| HS Code | 887753 |
| Density | 0.951 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 0.15 g/10 min |
| Tensile Modulus | 1400 MPa |
| Tensile Stress At Yield | 30 MPa |
| Tensile Strain At Yield | 9% |
| Tensile Stress At Break | 30 MPa |
| Tensile Strain At Break | 600% |
| Charpy Notched Impact Strength 23 C | 12 kJ/m² |
| Charpy Notched Impact Strength 30 C | 5 kJ/m² |
| Vicat Softening Temperature A50 | 128°C |
| Melting Temperature Dsc | 134°C |
| Crystallization Temperature Dsc | 116°C |
| Hardness Shore D | 62 |
| Environmental Stress Cracking Resistance Escr | >1000 h |
As an accredited Borealis HDPE FB1510 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Borealis HDPE FB1510 typically comes in 25 kg polyethylene bags, palletized, or 1,000 kg bulk bags for industrial shipment. |
| Container Loading (20′ FCL) | 20′ FCL loaded with Borealis HDPE FB1510, 25 kg bags, palletized, stretch-wrapped, and securely lashed for ocean transport. |
| Shipping | Borealis HDPE FB1510 is shipped as non-hazardous, solid polyethylene pellets in 25 kg moisture-resistant bags, octabins, or bulk trucks. Pallets are stretch-wrapped and labeled. Transport at ambient temperature in clean, dry vehicles. Keep dry, away from direct sunlight, heat, and ignition sources; avoid dust generation and follow local regulations. |
| Storage | Store Borealis HDPE FB1510 in original, unopened packaging within a clean, dry, well-ventilated warehouse. Protect from direct sunlight, moisture, heat, and contamination. Keep away from ignition sources and strong oxidizing agents. Maintain moderate temperatures and avoid prolonged UV exposure. Stack pallets securely to prevent package damage. Follow the manufacturer’s safety data sheet and all local storage regulations. |
| Shelf Life | Borealis HDPE FB1510 typically has a 24-month shelf life when stored dry, cool, and in unopened original packaging, away from UV light. |
Monolayer conversion of Borealis HDPE FB1510 into 10–18 µm T-shirt carrier bags begins with controlled feeding through a water-cooled grooved-feed extruder running a 30:1–36:1 L/D barrier screw and spiral Maddock mixing tip. The grade is specified at a nominal density of 0.951 g/cm³ (ISO 1183-1) and an MFR₂ of 0.10 g/10 min (ISO 1133-1:2022), placing it in the high-melt-strength HDPE blown-film envelope rather than in the lower-viscosity window used for cast film. Melt temperature at the die adapter is held between 200°C and 220°C, while the rear feed zone is maintained between 60°C and 90°C to prevent polymer plugging in grooved-feed liners with aggressive cooling. A monolayer die of 250–350 mm diameter is paired with a lip gap of 1.2–1.5 mm, and the bubble is raised in a high-stalk configuration with a blow-up ratio of 3.5:1–4.5:1. The frost line is positioned 8–10 die diameters above the air ring to orient the HDPE before solidification; at 10 µm final thickness the drawdown ratio reaches 120:1–140:1, and the bimodal molecular weight distribution of FB1510 suppresses the rhythmic bubble fluttering observed in conventional unimodal HDPE at equivalent drawdown. White-tinted carrier bags use 4–6 wt% of a 50–70% TiO₂-PE masterbatch, while slip/antiblock concentrate is added at 2–3 wt% when high-speed bag separation requires a kinetic coefficient of friction below 0.45 (ISO 8295). After extrusion, corona discharge raises surface polarity to 40–44 mN/m, flexographic inks are applied, and bottom-seal welding is performed at jaw temperatures of 145–165°C. Food-contact versions are reviewed under EU 10/2011 overall migration below 10 mg/dm² and FDA 21 CFR 177.1520; non-food versions fall under REACH 1907/2006 Article 33 and the heavy-metal constraint of 94/62/EC. The principal converting failure mode above 250 m/min is die-lip oxidation producing gel specks unless screen packs of 20/40/80 mesh are used and lip purge is maintained during line stops.
