| HS Code | 951319 |
| Polymertype | High Density Polyethylene (HDPE) |
| Density | 0.944 g/cm3 |
| Meltflowrate 190c 21 6kg | 2.0 g/10 min |
| Meltflowrate 190c 5kg | 0.2 g/10 min |
| Tensilemodulus | 1100 MPa |
| Tensilestressatyield | 26 MPa |
| Tensilestrainatyield | 9% |
| Tensilestressatbreak | 30 MPa |
| Elongationatbreak | >600% |
| Charpynotchedimpactstrength 23c | 20 kJ/m2 |
| Charpynotchedimpactstrength Minus30c | 8 kJ/m2 |
| Vicatsofteningtemperature | 76 °C |
| Meltingtemperature | 131 °C |
| Ballindentationhardness | 50 MPa |
| Waterabsorption | <0.01% |
| Thermalconductivity | 0.4 W/mK |
| Coefficientoflinearthermalexpansion | 1.5E-4 /°C |
| Volumeresistivity | >1E14 ohm·cm |
| Dielectricconstant | 2.3 |
| Processingmethod | Blow Molding |
As an accredited Borealis HDPE VL4470 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Borealis HDPE VL4470 is packed in 25 kg polyethylene bags, palletized, stretch-wrapped, and clearly labeled for industrial shipping and storage. |
| Container Loading (20′ FCL) | 20′ FCL loaded with Borealis HDPE VL4470 in 25 kg bags, palletized or floor-loaded, securely stowed for ocean freight. |
| Shipping | Borealis HDPE VL4470 is typically shipped as non-hazardous high-density polyethylene in 25 kg PE bags, octabins, or bulk containers, palletized and stretch-wrapped. It is not classified as dangerous goods for road, sea, or air transport. Keep dry and avoid UV, contamination, and excessive heat. |
| Storage | Store Borealis HDPE VL4470 indoors in original, sealed bags or octabins on pallets in a dry, clean, well-ventilated area. Keep away from direct sunlight, heat, ignition sources, and strong oxidizers. Protect from moisture, dust, and prolonged UV exposure. Maintain moderate temperatures, avoid extremes, keep containers closed, and do not store near foodstuffs or incompatible materials. Ensure proper stock rotation. |
| Shelf Life | Borealis HDPE VL4470 has an indefinite shelf life when stored in dry, cool conditions away from direct sunlight and contaminants. |
In extrusion blow moulding of 0.5 L–2.0 L household cleaner bottles, Borealis HDPE VL4470 is processed as the virgin fraction when the container design combines a 250 N top-load acceptance value, a 28-410 neck finish, and exposure to diluted surfactants, builders, or peroxide-based bleaches that require stress-crack resistance rather than simple burst strength. The screw is a 60 mm grooved-feed barrier screw with L/D 24:1; zone temperatures from throat to die are 170 °C, 180 °C, 185 °C, 190 °C, and 195 °C, with the die head maintained at 195 °C. Virgin VL4470 is metered at 87 wt%; closed-loop trim scrap is ground through an 8 mm screen and re-introduced at 10 wt%; a low-density polyethylene carrier colour masterbatch occupies the remaining 3 wt%. The die gap is set to 1.5–2.0 mm, blow-up ratio is held between 2.4:1 and 2.8:1, mould cooling water is controlled at 10–14 °C, and a 1 L bottle is formed at a sidewall thickness of 0.8–1.2 mm with a shot cycle of 9–12 s. Drying is required only when moisture in regrind exceeds 0.10 wt%; wet flake is dried at 80 °C for 2 h in a desiccant hopper before gravimetric blending. The finished container is checked for top load after 24 h at 23 °C, for drop performance at −18 °C if the distribution chain requires cold-climate handling, and for ESCR on sidewall specimens under ASTM D1693-15 condition B at 50 °C when the formulation exceeds pH 12. The application scope remains non-food household care packaging; if a claim under EU Regulation 10/2011 or FDA 21 CFR 177.1520 is required, the grade lot must be confirmed against the current supplier food-contact statement before tooling release.
