| HS Code | 983580 |
| Melt Flow Rate 190 C 2 16 Kg | 0.2 g/10 min |
| Density | 0.938 g/cm³ |
| Tensile Strength At Yield | 23 MPa |
| Tensile Elongation At Break | >600 % |
| Flexural Modulus | 900 MPa |
| Vicat Softening Temperature | 123 °C |
| Melting Temperature | 132 °C |
| Environmental Stress Crack Resistance Escr | >1000 h |
| Hardness Shore D | 60 |
| Water Absorption | <0.01 % |
| Dielectric Constant | 2.3 |
| Volume Resistivity | >1E15 ohm-cm |
| Dielectric Strength | 20 kV/mm |
| Thermal Conductivity | 0.4 W/m·K |
| Coefficient Of Linear Thermal Expansion | 1.2E-4 /°C |
| Specific Heat | 1.9 kJ/kg·K |
As an accredited QAPCO HDPE LOTRÈNE 3802 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | QAPCO HDPE LOTRÈNE 3802 is packed in 25 kg polyethylene bags, palletized and stretch-wrapped, with 1,250 kg jumbo bags available. |
| Container Loading (20′ FCL) | 20′ FCL loading: QAPCO HDPE LOTRÈNE 3802, non-hazardous, in 25 kg bags, palletized/shrink-wrapped, approximately 22 MT net, standard dry container. |
| Shipping | QAPCO HDPE LOTRÈNE 3802 ships as non-hazardous solid polyethylene pellets, typically in 25 kg bags, jumbo bags, or bulk liners. It is not classified as dangerous goods. Store in a cool, dry, ventilated area, away from sunlight, moisture, and contamination. Use standard handling and transport equipment. |
| Storage | Store QAPCO HDPE LOTRÈNE 3802 in a cool, dry, well-ventilated warehouse, in original closed bags or containers. Palletize and keep off the floor. Protect from direct sunlight, moisture, heat, and ignition sources. Avoid contact with strong oxidizers, acids, and contaminants. Keep away from incompatible materials. Use first-in/first-out rotation, good housekeeping, appropriate PPE, and follow the manufacturer’s SDS and local regulations. |
| Shelf Life | Store in a cool, dry, well-ventilated area; shelf life is typically 24 months in original, unopened packaging away from sunlight. |
In monolayer dairy and beverage bottle production, LOTRENE 3802 is typically run on long-stroke shuttle blow moulding machines with 65–80 mm grooved-feed extruders at an L/D ratio of 24:1 to 30:1. Barrel zone set points are held at 170–185 °C in the feed, 185–200 °C in the compression zone, and 200–210 °C in the metering zone, while head and die temperatures are maintained at 195–205 °C to avoid low-molecular-weight fraction breakdown. The grade is characterized by a density of 0.952 g/cm³ when tested in accordance with ISO 1183-1:2019, a melt-mass flow rate under 2.16 kg of 0.2 g/10 min, and a high-load melt-mass flow rate under 21.6 kg of 2.2 g/10 min measured at 190 °C according to ISO 1133-1:2022, producing a flow-rate ratio near 11 that controls parison hang time on multi-cavity tools. In food-contact formulations, 96.0–98.0 wt% LOTRENE 3802 is let down with 2.0–4.0 wt% titanium dioxide white masterbatch of 60 wt% typical TiO₂ content and 0.5–1.0 wt% of a food-grade processing aid only when output exceeds 120 kg/h on six-cavity or eight-cavity equipment. Compliance documentation for the finished container references FDA 21 CFR 177.1520(c) 3.2a for olefin polymers, EU Regulation (EU) No 10/2011 Annex I and Annex II migration limits, and China GB 4806.7-2016 for food-contact polyethylene. On production lines the parison is inflated at 0.6–0.9 MPa blow pressure into aluminium or beryllium-copper moulds held at 10–20 °C; wall thickness for 500 mL and 1 L milk bottles is programmed between 0.4 mm and 0.7 mm, with cycle times of 10–14 s on shuttle equipment. Finished types in this application segment include 200 mL–2 L milk bottles, 250 mL–1.5 L juice bottles, 5 L–10 L water containers, and 1 L–2 L dairy creamers, all heat-sealed with BOPP or foil induction seals. Because LOTRENE 3802 is not hygroscopic, pre-drying is unnecessary when storage is below 60 % relative humidity; regrind from edge trim and rejected bottles should be kept below 30 wt% to avoid measurable loss of environmental stress crack resistance, and any recycled content must carry food-contact compliance under the same migration framework.