For heavy-duty industrial liner production, FB1510 is not normally processed as a 100% HDPE monolayer at 40–70 µm because a fully HDPE web raises bending stiffness to a level that transmits concentrated tearing force along fold creases instead of absorbing it through local deformation. FB1510 is therefore dosed into LLDPE-rich formulations at 30–50 wt% to increase modulus and stacking stiffness while retaining the elongation required under waste collection puncture. A representative 50 µm liner formulation contains 45 wt% FB1510, 45 wt% butene-based LLDPE, and 10 wt% carbon black masterbatch, with the HDPE fraction processed through a 30:1 grooved-feed extruder at melt temperatures of 210–230°C. Tooling for this segment uses a 300–400 mm die, lip gap of 1.6–2.0 mm, blow-up ratio of 3.0:1–4.0:1, and a low-stalk bubble configuration to preserve machine-direction tear strength under haul-off tension. Acceptance testing is anchored to ISO 527-3 for film tensile properties, ISO 6383-2 for Elmendorf tear, and ASTM D1709 method B for dart impact. Procurement specifications for 50 µm waste collection liners commonly set a dart drop threshold above 80 g and MD tear above 1.5 N; however, published FB1510-specific comparative data for these thresholds is limited, and line qualification should generate capability data before a purchaser locks the blend ratio. Above 50 wt% FB1510, MD tear and slow puncture resistance deteriorate rapidly on thin webs, and the edge-fold welding window narrows to 155–175°C. The terminal products in this segment are construction debris bags, compacted waste sacks, and industrial parts liners, where the HDPE share raises stacking rigidity and reduces film stretch under load. Chemical compliance is governed by REACH 1907/2006, with combined heavy metals limited to 100 mg/kg under 94/62/EC; food-contact claims are generally not required unless the liner enters a packaged-food waste stream with specific hygiene protocols.
In frozen-food packaging, FB1510 is placed in the outer or core layer of a coextruded three-layer web rather than in the sealant layer because HDPE seal initiation temperature runs approximately 10–15°C higher than a low-medium density polyethylene or EVA sealant. A common structure for frozen vegetable and seafood packs is a 20–40 µm film with an outer layer containing 35 wt% FB1510 and 65 wt% LLDPE, a core of post-industrial regrind, and a sealant layer of low-viscosity LLDPE or EVA. The HDPE-bearing outer layer increases case rigidity and reduces package spring-back during frozen storage between −25°C and −18°C, but the layer ratio must remain below 40% of total film thickness to avoid flex-crack initiation at fold points. Three-layer lines for this segment use die diameters of 200–400 mm, lip gaps of 1.2–1.5 mm, blow-up ratios of 2.5:1–3.5:1, and melt temperatures of 200–220°C for the HDPE-bearing layer. After conditioning at −20°C, the film is tested for dart impact or slow puncture; procurement specifications often adapt ASTM D1709 and EN 14477 for this purpose, although published test data for FB1510-specific frozen-film constructions is not extensive. Seal integrity is validated at 120–135°C jaw temperatures on vertical form-fill-seal machines running 40–80 packages per minute, and the HDPE layer reduces upright bag display spring-back. Compliance is anchored to EU 10/2011 overall migration below 10 mg/dm² and to FDA 21 CFR 177.1520 for the olefin polymeric fraction. The operational boundary is the low-temperature brittleness of HDPE-rich layers: exceeding 40% HDPE content in the outer web leads to shatter failure when bags are dropped onto hard frozen surfaces, especially at film gauges below 25 µm.
Agricultural silage cover production uses FB1510 as a high-yield stiffening fraction in wide-width blown-film lines running 80–150 µm finished thickness. A workable silage cover formulation contains 70 wt% FB1510, 20 wt% LLDPE, and 8–10 wt% UV-stabilized masterbatch; carbon black is added at 2–4 wt% when black cover film is specified for long-term clamp exposure. The die diameter is typically 400–600 mm with a lip gap of 2.0–2.4 mm, blow-up ratio of 3.0:1–4.0:1, and melt temperature of 210–225°C; the wide web is edge-gusseted or centre-slit to produce 6–12 m cover sheets. Wind-up tension is held between 40 N/m and 80 N/m to prevent corrugation wrinkles. Because agricultural films must resist wind and mechanical abrasion, tensile modulus and puncture resistance are specified under EN 13206 for thermoplastic covering films used in agriculture, and residual heavy-metal content is controlled to the same 94/62/EC packaging limits in many national agricultural film collection schemes. The high HDPE fraction lowers film elongation relative to pure LLDPE silage sheeting, so prestretching during cover placement is limited to 10–15% before the film hardens and tears along the clamp edge. End products include clamp covers, round-bale overwrap, and temporary silo pit liners. The primary processing constraint is UV masterbatch dispersion: below 210°C melt temperature, agglomerates can form in the lip gap, producing local thin spots that fail during extended outdoor UV exposure.
