| HS Code | 581333 |
| Density | 0.955 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 0.35 g/10 min |
| Melt Flow Rate 190 C 5 Kg | 1.2 g/10 min |
| Melt Flow Rate 190 C 21 6 Kg | 25 g/10 min |
| Tensile Modulus | 1200 MPa |
| Tensile Stress At Yield | 28 MPa |
| Tensile Strain At Yield | 9% |
| Tensile Strain At Break | >600% |
| Flexural Modulus | 1200 MPa |
| Charpy Notched Impact Strength 23 C | 15 kJ/m² |
| Charpy Notched Impact Strength 30 C | 6 kJ/m² |
| Vicat Softening Temperature A | 128°C |
| Vicat Softening Temperature B | 76°C |
| Melting Temperature | 133°C |
| Crystallization Temperature | 115°C |
| Environmental Stress Crack Resistance | >1000 h |
| Water Absorption | <0.01% |
| Volume Resistivity | >10^15 Ω·cm |
| Surface Resistivity | >10^14 Ω |
| Dielectric Constant | 2.3 |
| Dissipation Factor | 0.0002 |
| Thermal Conductivity | 0.4 W/mK |
| Specific Heat Capacity | 1900 J/kgK |
| Coefficient Of Linear Thermal Expansion | 1.5E-4 /°C |
| Shore D Hardness | 62 |
| Ball Indentation Hardness | 50 MPa |
| Brittleness Temperature | < -70°C |
| Oxidative Induction Time | >20 min |
As an accredited Borealis HDPE HE1355 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Borealis HDPE HE1355 is supplied in 25 kg polyethylene bags, stacked on pallets, or 1,000 kg octabins for bulk handling. |
| Container Loading (20′ FCL) | Borealis HDPE HE1355 20′ FCL loading: 25 kg bags, approximately 18–20 metric tons per container, subject to carrier weight limits. |
| Shipping | Borealis HDPE HE1355 is shipped as non-hazardous solid polymer pellets, typically in 25 kg bags, big bags, or bulk containers. Transport in clean, dry vehicles; protect from moisture, contamination, direct sunlight, and excessive heat. No special dangerous-goods classification required under normal conditions. Store in original packaging, keep sealed; handle with standard industrial hygiene. |
| Storage | Store Borealis HDPE HE1355 in a cool, dry, well-ventilated indoor area in original, sealed packaging. Keep away from direct sunlight, heat, flames, and strong oxidizers. Protect from moisture, contamination, and UV degradation. Maintain clean handling to prevent dust and static buildup. Use first-in, first-out stock rotation and keep containers closed when not in use. Follow local regulations and SDS guidance. |
| Shelf Life | Borealis HDPE HE1355 shelf life: 12 months when stored in original, unopened packaging, dry, cool, and protected from direct sunlight and heat. |
Borealis HE1355 is a high-density polyethylene injection moulding grade with a melt flow rate of 5.5 g/10 min at 190 °C under 2.16 kg load measured to ISO 1133-1:2022, a density of 0.958 g/cm³ measured to ISO 1183-1:2019, a tensile yield stress of approximately 27 MPa measured to ISO 527-2:2012, and a flexural modulus of approximately 1200 MPa measured to ISO 178:2019. In beverage closure production, the grade is processed on high-cavitation moulds of 16 to 48 cavities, with barrel temperatures ramped from 180 °C in the feed zone to 210–220 °C at the nozzle, and hot runner temperatures held between 210 °C and 230 °C. The closing ring and tamper-evident band require consistent melt cushion control; screw retraction after hold should not exceed 2 mm to avoid gate freeze-off at the hot-tip or tunnel gate. Injection speeds of 120–180 mm/s are typical for 1.8–2.5 g caps, with holding pressure between 35 MPa and 50 MPa hydraulic and back pressure at 5–10 bar. Mould temperature is maintained at 10–30 °C to reduce cycle time, but mould surfaces below 10 °C can create condensation and surface splay in high-humidity plants. Cycle times on 32-cavity closure lines fall between 4 s and 7 s, depending on cap mass and cooling channel layout. For still water and non-carbonated beverage caps, 100 wt% HE1355 is used without added impact modifier. For carbonated soft drink closures, a blend of 80–90 wt% HE1355 with 10–20 wt% hexene-based LLDPE is sometimes introduced to improve hinge integrity and stress cracking resistance at the knurl, at the cost of a flexural modulus reduction of roughly 10–15% relative to the neat grade; the exact reduction is grade-dependent and published data for this specific configuration is limited. Slip and antiblock masterbatches, when specified, are typically added at 1–2 wt% and must be selected from FDA-compliant carriers. The terminal components are 29/25 mm and 30/25 mm HDPE beverage closures, sports drink caps, and tamper-evident bands. Regulatory compliance for food-contact use is covered by EU Regulation (EU) No 10/2011 overall migration limits and FDA 21 CFR 177.1520(c) for olefin polymers.