Cleanroom extrusion blow moulding of LOTRENE 3802 for pharmacopoeial articles requires isolation of granulate feed from the mould clamp to reduce particulate contamination, with ISO 14644-1 Class 8 or Class 7 particle counts maintained across the forming area. The extruder is typically a 50–65 mm single-screw unit with an L/D ratio of 24:1 to 28:1, barrel temperatures of 170–195 °C in the feed and compression sections, 195–210 °C in the metering section, and 195–205 °C at the head and die; compressed air for parison inflation is filtered through 0.2 µm membrane elements to prevent oil carryover into the bottle interior. For white opaque tablet bottles the formulation is 96.0–98.0 wt% LOTRENE 3802 and 2.0–4.0 wt% pharmaceutical-grade TiO₂ masterbatch; coloured nutraceutical packs use 95.0–97.5 wt% resin and 2.5–5.0 wt% masterbatch, with every additive package accompanied by change-control documentation. Compliance and compendial testing align to Ph. Eur. monograph 3.1.3 for polyolefines, USP ⟨661.1⟩ plastic packaging components, and FDA 21 CFR 177.1520 for the US market. Downstream manufacturing includes extrusion blow moulding of round and square bottles from 30 cc to 200 cc, automatic deflashing, leak testing at 0.03–0.07 MPa differential pressure, and induction or heat-seal closure lining. For 0.5 mm wall sections, moisture vapour transmission values are typically 0.12–0.20 g/m²/day at 25 °C and 60 % RH under ASTM F1249, making desiccant canisters necessary for hygroscopic solid-dose formulations. Finished types include amber and white tablet bottles, 30–200 cc packer bottles for dry syrups, and 50–150 mL nutraceutical bottles for powders and capsules; white opaque packaging is preferred when light-sensitive actives require less than 1 % light transmission, but LOTRENE 3802 alone does not provide complete UV barrier and requires a UV-absorbing masterbatch or secondary carton for photolabile compounds. Regrind is not permitted in many pharmacopoeial applications unless validated at 10–20 wt% maximum and segregated by lot to maintain batch-to-batch identity.
Because agricultural chemical and industrial cleaning concentrates often contain nonionic surfactants, glycol ethers, chlorinated methanes and high-pH builders, stress cracking resistance rather than short-term burst strength governs the service life of blow moulded containers made from LOTRENE 3802. In this application, 97.0–99.0 wt% resin is compounded with 1.0–3.0 wt% carbon black masterbatch for UV stabilization and 0.5–1.5 wt% of an antioxidant and processing stabilizer package; when the packaged liquid contains free chlorine or hypochlorite, converters should avoid phenol-based stabilizers and validate the head-space wetted contact under ASTM D1693 Condition B in a 100 % Igepal CO-630 environment, where F50 values above 50 h are normally required for product liability sign-off. The downstream production process is continuous extrusion blow moulding of 1 L–25 L jerrycans and utility bottles on shuttle or single-head machines with 65–90 mm grooved-feed extruders, L/D ratios of 24:1 to 30:1, melt temperatures of 190–215 °C, and die heads designed for 35–50 % parison swell. Blow pressure is held at 0.6–0.8 MPa and mould temperature at 10–25 °C; handle pinch-offs require axial parison programming with 50–128 point profiles to avoid thin spots below 0.8 mm at the pinch line. Finished types include 1 L–5 L agricultural chemical bottles, 5 L–25 L industrial cleaning jerrycans, 4 L–20 L lubricant containers and 3 L–10 L laundry detergent bottles with UN 1H1 or 1H2 certification for dangerous goods when applicable, under ADR/RID/IMDG Chapter 6.1 and DOT 49 CFR for North American shipments. If multi-layer co-extrusion is required for solvent-containing formulations with benzene or toluene, LOTRENE 3802 serves as the inner and outer HDPE skin with an EVOH or polyamide barrier core at 3–6 wt% of total wall thickness; delamination at the tie layer is a known failure mode when interlayer melt temperatures differ by more than 10 °C, so co-extrusion feedblock and die temperatures are controlled to 195–205 °C.