FB1510 is converted into 12–20 µm blown base webs for adhesive or extrusion lamination in dry-food pouches where the HDPE layer contributes cut-stiffness, print-holdout, and down-gauging capability. The film is produced on automatic profile-controlled blown-film lines with die diameters of 250–350 mm, die gaps of 1.2–1.5 mm, blow-up ratio of 3.0:1–4.0:1, and melt temperatures of 200–220°C. Thickness variation across the web is held to ±0.5 µm at 15 µm using segmented air-ring control, and the film is corona-treated to 42–46 mN/m before flexographic or gravure printing. In a dry-food laminate, the FB1510 web is bonded to a sealant film with a solventless two-component polyurethane adhesive applied at coat weights of 1.8–2.5 g/m²; the laminate is then cured for 24–48 h at 35°C. The HDPE layer remains outside the seal and is selected for stiffness rather than barrier, since its moisture vapour transmission rate is not low enough for highly moisture-sensitive products without an additional barrier coating. The laminate is tested for bond strength using ASTM F904, and the printed base web is tested for tensile properties under ISO 527-3. Food-contact compliance requires the HDPE layer and the total construction to satisfy EU 10/2011 overall migration below 10 mg/dm² under worst-case time-temperature conditions; the olefin fraction additionally references FDA 21 CFR 177.1520 when exporting to North American dry-food converters. The relevant operational boundary is flex-crack sensitivity at 12 µm: repeated transport abrasion can generate pinholes at fold lines unless the laminate is structured with at least 20 µm total thickness and the HDPE layer is not creased under high tension during slitting.
| Standard or regulation | Cited clause or method | Operational boundary |
|---|---|---|
| EU 10/2011 | Article 3 and Annexes I–V | Overall migration below 10 mg/dm² for food-contact films |
| FDA 21 CFR 177.1520 | Olefin polymers | Direct food contact under specified conditions of use |
| REACH 1907/2006 | Article 33 | SVHC communication at concentration above 0.1 wt% |
| 94/62/EC | Article 11 | Combined lead, cadmium, mercury and hexavalent chromium below 100 mg/kg |
| EN 13206 | Agricultural covering film provisions | Mechanical and UV performance for silage covers |
| ISO 527-3 | Test method designation | Tensile modulus and elongation of film |
| ISO 6383-2 | Test method designation | Trouser tear of plastic film |
| ASTM D1709 | Method B | Free-falling dart impact of film |
E-commerce mailer production has adopted coextruded white-coloured outer webs containing FB1510 at 20–40 wt% to improve puncture resistance and support downgauging from 80 µm to 50–60 µm. The mailer structure is typically a three-layer blown film with an outer HDPE-containing layer, a recycled LLDPE or PCR core, and a sealant layer processed at melt temperatures of 205–220°C. Blown-film lines for this segment run die diameters up to 500 mm, die gaps of 1.6–2.0 mm, blow-up ratio of 2.5:1–3.5:1, and automatic gauge control maintaining ±1.0 µm thickness variation. FB1510 raises outer-surface scratch resistance and torsional rigidity, but the HDPE-bearing layer must not exceed 40% of total thickness because higher levels create edge cracking during folded mailer packing. The finished mailer is tested for Elmendorf tear under ISO 6383-2, dart impact under ASTM D1709, and seal strength under ASTM F88. Regulatory alignment for courier bags is primarily REACH 1907/2006 and 94/62/EC, with the sum of lead, cadmium, mercury and hexavalent chromium limited to 100 mg/kg. Published data for FB1510-specific mailer formulations is limited, and production qualification therefore requires a pilot film line trial with at least 500 kg of the compound to verify outer-layer dispersion and long-run bubble stability.
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Borealis HDPE FB1510 is a bimodal high density polyethylene film resin produced in the Borstar loop-gas phase cascade. The nominal density is 951 kg/m³ per ISO 1183-1, and the melt flow rate is 0.10 g/10 min at 190 °C under 2.16 kg load per ISO 1133-1. The low molecular weight fraction controls high-shear extruder flow and surface finish, while the high molecular weight fraction with controlled short-chain branching raises melt strength, dart impact, and environmental stress crack resistance. The resin is supplied as a natural pellet stabilised with a phenolic-phosphite antioxidant package. It is intended for monolayer and coextruded blown film from 15 µm to 60 µm. It is not formulated for injection moulding, rotomoulding, or sheet extrusion because the low melt flow rate generates excessive back pressure and melt distribution defects.