In thin-wall dairy cup and margarine tub production, HE1355 is injected at melt temperatures of 220–240 °C with injection speeds from 150 mm/s to 250 mm/s. The mould temperature is set between 15 °C and 30 °C to balance part release and label adhesion in in-mould labelling cells. At a nominal wall thickness of 0.8 mm, the flow length to wall thickness ratio reachable in production tooling is generally in the order of 150:1 to 200:1, depending on gate geometry, runner diameter, and melt temperature; for 200 ml cups with a flow path of 120–150 mm, this corresponds to a fill pressure of 90–120 MPa at the injection unit. Holding pressure is staged from 50 MPa for 0.5 s to 30 MPa for 1.5 s, then released before the gate seal time to prevent sink marks at thicker rim sections. Cycle times of 4–6 s are achievable on 8-cavity in-mould labelling cup lines with ejector stroke capacities above 100 mm. The narrow molecular weight distribution and MFR of 5.5 g/10 min keep the melt viscosity sufficiently low for high-speed filling, but shear heating under 250 mm/s injection speed should be monitored; melt temperatures above 260 °C can cause odour and a visible surface haze in translucent cups. Each cavity is typically equipped with a hot runner valve gate; gate diameters of 0.8–1.2 mm are used to limit gate vestige. The terminal parts are 125 g margarine tubs, 200–500 ml dairy cups, and thin lids for spreading fats. Food-contact compliance includes EU Regulation (EU) No 10/2011 with an overall migration limit of 10 mg/dm², tested under EN 1186-1:2002 and EN 1186-3:2002 for aqueous simulants, and FDA 21 CFR 177.1520 for use conditions A through H.
| Application segment | Melt temperature (°C) | Mould temperature (°C) | Injection speed (mm/s) | Holding pressure (MPa) | Typical cycle time (s) |
|---|---|---|---|---|---|
| Beverage closures | 180–230 | 10–30 | 120–180 | 35–50 | 4–7 |
| Thin-wall dairy cups | 220–240 | 15–30 | 150–250 | 30–50 | 4–6 |
| Industrial pails and crates | 200–230 | 15–25 | 50–100 | 40–60 | 15–25 |
| Personal care closures | 190–210 | 10–20 | 60–120 | 60–90 | 8–12 |
For returnable crates, pails, and pallets, HE1355 is dry-blended at the hopper with a HALS-based UV stabilizer masterbatch at 1.5–2.5 wt% and, in black outdoor grades, with a 40% carbon black masterbatch at 2–3 wt%. The melt temperature is held at 200–230 °C, and mould temperature is set to 15–25 °C to control warpage in deep-draw geometries. Injection moulding machines for 20 L pails require clamp forces in the range 5000–8000 kN, with shot sizes adjusted to deliver 700–1100 g per pail depending on wall thickness and lid seat design. Holding pressure is maintained at 40–60 MPa for 4–8 s to pack the thick corner sections, followed by cooling times of 15–25 s for pails with nominal wall thickness of 1.8–3.5 mm. Crates and pallets use lower holding pressures and longer cooling due to ribbed structures; sink marks are controlled by rib-to-wall ratios below 0.6:1 and by gas counterpressure where available. Mechanical acceptance is based on Charpy notched impact testing according to ISO 179-1:2010 at 23 °C and, for cold-chain use, at -30 °C; environmental stress cracking resistance is assessed under ASTM D1693 condition A in 10% Igepal CO-630 at 50 °C. Published data for HE1355-specific ESCR at high wall thickness is limited, but HDPE injection grades with 0.958 g/cm³ density typically fail below 30 h if contaminated with low-molecular-weight process aids; therefore no external lubricants are used in this segment. For detergent and agrochemical pails, the finished container is qualified under UN dangerous goods packaging performance tests applicable to 1H2 plastics boxes and jerricans, including drop tests and stack load tests. The terminal products are returnable transit crates, 20 L detergent pails, pallet boxes, and outdoor storage bins.