When UN 1H1 certification is specified for 60–220 L tight-head drums, LOTRENE 3802 is processed on accumulator blow moulding machines with screw diameters of 80–100 mm, grooved-feed or smooth-feed extruders at L/D ratios of 24:1 to 30:1, and accumulator head volumes of 15–25 L. The large parison mass requires stable high zero-shear viscosity; parison sag between die exit and mould closure is controlled by melt temperature held at 190–205 °C and by 64–128 point axial wall-thickness programming that thickens the shoulder, bottom pinch-off and chime areas to compensate for draw-down. Typical drum wall thickness is 2.5–5.0 mm, blow pressure is 0.5–0.7 MPa, and mould temperature is maintained at 5–15 °C to cool thick sections. Formulation for outdoor-stored drums uses 96.0–98.0 wt% LOTRENE 3802, 2.0–4.0 wt% carbon black or grey masterbatch with UV absorber and HALS package, and 0.5–1.0 wt% processing aid; natural drums for food or pharmaceutical intermediates use 99.0–99.5 wt% resin and 0.5–1.0 wt% acid-neutralizing masterbatch. Compliance testing for dangerous goods packaging requires the drop test, stack load test at 45 °C for 28 days, and leakproofness test per ADR 6.1.5.2–6.1.5.6 and DOT 49 CFR Subpart B, with ESCR acceptance above 50 h under ASTM D1693 Condition B. Downstream equipment includes automatic deflashers, leak testers, drum flanging and bung insertion stations; closed-loop process parameters are archived by batch, screw speed and clamp force. Finished products in this segment are 60 L, 120 L, 200 L and 220 L tight-head drums for industrial chemicals, food intermediates, and UN 1H1-certified bulk liquid transport, alongside IBC inner bottles blow moulded at 10–15 kg shot weights. Operational boundaries include a minimum mould cooling time of 180–300 s for 220 L drums to prevent post-mould shrinkage and dimensional deviation, and a maximum regrind level of 15–20 wt% when drop-test performance is critical; wet granulate or outdoor storage at RH above 60 % requires pre-drying at 80 °C for 2–4 h to prevent splay at the die line.
Personal care and home care bottle production from LOTRENE 3802 emphasizes surface gloss, in-mould label adhesion, and dimensional stability for cap torque retention across distribution. The resin is processed on continuous shuttle or rotary wheel blow moulding systems with 50–65 mm extruders at L/D ratios of 24:1 to 28:1, zone temperatures of 170–195 °C in the feed and compression sections, 195–210 °C in the metering section, and 190–205 °C at the head and die. In-mould labels are inserted robotically before parison inflation; mould temperature is set at 10–18 °C and blow pressure at 0.6–0.9 MPa to press the label into the bottle wall, with a cycle time of 8–12 s typical for 200–500 mL oval and cylindrical bottles. Formulations are 95.0–98.0 wt% LOTRENE 3802 and 2.0–5.0 wt% colour masterbatch, with 0.5–1.0 wt% external lubricant or processing aid added only when surface melt fracture appears at output rates above 90 kg/h; pearlescent and high-gloss masterbatches require pigment let-down validation because oversized particles above 10 µm can produce pinholes at the label edge. Regulatory compliance for the package, not the cosmetic formulation, is evaluated under EC Regulation (EC) No 1223/2009 Article 17 for packaging safety, REACH Annex XVII restrictions, and California Proposition 65 for print ink and label adhesive components; the resin itself meets FDA 21 CFR 177.1520 when the same bottle design is used for food-adjacent cosmetic products. Finished containers include 150–750 mL shampoo bottles, 200–500 mL conditioner bottles, 250–750 mL body wash bottles, and 500–2000 mL household cleaning bottles with trigger or pump closures; neck dimensions are machined to hold torque within ±0.2 N·m over a 28-day pack-out test, and cap flatness is verified with a digital torque tester after 24 h at 45 °C. A known failure mode on high-gloss moulds is uneven cooling of the label area, which distorts label adhesion and creates bubbles; this is mitigated by mould temperature zoning and by placing cooling channels no more than 10 mm from the cavity surface in the label zone. LOTRENE 3802 is not recommended for formulations requiring high oxygen barrier or fragrance impermeability unless fluorination surface treatment is applied post-moulding; unfluorinated HDPE allows measurable fragrance loss through the wall over 12–16 weeks of shelf life.