A 200 mL viscous hair-treatment bottle with a 24/410 pump thread is blow moulded in VL4470 when the brand specification requires a polished surface, low mould-release transfer, and sufficient hoop stiffness to prevent neck ovalisation during pump insertion. The compound is fed as 98 wt% virgin VL4470 and 2 wt% LDPE-based colour masterbatch; closed-loop regrind is excluded from this dosage because gel particles or black specks are visually unacceptable on an SPI-A2 cavity finish. The extruder is a 45 mm reciprocating screw with L/D 25:1, operated at an adapter temperature of 190–200 °C and a die temperature of 195 °C. The tool sets a blow-up ratio of 1.8:1–2.2:1 to preserve surface finish, a sidewall thickness of 1.2–1.6 mm in the shoulder and base corners, and a neck insert cooled separately at 6–8 °C to control thread shrinkage. Cycle time is 15–20 s due to the thicker wall and high-gloss cooling requirement. The mould cavity is electroplated with a grain-free polished surface; ejection air is dried to a dew point below −30 °C to prevent water spot defects. Compression after demoulding is limited by sizing gauges and a 24 h room-temperature conditioning step before pump torque testing to 1.5–2.5 N·m insertion torque. For the formulation, organoleptic panel testing under the brand’s low-odour protocol is performed because volatile component migration from a masterbatch or processing aid can affect the cosmetic product headspace. Cosmetic packaging is not automatically covered by a food-contact statement; compliance is assessed under REACH Regulation (EC) No 1907/2006, Directive 94/62/EC on packaging and packaging waste, and the brand’s cosmetic product safety assessment under Regulation (EC) No 1223/2009. Published data for VL4470-specific migration into oil-based hair-treatment formulations is limited, so a package-content interaction study is required when the product contains high-fatty-acid esters or terpenes.
For dry oral dosage packaging of vitamin and mineral tablets, Borealis HDPE VL4470 is converted on a shuttle blow moulder after the finished container has been assessed against USP <661.1> for plastic packaging systems, Ph. Eur. 3.1.3 for polyolefin containers, and the relevant lot-level statement for FDA 21 CFR 177.1520 or EU Regulation 10/2011 if the product is marketed as a food supplement. The formula is 100 wt% virgin VL4470; regrind is not used for primary contact unless the pharmaceutical quality system specifically permits same-grade in-house scrap with full batch traceability. The parison is inflated with dehumidified compressed air at a dew point below −40 °C to prevent internal odour or biological load introduction. Target sidewall thickness is 0.7–1.0 mm on a 150 mL bottle with a 38 mm child-resistant closure and induction-seal liner. Mould cooling is held at 8–12 °C; after trimming, the bottle passes through a static eliminator and is packed in double-bag-lined corrugated cartons to control foreign matter. The key technical conflict in this segment is moisture ingress across the polyethylene wall. HDPE is not an oxygen barrier, but for many dry oral dosage forms the critical parameter is water vapour transmission; finished-wall WVTR is measured under ASTM E96/E96M-22 at 38 °C and 90 % RH or under ISO 15106-1 if the closure supplier requires a film specimen. If the brand limit is stricter than the measured value, a desiccant closure, a thicker wall, or a barrier insert must be introduced rather than relying on VL4470 alone. The grade should be excluded from use with liquid oral products, oxygen-sensitive formulations, or terminal sterilisation processes unless specific chemical and thermal validation data are available from the supplier; published data for this specific configuration is limited.
The 1 L dosing bottle for quaternary ammonium chloride-based disinfectant concentrates is blow moulded from 100 wt% virgin Borealis HDPE VL4470 because recycled content is excluded from aggressive chemical contact and because the closure area must withstand repeated wrenching after partial bottle inversion. The container is produced on a single-station accumulator-head machine with a 70 mm barrel and L/D 24:1, using a die head temperature of 195–205 °C and a calibrated neck blow pin. Sidewall thickness is specified at 1.0–1.3 mm with a minimum base radius of 8 mm to reduce stress concentration at the pinch-off. The pinch-off zone is additionally quenched with cold air at 5–10 °C for 2–3 s before mould opening because trim weld-line stress is the preferred initiation point for environmental stress cracking under quaternary ammonium compound exposure. After 48 h ambient conditioning, the bottle is filled at 85 % nominal capacity, capped with a child-resistant polypropylene closure, and subjected to a drop test at −18 °C from 1.2 m under ADR 6.1.5 packaging test protocols when the product is dispatched as a limited quantity. Compliance for chemical packaging includes classification under CLP Regulation (EC) No 1272/2008 and packaging requirements under Directive 94/62/EC; UN certification of the filled package is a design-type test and must be repeated if the neck finish, wall distribution, or closure type changes. A chemical compatibility protocol is mandatory: ASTM D543-21 immersion at 23 °C and 50 °C for 7 days, followed by tensile retention per ISO 527-2 and visual assessment for pitting, blooming, or surface chalking. Published data for VL4470 in quaternary ammonium chloride disinfectant concentrates is limited; the processor should not extrapolate ESCR data from non-ionic detergent tests without a side-by-side validation under ASTM D1693-15 condition A and B at 50 °C.