The melting peak determined by differential scanning calorimetry per ISO 11357-3 is typically 133 °C, with crystallisation onset near 118 °C at a cooling rate of 10 K/min. The Vicat softening point measured per ISO 306/A50 is near 127 °C. These thermal values place FB1510 above MDPE sealant grades and below many high-density blow moulding grades, matching its intended function as a stiff, high-barrier blown film layer rather than a low-temperature sealant. The bulk density of the pellet is approximately 540 kg/m³; pellet size and fines are controlled to reduce streamer formation in silo conveying.
Compared with an LLDPE blown film grade of density 918-925 kg/m³, FB1510 provides higher tensile modulus and lower elongation at break but lower dart impact for a given thickness. Compared with an MDPE grade of density 930-935 kg/m³, it has lower environmental stress crack resistance but higher stiffness and lower water vapour transmission. These differences limit FB1510 to stiffness- and barrier-dominated blown film applications; it is not a universal replacement for LLDPE stretch film or MDPE heavy-duty sacks. In blow moulding grades of similar density, the melt flow rate is typically 0.20-0.35 g/10 min; FB1510 is below that range and is unsuitable for normal blow moulding clamp-speed requirements.
The principal difference is the shape of the molecular weight distribution. A unimodal HDPE with density near 951 kg/m³ and MFR below 0.2 g/10 min retains high viscosity across all molecular weights; this can require die gaps of 1.8 mm to 2.2 mm to avoid sharkskin and can limit bubble stability at high frost line heights. In FB1510, the low molecular weight fraction lowers viscosity at shear rates above 100 s⁻¹, while the high molecular weight fraction maintains low-shear viscosity and melt tension. The result is processing through die gaps of 1.2 mm to 1.8 mm and stable operation at blow-up ratios from 2.5:1 to 4:1. At equal density and thickness, the bimodal comonomer distribution places tie chains and short-chain branches in the high molecular weight fraction, improving dart impact and stress crack resistance without the stiffness penalty that would accompany a density reduction.
The trade-off is back pressure. Because the melt flow rate is 0.10 g/10 min, extruders with shallow-channel barrier screws may reach excessive melt temperature before target output. Grooved-feed extruders with L/D ratios of 28:1 or 30:1 are preferred. Melt pump systems should be sized for the low shear viscosity of the resin; undersized melt pumps can cavitate at high screw speed and produce output surging.
Dynamic shear rheology at 190 °C shows a broad relaxation spectrum with a long high molecular weight tail; the storage modulus at low frequency is higher than for a unimodal HDPE of equivalent density and MFR. The crossover frequency at which storage and loss moduli intersect shifts to lower frequency, a rheological signature of the high molecular weight fraction that correlates with bubble stability and melt tension. This combination allows the resin to hold a stable bubble at high frost lines but also requires sufficient torque capacity during screw start-up.
On a grooved-feed blown film line with screw L/D of 30:1 or higher, barrel temperatures are typically profiled from 180 °C in the feed zone to 210 °C in the metering and die zones. Melt temperature at the die should be held between 210 °C and 225 °C; excursions above 240 °C accelerate oxidative gel formation and can produce odour in thin films. A die gap between 1.2 mm and 1.8 mm is required. Below 1.0 mm, shear stress at the die lip can exceed the critical melt fracture threshold and produce surface roughness. The blow-up ratio is set from 2.5:1 to 4:1, and the frost line is placed at 8 to 12 die diameters from the air ring. At blow-up ratios below 2:1, unbalanced orientation reduces dart impact; above 4:1, transverse direction tear increases but machine direction modulus declines. During start-up, purging with a 0.5-1.0 g/10 min LDPE or MDPE is advisable to reduce screw torque before introducing FB1510.
The high molecular weight fraction is sensitive to frost line height and cooling uniformity. On a 90 mm blown film line with external air ring, a frost line variation of more than two die diameters across the bubble circumference has been documented to produce gauge variation and film blocking in slit-seal applications. Alignment of the air ring and tower air flow should be checked before adjusting the frost line. Moisture on pellet surfaces after transfer from cold outdoor silos into a warm production hall is a field failure mode; condensation on the pellet surface can exceed the feed-throat dew point and cause bubble defects. Sealed storage in conditioned silos does not require pre-drying, but surface condensation must be managed before the resin reaches the feed hopper.