For potable water pressure vessels and filter housings, LOTRENE 3802 is converted on accumulator blow moulding equipment where long-term hydrostatic strength and dimensional stability are evaluated alongside organoleptic migration. In these applications, 98.0–99.5 wt% LOTRENE 3802 is let down with 0.5–2.0 wt% blue or grey masterbatch and 0.5–1.0 wt% acid-neutralizing and processing stabilizer; carbon black is avoided in potable water contact unless the pigment carries independent food-contact or potable-water certification. Compliance testing follows NSF/ANSI 61 for drinking water system components, with total organic carbon migration evaluated under the specific surface-area-to-volume ratio of the finished vessel; published third-party data for LOTRENE 3802 under all NSF/ANSI 61 conditions is limited, so converters must obtain formulation-specific certification. Process machinery includes accumulator blow moulding units with 80–100 mm extruders and 5–10 kg parison heads, operating at melt temperatures of 185–200 °C, die temperatures of 185–200 °C, blow pressure of 0.5–0.8 MPa, and mould temperatures of 8–18 °C; wall thickness is held to 2.0–4.0 mm, with axial parison programming to prevent the bottom weld from thinning below 1.5 mm. Hydrostatic burst testing per ASTM D1599 is commonly specified at 1.5–2.0 times maximum working pressure, and creep rupture data under ISO 9080 establishes service life. Finished product types are 10–20 L vertical pressure tanks, 5–15 L reverse-osmosis accumulator vessels, and 2–10 L filter housings with threaded port connections. The primary operational boundary is long-term chloramine and chlorine resistance; HDPE shows acceptable resistance below 1 ppm free chlorine at ambient temperature, but repeated high-temperature sanitization above 60 °C or repeated high-dose hypochlorite exposure reduces oxidative stability, and the component should be downgauged or fitted with a liner when sanitization protocols exceed 80 °C.
| Application segment | Primary compliance reference | Test method or condition | Typical acceptance basis |
|---|---|---|---|
| Dairy and beverage monolayer bottles | FDA 21 CFR 177.1520(c) 3.2a; EU 10/2011; GB 4806.7-2016 | Overall migration and specific migration limits | Food-contact declaration |
| Pharmaceutical solid-dose containers | Ph. Eur. 3.1.3; USP ⟨661.1⟩; FDA 21 CFR 177.1520 | Compendial extraction and light transmission | Pharmacopoeial conformity |
| Agrochemical and industrial cleaning jerrycans | UN 1H1/1H2; ADR/RID/IMDG 6.1; DOT 49 CFR | Drop, stack, leakproofness; ASTM D1693-B | UN certification |
| Large-volume tight-head drums | UN 1H1; ADR 6.1.5.2–6.1.5.6; DOT 49 CFR | Drop, stack at 45 °C for 28 days, leakproofness | UN certification |
| Personal care and home care bottles | EC 1223/2009 Article 17; REACH Annex XVII; California Proposition 65 | Package safety assessment, ink and label compliance | Not harmful under normal use |
| Potable water pressure vessels | NSF/ANSI 61 | Total organic carbon migration; ASTM D1599 burst; ISO 9080 creep | Formulation-specific certification |
| Application segment | Extruder or machine type | Melt temperature range | Mould temperature | Blow pressure | Cycle or cooling window |
|---|---|---|---|---|---|
| Dairy and beverage bottles | 65–80 mm shuttle blow moulder; 24:1–30:1 L/D | 190–210 °C | 10–20 °C | 0.6–0.9 MPa | 10–14 s |
| Pharmaceutical bottles | 50–65 mm cleanroom shuttle; 24:1–28:1 L/D | 190–210 °C | 10–18 °C | 0.6–0.8 MPa | 9–13 s |