In food packaging, the grade is not treated as a single compliance point; the complete formulation, including colour masterbatch, slip additives, and nucleating agents, falls under the same migration testing scope. Under EU Regulation (EU) No 10/2011, high-density polyethylene used as a food-contact polymer is subject to an overall migration limit of 10 mg/dm² for all food simulants, with the test performed according to EN 1186-1:2002 and EN 1186-3:2002 for aqueous, alcoholic, and acidic food simulants. For dairy tubs operating with fat-containing foods, the relevant simulant is D1 (50% v/v ethanol) or D2 vegetable oil, depending on the intended use; the latter requires replicate extraction because polyolefin absorption of oil can complicate mass-balance calculations. The specific migration of additives is evaluated only if the additive has a specific migration limit listed in Annex II; the base HDPE polymer itself is exempt from specific migration limits, but residual catalyst components such as titanium and aluminium are controlled in the material specification. For export to the United States, FDA 21 CFR 177.1520(c) applies to olefin polymers; this citation covers high-density polyethylene for food contact but does not automatically cover colour concentrates, which must be evaluated independently under 21 CFR 178.3297 or an applicable food additive petition. Processing at melt temperatures above 220 °C does not require pre-drying at relative humidity below 60%, but condensation can increase moisture in the hopper; HDPE is non-hygroscopic, so pre-drying is not used unless the material has been stored in damp conditions or regrind carries surface moisture. Regrind addition up to 20 wt% is common in dairy tub production, but the material must be infrared-sorted or full-colour-stable to avoid black specks. Terminal products are single-use dairy cups, margarine tubs, and lids that require sensory neutrality tested by DIN 10955-1:2004 or an equivalent taste and odour panel method.
| Application segment | Regulatory framework | Test method | Critical limit |
|---|---|---|---|
| Beverage closures | EU 10/2011 | EN 1186-3:2002 | Overall migration 10 mg/dm² |
| Thin-wall dairy cups | FDA 21 CFR 177.1520 | EN 1186-1:2002 | Overall migration 10 mg/dm² |
| Industrial pails | UN dangerous goods packaging tests | Stack and drop tests | Packaging group II performance |
| Personal care closures | USP <661.1> | Extractables testing | Defined extractables profile |
| Consumer storage | RoHS Directive 2011/65/EU | XRF screening | Pb, Cd, Hg, Cr(VI), PBB, PBDE limits |
In non-food injection moulding, HE1355 is processed without a pre-drying step unless the regrind fraction exceeds 30 wt% and has been stored in unlined containers. Melt temperature for houseware boxes and appliance housings is set at 210–230 °C, with the mould at 20–35 °C to reduce surface stress whitening at ribs and bosses. Injection speeds are moderate, 80–150 mm/s, to prevent jetting in flat-panel geometries with wall thickness between 1.2 mm and 2.5 mm. For rigid storage boxes, 100 wt% HE1355 is typical; for cost-reduction programmes, 20–30 wt% post-consumer recycled HDPE is blended at the machine hopper, but this reduces tensile yield stress by 5–12% depending on the recycled stream and increases lot-to-lot variability in Charpy impact by up to 15%. The material is not recommended for thin-wall live hinges where repeated flexing exceeds 10,000 cycles without modification; if hinge performance is required, the hinge should be redesigned with a minimum thickness of 0.3–0.5 mm and gated perpendicular to the hinge line. Compliance for this segment is governed by REACH Article 33 SVHC communication requirements, RoHS Directive 2011/65/EU Annex II restriction limits for lead, cadmium, mercury, hexavalent chromium, PBB, and PBDE, and, for toy-adjacent storage articles, EN 71-3:2019 migration limits for nineteen elements. Terminal products include stackable storage boxes, appliance housings, and small furniture components.
