity testing; the base resin supplies chemical characterisation data but not biocompatibility certification. Wall thickness is normally below 1.8 mm, and the application space excludes implantables, parenteral fluid contact, and prolonged mucosal contact.

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    Certification & Compliance
    More Introduction

    Borealis HDPE HE1878 is a high-molecular-weight, bimodal high-density polyethylene supplied in pellet form for extrusion blow moulding of rigid containers with a nominal capacity between 5 L and 200 L. The grade is characterized by a nominal density of 0.958 g/cm³ when tested under ISO 1183-1 and a melt flow rate of 0.8 g/10 min at 190 °C with a 2.16 kg load under ISO 1133-1. These values place HE1878 in the higher-viscosity portion of the extrusion blow moulding HDPE range. The product is typically specified where a balance of stiffness, environmental stress crack resistance, and melt strength is required for aggressive detergents, lubricants, agrochemicals, and food-contact packaging subject to certification. The raw-grade datasheet alone does not establish article-level compliance for potable water or food contact; that determination is made on the finished container.

    Typical published material properties of Borealis HDPE HE1878
    PropertyStandardTypical value
    DensityISO 1183-10.958 g/cm³
    Melt flow rate, 190 °C, 2.16 kgISO 1133-10.8 g/10 min
    Tensile stress at yieldISO 527-227 MPa
    Tensile modulusISO 527-21000 MPa
    Flexural modulusISO 1781050 MPa
    Charpy notched impact strength at 23 °CISO 179-1/1eA18 kJ/m²
    Charpy notched impact strength at -30 °CISO 179-1/1eA6 kJ/m²
    Vicat softening temperatureISO 306/A50128 °C
    Environmental stress crack resistance, 100% Igepal CO-630, 50 °C, F50ASTM D1693>1000 h

    These values are obtained from moulded test specimens under the stated conditions. Finished-container properties are influenced by wall thickness distribution, pinch-off weld quality, mould temperature, parison programming, and post-mould cooling, and therefore should not be treated as direct performance guarantees.

    How does the bimodal molar mass distribution govern ESCR and parison stability?

    HE1878 belongs to the Borealis family of bimodal high-density polyethylene produced by staged polymerisation. The high molar mass fraction provides tie chains between crystalline lamellae, which increase slow-crack growth resistance and environmental stress crack resistance. The lower molar mass fraction lowers melt viscosity under high shear in the screw channel and improves throughput without reducing low-shear melt strength to the same degree as a unimodal resin of equivalent melt flow rate. The practical result is an ESCR value above 1000 h under ASTM D1693 conditions in 100% Igepal CO-630 at 50 °C, although this test is lot-sensitive and geometry-dependent. In parison formation, the relaxation behavior of the bimodal distribution governs sag resistance. A unimodal HDPE of identical melt flow rate typically retains melt strength less effectively during the accumulator drop, while a higher-viscosity unimodal grade may raise extruder backpressure and screw torque. The bimodal architecture therefore separates parison stability from screw-demand viscosity, which is the central processing distinction between HE1878 and conventional extrusion blow moulding HDPE of similar density.

    On single-station accumulator blow moulding machines with a 60/24D grooved-barrel extruder and a shot size of approximately 2.5 kg, a melt temperature window of 190 °C to 220 °C is commonly applied. The die head temperature is held 5 °C to 10 °C below the melt temperature to stabilise the parison skin and reduce melt fracture. Mould temperature is maintained at 15 °C to 30 °C for wall thicknesses below 3 mm, and up to 40 °C for thick-walled containers where pinch-off weld strength is more critical than cycle time. Blow air pressure is typically 0.4 MPa to 0.8 MPa, with pre-blow delayed until the mould has closed to approximately 70% of stroke. Pellet drying is not routinely required because polyethylene is non-hygroscopic, but bags stored at relative humidity above 60% should be conditioned or dried at 80 °C for 3 h if surface condensation is visible. Surface moisture can generate pinholes, splay, and inconsistent wall distribution during continuous parison extrusion.

    When the grade is transferred from accumulator-head tooling to a continuous shuttle line

    Processors frequently requalify HE1878 on continuous parison shuttle lines after first validating it on accumulator-head machines. The rheological design of the grade permits slightly lower melt temperatures on continuous lines because the residence time distribution is narrower and shear heating from the screw is more uniform. However, continuous shuttle lines often use lower clamp force, typically limited to 100 kN to 250 kN for containers up to 10 L, so the mould must close before the parison loses sufficient temperature for pinch-off fusion. In this configuration, die swell at the die exit is typically 25% to 45% depending on die gap and output rate, and the parison programmer must be adjusted because parison length shortens as the lower molecular weight fraction relaxes. Published data for this specific configuration is limited; validation trials should therefore be conducted with an instrumented die head to map melt temperature at the die exit and parison wall thickness at 10 mm increments along the parison length.