| Agrochemical and industrial jerrycans | 65–90 mm shuttle or single-head; 24:1–30:1 L/D | 190–215 °C | 10–25 °C | 0.6–0.8 MPa | 12–20 s |
| Large-volume tight-head drums | 80–100 mm accumulator; 24:1–30:1 L/D | 190–205 °C | 5–15 °C | 0.5–0.7 MPa | 180–300 s cooling |
| Personal care and home care bottles | 50–65 mm shuttle or rotary wheel; 24:1–28:1 L/D | 185–210 °C | 10–18 °C | 0.6–0.9 MPa | 8–12 s |
| Potable water pressure vessels | 80–100 mm accumulator; 5–10 kg parison head | 185–200 °C | 8–18 °C | 0.5–0.8 MPa | Wall-dependent cooling |
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QAPCO HDPE LOTRÈNE 3802 is a high-density polyethylene resin supplied by Qatar Petrochemical Company under the Lotrène grade family. The designation identifies a single grade rather than a polymer family, and the resin is delivered as cylindrical pellets. The grade is specified by a nominal density of 0.938 g/cm³ measured in accordance with ISO 1183-1, and a melt flow rate of 0.2 g/10 min measured under a 2.16 kg load at 190 °C according to ISO 1133-1. These two values place the material at the lower-density boundary of the high-density polyethylene class and indicate a medium-to-high-molecular-weight extrusion resin rather than a high-flow injection-moulding grade.
Applications for LOTRÈNE 3802 are concentrated in blown film extrusion of thin-gauge sacks, liners, and merchandise bags, with additional use in blow-moulded containers where environmental stress-crack resistance is valued. The low melt flow rate provides sufficient melt strength for stable bubble formation at commercial output rates, while the 0.938 g/cm³ density reduces stiffness relative to rigid packaging grades but improves puncture and tear balance. The product is also used in sheet extrusion when secondary thermoforming requires a combination of moisture barrier and surface hardness.
The grade is produced by a low-pressure ethylene polymerisation process; the exact reactor configuration is proprietary to QAPCO. Because the density is lower than typical blow-moulding HDPE, the product is sometimes described as a high-density film resin rather than a rigid blow-moulding resin. The distinction is functional: the lower density shifts the property profile toward toughness and sealability and away from maximum top-load strength.
The melting temperature of this class is typically observed between 126 °C and 130 °C by differential scanning calorimetry at 10 K/min. Crystallinity is lower than that of 0.960 g/cm³ HDPE due to short-chain branch incorporation, with typical crystallinity in the 55–65% range. The lower crystalline fraction contributes to reduced thermal conductivity and lower flexural modulus, while the amorphous phase improves slow crack-growth resistance. These morphology differences must be considered when downgauging from a higher-density grade.
The grade specification is anchored to ISO methods rather than to single-point declarations. Density is determined by immersion or pycnometric methods under ISO 1183-1; melt flow rate requires a dead-weight plastometer with controlled melt temperature and piston travel under ISO 1133-1. Tensile properties are obtained from type 5A specimens per ISO 527-2, and flexural modulus is measured by three-point bending per ISO 178. Thermal performance is reported as Vicat softening temperature under ISO 306/A50. Compliance with food-contact legislation for the Lotrène polyethylene family is evaluated under FDA 21 CFR 177.1520 or EU Regulation 10/2011, but the specific migration status of LOTRÈNE 3802 must be confirmed from the current QAPCO regulatory statement.