For flip-top and push-pull closures used in personal care and pharmaceutical packaging, HE1355 is moulded at a lower melt temperature of 190–210 °C to suppress formation of low-odour degradation products, because the closure is in direct or indirect contact with lipid-based formulations that can sorb volatile species. Mould temperature is kept at 10–20 °C to freeze the hinge surface quickly and improve cycle time; internal threads are formed by unscrewing cores or collapsible cores, with a valve gate located at the top centre of the closure. The grade is used at 100 wt% in this segment; external lubricants and amide-based slip additives are excluded unless they are supported by extraction data, because amide migration can exceed the sensory threshold in cosmetic emulsions and oral pharmaceutical solutions. Additive masterbatches are restricted to 1 wt% maximum and must be tested for USP <661.1> plastic packaging extractables and Ph. Eur. 3.1.3 polyolefin requirements where relevant. Injection pressure is set between 60 MPa and 90 MPa, with holding time of 1–2 s for closures weighing 1.5–3.5 g. Cycle time on 24-cavity unscrewing tools is 8–12 s, extended by the unscrewing sequence rather than cooling. Terminal components are shampoo flip-top caps, pump overcaps for lotion bottles, and pharmaceutical bottle closures requiring child-resistant features. Regulatory submissions for pharmaceutical packaging reference ICH Q3D elemental impurity limits and USP <661.1> plastic packaging chapters, while cosmetic packaging falls under Regulation (EC) No 1223/2009 Article 17 for the safety of packaging materials in contact with cosmetic products.
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Borealis HE1355 is a high-density polyethylene resin intended for extrusion blow moulding of small- to medium-volume rigid containers. The grade is supplied as natural pellets and is characterized by a nominal density of 0.945 g/cm³ and a melt flow rate of 0.35 g/10 min at 190 °C/2.16 kg according to ISO 1183-1 and ISO 1133-1. The material is based on a bimodal molecular architecture that separates high-molecular-weight fractions for melt strength and environmental stress crack resistance from lower-molecular-weight fractions for processability. Its primary industrial application is rigid packaging for household chemicals, detergents, personal care products, and small industrial containers up to approximately 5 L.
Compared with chromium-catalyzed unimodal HDPE grades in the same density range, HE1355 differs in the shape of the molar mass distribution and the resulting balance between stiffness, ESCR, and parison stability. It is not intended for cast film, blown film, or injection moulding applications because the high molecular weight tail generates elevated melt pressure and low drawability in film processes.
At 0.945 g/cm³, HE1355 contains sufficient butene or hexene comonomer to disrupt crystallinity for environmental stress crack resistance while retaining enough linear polyethylene sequences to maintain top-load strength. Table 1 reports the standard specification set used for incoming inspection and industrial release.
| Property | Test method | Typical value |
|---|---|---|
| Density | ISO 1183-1 | 0.945 g/cm³ |
| Melt flow rate (190 °C/2.16 kg) | ISO 1133-1 | 0.35 g/10 min |
| Tensile modulus (1 mm/min) | ISO 527-2 | 1000 MPa |
| Tensile stress at yield | ISO 527-2 | 25 MPa |
| Elongation at break | ISO 527-2 | >600 % |
| Environmental stress crack resistance (100 % Igepal, F50) | ASTM D1693-15 | >300 h |
| Vicat softening temperature (A50) | ISO 306 | 127 °C |
| Shore D hardness | ISO 868 | 62 |
For intermittent blow moulding on shuttle machines with grooved-barrel extruders of 60–80 mm screw diameter and L/D 24–30, the recommended melt temperature window is 180–210 °C. Barrel temperatures are usually profiled from 170 °C in the feed zone to 195 °C at the die head. Pre-drying is not routinely required because the resin has negligible hygroscopic uptake; however, surface condensation on pellets stored below 10 °C or at relative humidity above 60 % should be removed with hopper air at 60–70 °C for 1–2 h before processing.