In 25 µm monolayer film produced at 2.5:1 blow-up ratio and 10 die diameters frost line height, tensile modulus in the machine direction is approximately 850 MPa and in transverse direction approximately 950 MPa per ISO 527-3 at 23 °C and 50% RH. Dart impact resistance per ISO 7765-1 method A generally falls between 120 g and 180 g for 25 µm film, depending on line speed and cooling uniformity. Published data for exact Elmendorf tear and puncture resistance of FB1510 film below 20 µm is limited; these values should be confirmed on the production line because frost line and blow-up ratio dominate orientation.
The antioxidant package is designed to provide an oxidation induction time at 200 °C of at least 20 min under oxygen per ISO 11357-6 as a thermal stabilisation control value. Repeated high-temperature recycling or long residence times above 240 °C deplete the phenolic stabiliser and increase gel counts. Regrind addition should be limited to 15% of the layer weight unless validated on the specific line.
Because the density of FB1510 is higher than MDPE at 930-935 kg/m³, replacement raises film stiffness and lowers water vapour transmission at equal thickness. Seal bar temperatures on high-speed vertical form-fill-seal lines should be raised by 5 °C to 10 °C compared with MDPE sealant grades because the melting peak of FB1510 is near 133 °C. At a 25 µm monolayer film, water vapour transmission rate measured per ISO 15106-3 at 38 °C and 90% RH typically falls between 2.5 g/m²·24 h and 3.5 g/m²·24 h; the exact value depends on blow-up ratio, frost line height, and thickness profile. In a three-layer cereal liner, the resin is typically used as the stiff outer layer with an EVA or metallocene LLDPE seal layer. This structure gives a low seal initiation temperature from the sealant and stiffness and moisture barrier from the HDPE layer.
For unsupported lamination to BOPP or PET, the HDPE surface is corona treated to 42-48 mN/m wetting tension before solventless polyurethane adhesive application. Without this treatment, peel adhesion is insufficient because the high molecular weight fraction produces a low surface energy, non-polar surface.
In coextruded films with EVOH or nylon, the HDPE layer functions as a moisture barrier and inexpensive bulk layer. The oxygen barrier of EVOH is degraded by moisture ingress; the FB1510 layer reduces water vapour transmission to the EVOH layer, delaying barrier loss. In dry food packaging, the moisture vapour transmission rate of the HDPE layer is governed by density and crystal structure, not by the bimodal distribution alone. At 20 µm, a monolayer film typically shows water vapour transmission rate near 5 g/m²·24 h at 23 °C and 85% RH; this is an approximate value that must be verified because frost line height and draw-down affect crystal orientation.
The resin is not compatible with direct contact amine-based purge compounds or acidic flame treatments that deactivate the phenolic antioxidant package; such combinations shorten oxygen induction time at elevated temperature. In multilayer lines, purge with LLDPE or MDPE before shutdown. For long campaigns exceeding 225 °C, nitrogen blanket and hopper ventilation are required. At thickness below 12 µm, bubble stability is line-dependent; published data for this specific configuration is limited, and line trials are required to establish the gauge profile.
| Framework | Relevant provision | Operational boundary |
|---|---|---|
| US FDA | 21 CFR 177.1520(c) | Olefin polymer permitted for food contact; final article compliance is required under conditions of use. |
| European Union | Regulation (EU) 10/2011 | Overall migration limit 10 mg/dm² or 60 mg/kg; verification in final food simulant is mandatory. |
| REACH | Regulation (EC) No 1907/2006 | No intentionally added SVHC above 0.1% w/w. |
| RoHS | Directive 2011/65/EU | Pb, Hg, Cr VI, PBB, PBDE each below 0.1% w/w; Cd below 0.01% w/w. |
| Packaging waste | Directive 94/62/EC | No intentional heavy metals; inert polymer matrix. |
In a hinge-lid cereal box liner produced on a 3-layer blown film line, the HDPE layer is typically placed at the outside with a metallocene LLDPE seal layer and an EVA tie layer. The HDPE layer may be 40% to 60% of the total structure, providing enough stiffness to reduce total film thickness while keeping the seal initiation temperature low. If the HDPE layer exceeds 60% of total thickness, seal strength shifts upward in temperature and may require increased dwell time on high-speed sealing jaws. This is the final application boundary relevant to dry food packaging.