| Property | Test method | Unit | Value for LOTRÈNE 3802 or typical class range |
|---|---|---|---|
| Density | ISO 1183-1 | g/cm³ | 0.938 |
| Melt flow rate | ISO 1133-1 at 190 °C/2.16 kg | g/10 min | 0.2 |
| Tensile stress at yield | ISO 527-2 | MPa | 20–24 typical for the class |
| Tensile strain at break | ISO 527-2 | % | 500–800 typical for the class |
| Flexural modulus | ISO 178 | MPa | 700–900 typical for the class |
| Vicat softening temperature | ISO 306/A50 | °C | 121–125 typical for the class |
Published product-specific tensile and thermal values are limited beyond the density and melt flow rate shown above; the mechanical property ranges reflect the broader HDPE film-grade class and must not substitute for the certified QAPCO lot-specific values. Environmental stress-crack resistance is determined using ASTM D1693 with 10% Igepal CO-630 solution at 50 °C. HDPE grades with density below 0.940 g/cm³ generally exhibit significantly longer F₅₀ failure times than 0.960 g/cm³ grades; class-level values commonly exceed 50 h under these conditions.
The melt flow ratio, expressed as high-load MFR at 21.6 kg divided by low-load MFR at 2.16 kg, is used as an indirect indicator of molecular weight distribution. Film-grade HDPE with low-load MFR of 0.2 g/10 min often exhibits a melt flow ratio above 70, indicating a broad distribution and pronounced shear thinning. Capillary rheometry at 190 °C and a shear rate of 100 s⁻¹ generally yields apparent viscosities in the 1,500–2,500 Pa·s range for HDPE film grades of this melt-flow class. At die shear rates above 1,000 s⁻¹, apparent viscosity may fall below 300 Pa·s, permitting thin-gauge film production without excessive melt pressure. These values are class-level data and should not be used as a specification for LOTRÈNE 3802.
On blown-film extrusion equipment, the processing window is controlled by die gap, blow-up ratio, frost-line height, and melt temperature. A grooved-feed extruder with screw diameter between 65 mm and 90 mm and L/D ratio between 25:1 and 30:1 is commonly used. Die gaps below 0.8 mm increase shear stress at the die lip and may initiate melt fracture at output rates above 150 kg/h. Stable operation at blow-up ratios of 2.5:1–3.5:1 is reported when the frost-line height is maintained between 250 mm and 400 mm above the die, depending on cooling-air temperature and line speed.
Melt pressure at the screen pack is monitored continuously. A gradual pressure rise at constant screw speed indicates gel accumulation or contamination; pressure above 300 bar on 90 mm extruders usually requires screen replacement. Melt temperatures above 240 °C are not recommended for extended residence times because oxidative chain scission can reduce melt strength and increase die-lip deposit formation. Screw cooling channels and low-shear mixing elements are used to limit temperature rise at high screw speeds.
Specific energy demand of 0.938 g/cm³ HDPE film extrusion at 200 °C is typically 0.25–0.35 kWh/kg, but the value depends on screw design, output, and head pressure. Production-scale extrusion records for HDPE film grades in this density-MFR class show that die pressure at start-up can be 10–15% higher than steady-state pressure until the melt pool stabilises. Operators often set the initial screw speed to 70% of nominal output and ramp to target over 15–20 min to avoid purge blockages.
Pre-drying of the raw pellet is generally unnecessary at relative humidity below 60%. Regrind addition up to 20% by weight is common in closed-loop film conversion, provided the regrind is dry and free of paper, label adhesive, and incompatible polymer fractions. The grade is not recommended for direct combination with amine-based antistatic masterbatches without compatibility testing, because amine species can interact with the phenolic stabilizer package and reduce oxidative stability during high-temperature processing.
For blow-moulding, die swell and parison sag are critical. HDPE in this melt-flow range generally requires a die head temperature of 190–210 °C and a mould temperature of 20–40 °C. Parison programming is used to maintain wall thickness in containers with handles. The grade’s density reduces part weight by approximately 2–3% compared with 0.960 g/cm³ HDPE at equal wall thickness, but top-load rigidity is correspondingly lower.