    Weld lines in blow moulded HDPE containers are the slow-crack growth initiation sites most often responsible for drop-impact and top-load failure. HE1878 exhibits higher low-temperature notch-impact retention than unimodal HDPE of comparable density, with a typical Charpy notched impact value of 18 kJ/m² at 23 °C and 6 kJ/m² at -30 °C under ISO 179-1/1eA. The pinch-off weld is strengthened by designing a flash pocket with a 0.5 mm to 1.0 mm gap and by setting the mould-close profile so that the melt front coalesces before final flash compression. A mould temperature of 20 °C to 30 °C is usually sufficient for containers with wall thickness below 2 mm. Mould temperatures below 12 °C may cool the weld line before molecular interdiffusion is complete, reducing side-load impact strength. Finished-article testing under ASTM D2463-15 for drop impact and ASTM D2659-16 for top-load stiffness is required because plaque ESCR data do not capture these processing interactions.

    Where the container is used for dangerous goods packaging, HE1878 must be qualified only as part of a finished package under UN Model Regulations chapter 6.1 or 6.5 for jerricans and drums. The resin contribution is primarily slow-crack resistance and impact toughness, but pass/fail depends on wall thickness distribution, handle design, flash removal, and closure interface quality. Drop tests from 1.2 m to 1.8 m at -18 °C for certain packing groups frequently produce failure at the pinch-off weld, so pinched areas must be reinforced by design rather than by relying on the resin alone.

    Compliance verification and end-use documentation

    Compliance documentation for HE1878 should be obtained from the raw material supplier and should specify the regulated formulations applicable to the specific lot. Under United States law, high-density polyethylene is addressed in 21 CFR 177.1520(c) 3.2a and 3.2b; compliance is conditioned on density limits, conditions of use, and migration testing where applicable. Under EU Regulation (EU) No 10/2011, the finished article must be evaluated for overall migration and specific migration of catalysts, co-monomers, and additives. The grade is generally considered REACH-compliant when the supplier’s Safety Data Sheet confirms registration under EC 1907/2006. RoHS 2011/65/EU compliance is typically declared for the base resin with respect to lead, cadmium, mercury, hexavalent chromium, PBB, and PBDE at a maximum concentration value of 0.1% by weight in homogeneous material, and 0.01% for cadmium. These documents do not automatically transfer to the finished article if colour masterbatches, processing aids, or recycled process regrind are introduced.

    Regulatory and test documentation checklist for HE1878 container applications
    RequirementStandard or regulationDocumentation focus
    US food contact21 CFR 177.1520(c) 3.2a/3.2bBase resin formulation and density limits
    EU food contactEU 10/2011Overall migration and specific migration testing
    REACH registrationEC 1907/2006Safety Data Sheet and registration number
    RoHS restricted substances2011/65/EUBase resin declaration of conformity
    Dangerous goods packagingUN Model Regulations 6.1/6.5Finished package drop, leakproofness, hydraulic, and stack test reports

    Compared with unimodal blow moulding HDPE of similar density and melt flow rate, HE1878 generally permits a reduction in wall thickness without sacrificing stress crack resistance because of its higher ESCR and higher notched impact strength at low temperature. Compared with high-density polyethylene grades designed for injection moulding, the melt flow rate is lower by roughly an order of magnitude, which is intentional: injection moulding grades sacrifice melt strength for spiral flow length. Compared with higher-viscosity blow moulding grades with melt flow rates near 0.3 g/10 min, HE1878 offers faster cycle times on continuous systems but slightly lower parison sag resistance. The selection trade-off is between top-load stiffness, ESCR, and die swell; no single HDPE grade maximises all three simultaneously.

    Prolonged hold-up of HE1878 at melt temperature above 240 °C increases the risk of oxidative degradation, visible as yellowing and loss of environmental stress crack resistance. The recommended melt temperature should not exceed 230 °C in normal production, and shutdown procedures should purge the material from the accumulator head to prevent stagnation in dead zones. Masterbatches used with HE1878 should be based on polyethylene carriers with melt viscosity comparable to the base resin. Polar carrier masterbatches can reduce weld-line strength and compromise ESCR. For food-contact and potable-water applications, migration-resistant pigment systems are required, and the finished container must be tested under the applicable regulation rather than relying solely on the raw-grade compliance statement.

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