The bimodal molar mass distribution reduces die swell relative to broad unimodal resins at equivalent die gap settings, but the low melt flow rate requires sufficient head pressure to avoid unmelts. Parison sag on a 300 mm parison length is typically controlled by adjusting extrusion speed rather than melt temperature, because excess temperature depresses melt strength and increases the risk of wall-thickness variation.
The grade’s high-molecular-weight tail provides the extensional viscosity required to hold a parison during mould transfer. Capillary rheometry at 190 °C shows a shear-thinning response consistent with the broad molar mass distribution; quantitative power-law constants for this grade are not specified on the standard datasheet and should be measured on production extruders. Because the resin is formulated for blow moulding, extensional hardening is more pronounced than in injection moulding grades with equivalent melt flow rate.
Containers blow moulded from HE1355 are evaluated by top-load compression testing according to ASTM D2659 or DIN 55440, drop-impact testing at −20 °C, and ESCR screening in 10 % Igepal CO-630 at 50 °C per ASTM D1693-15. For a 1 L detergent bottle with nominal wall thickness 0.7 mm, top-load strength typically exceeds 300 N when the bottle design minimises pinch-off discontinuities. Published data for this specific geometry is limited; the value should be verified on production tooling.
In multi-layer packaging structures, HE1355 is used as the structural layer adjacent to barrier layers of polyamide or ethylene vinyl alcohol. Regression of the barrier layer due to moisture accumulation is reduced because the HDPE layer provides stiffness and limits creep under top load. The pinch-off region remains the critical failure site under drop impact, and tool maintenance and die temperature profiling affect performance more than minor shifts in melt flow rate.
Tooling changes are generally not required if the replacement grade has similar density and MFR. The most significant adjustment is a reduction in die-head temperature of 5–10 °C because the bimodal resin develops a lower extrudate swell at equivalent wall shear stress. Operators may observe a narrower processing window for parison curvature on asymmetric bottle shapes; this should be compensated by moving the die gap or adjusting the accumulator programme rather than increasing melt temperature. Compared with a unimodal grade of 0.945 g/cm³ and MFR 0.30–0.40 g/10 min, HE1355 typically shows longer spiral-flow length at equal pressure and improved ESCR retention after regrind addition at 20–30 %.
The higher molecular weight tail also reduces melt fracture in heavy-wall applications, but it may increase extruder amperage by 5–10 % on screw designs with shallow barrier sections. For grooved-barrel machines, barrel temperature profiles should be kept below 210 °C to prevent degradation of the stabilizer package and generation of off-odour in the finished container.
Regulatory compliance depends on the specific masterbatch, regrind, and processing aid used in the finished article. The base resin can be supplied with compliance to FDA 21 CFR 177.1520 for olefin polymers, Commission Regulation (EU) No 10/2011 for food contact plastics, Regulation (EC) No 1907/2006 for REACH SVHC absence, and Directive 2011/65/EU for RoHS substances. The material is not intended for implantable medical devices or for use with strong oxidizing agents; continuous exposure to fumes of nitric acid or chlorinated solvents above 40 °C may cause stress cracking.
| Requirement | Standard or regulation | Scope |
|---|---|---|
| Food contact | FDA 21 CFR 177.1520 | Olefin polymers, conditions of use |
| EU food contact | Commission Regulation (EU) No 10/2011 | Overall migration and specific migration |
| REACH | Regulation (EC) No 1907/2006 | SVHC absence |
| RoHS | Directive 2011/65/EU | Lead, mercury, cadmium, Cr(VI), PBB, PBDE |
| Additive regulations | EU 10/2011 positive list | Specific migration limits for additives |
In a 750 mL multi-layer bottle with regrind content of 25 %, processors using shuttle machines with 50 ton clamping force and 2+2 cavity moulds report stable cycle times of 8–12 s when the accumulator programme maintains a constant parison speed during transfer. Published data for this specific configuration is limited; cycle time should be confirmed on the target line.