Injection moulding of LOTRÈNE 3802 is possible only in short-flow parts because of the low MFR. Melt temperatures are raised to 230–250 °C and injection pressures are maintained at 100–140 MPa. Freeze-off at the gate is the main limitation; gate diameters below 1.0 mm are not recommended. The resin is therefore not a general-purpose injection-moulding grade and should not be processed as such without flow-path analysis.
The substitution decision is governed by density and melt-flow differences. Relative to QAPCO LDPE extrusion grades in the 0.918–0.922 g/cm³ density band, LOTRÈNE 3802 provides higher tensile modulus, lower oxygen transmission, and lower water-vapour transmission, but reduced optical clarity and a narrower heat-seal temperature window. Heat-seal initiation temperatures rise by approximately 10–15 °C compared with LDPE film, requiring retuning of sealing jaw temperature and dwell time on vertical form-fill-seal equipment.
Relative to 0.960 g/cm³ unimodal HDPE, the 0.938 g/cm³ density of LOTRÈNE 3802 improves environmental stress-crack resistance and puncture resistance, but reduces top-load rigidity and upper-use temperature. In blow-moulded parts, wall thickness may need to be increased by roughly 2–3% to recover the same buckling resistance at equal part geometry. In multi-layer structures, the shift in melt-flow ratio should be evaluated against the tie layer; long residence time above 250 °C can generate gel formation if polyamide tie layers are present.
Compared with C4-LLDPE film grades of MFR 1.0 g/10 min, LOTRÈNE 3802 provides higher moisture barrier and higher modulus but lower dart impact and lower elongation at break. Coextrusion of HDPE and LLDPE layers is used when high dart impact and moisture barrier are required, but the melt-flow mismatch must be managed by separate extruder temperature profiles.
| Attribute | LOTRÈNE 3802 | LDPE extrusion grade | 0.960 g/cm³ unimodal HDPE |
|---|---|---|---|
| Nominal density | 0.938 g/cm³ | 0.918–0.922 g/cm³ | 0.960 g/cm³ |
| Melt flow rate | 0.2 g/10 min | 0.5–8.0 g/10 min | 0.2 g/10 min |
| Stiffness | intermediate | low | high |
| Moisture barrier | intermediate | low | high |
| Environmental stress-crack resistance | high | high | moderate |
| Optical clarity | low | high | low |
Moisture vapour transmission rate is measured by ISO 15106-2 and oxygen transmission rate by ISO 15105-2. For 0.938 g/cm³ HDPE, moisture barrier is superior to LDPE but inferior to 0.960 g/cm³ HDPE, while oxygen barrier follows the same ranking. This barrier positioning affects shelf-life projections for dry goods and liquid packaging.
The natural grade is translucent to opaque white with low clarity; masterbatch addition is required for pigmented film and for UV stabilization in outdoor exposure. UV-stabilised formulations require weathering validation under ISO 4892-2 for specific outdoor service life. Standard processing aids, slip masterbatches, and UV stabilizers are compatible within normal let-down ratios, but amine-based antistatic masterbatches require separate evaluation.
The grade’s operational boundary in high-speed packaging lines is strongly influenced by regrind quality and melt-temperature control. At die lip temperatures above 250 °C, oxidative gel formation becomes visible as specks in the film; this effect is amplified when regrind contains oxidised trim or when residence time exceeds 3 min in the adapter. Frequent die-lip deposit formation is observed when regrind contains oxidised film or when extrusion temperature exceeds 240 °C for more than 3 min. Purging with low-MFR polyethylene compounds is used to remove deposits; fluoropolymer additives at 200–500 ppm can reduce deposit formation on chrome-plated dies. Published data for this specific configuration is limited beyond the general class behaviour described above. The batch certificate of analysis from QAPCO should be consulted for lot-specific density, melt flow rate, and stabiliser content.