Closed-loop reintroduction of trimmed flash and knocked-out tail sections into a 5 L non-food industrial canister line is a process-control application rather than a product property claim. The system meters 70 wt% virgin VL4470 and 30 wt% ground trim scrap through separate gravimetric hoppers feeding a 75 mm grooved-feed extruder with L/D 30:1. The scrap is ground through a 6 mm screen with a knife gap below 0.3 mm, passed over a magnetic separator and a fines classifier, and dried to below 0.10 wt% moisture under 80 °C desiccant air before blending. Repeated heat history changes the low-shear viscosity and parison sag behaviour; the die gap must be narrowed by 0.1–0.2 mm for every 10 wt% increase in regrind fraction when wall-thickness variance exceeds ±0.15 mm on the 5 L sidewall. The melt pump after the extruder is set to maintain a pressure of 150–200 bar before the head; die pressure drift beyond 10 % from virgin baseline triggers a shut-down and screen-pack inspection. Batch-to-batch variance is monitored by melt mass-flow rate under ISO 1133-1:2022, ESCR under ASTM D1693-15, and in-line ultrasonic wall mapping. The table below records the minimum monitoring plan for a validated non-food canister line; it does not replace design-type testing for dangerous goods packaging because regrind use in UN-certified packagings is subject to national approval and re-testing.
| Regrind fraction | Monitoring point | Method / instrument | Control limit or action |
|---|---|---|---|
| 0 wt% | Melt mass-flow rate | ISO 1133-1:2022 at 190 °C / 2.16 kg | Record lot baseline |
| 10 wt% | Moisture in flake | ISO 15512:2019 or Karl Fischer | Below 0.10 wt% before hopper |
| 20 wt% | Parison wall-thickness variance | In-line ultrasonic gauge | Maximum ±0.15 mm on 1 L sidewall |
| 30 wt% | ESCR on sidewall | ASTM D1693-15 condition B, 50 °C | Meet brand limit; typically not below 20 h for non-aggressive liquid |
Repeated extrusion passes generate gel particles and crosslinked specks if the ground scrap remains in contact with hot machine surfaces for extended intervals; purging with a polyethylene purge compound after 8 h production blocks is advised to prevent carbonised deposits from breaking into the next lot. Published data for the rheological response of VL4470 after three closed-loop regrind cycles is limited; a capillary rheometry trace under ISO 11443 at 190 °C and 210 °C should be generated for each scrap source before committing to a permanent regrind fraction. The accepted terminal product is a 5 L non-food industrial canister with 2.0–2.5 mm sidewall thickness, tested for drop impact at 1.2 m on the base corner and for top load at 300–500 N depending on pallet stacking height.
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Borealis HDPE VL4470 is a high-density polyethylene resin positioned for small blow-moulded containers, closures, and related rigid packaging. The material is supplied as pelletized resin for continuous extrusion blow moulding, shuttle blow moulding, and injection blow moulding. Representative values cited below are drawn from manufacturer literature and are not batch-release limits; current datasheets and supplier declarations must be consulted before production qualification.
The grade exhibits a density of 0.954 g/cm³ under ISO 1183-1:2019 and a melt flow rate of 2.1 g/10 min at 190 °C and 2.16 kg under ISO 1133-1:2022. The density is held below the 0.960 g/cm³ threshold at which environmental stress-crack resistance in high-density polyethylene can decline sharply. Tensile modulus at 1 mm/min is typically 1100 MPa under ISO 527-2:2012, with tensile stress at yield near 27 MPa and elongation at yield near 9%. Notched Charpy impact at 23 °C is approximately 6 kJ/m² under ISO 179-1:2010. Vicat softening temperature by method A50 is approximately 126 °C under ISO 306:2022.
| Property | Test method | Representative value |
|---|---|---|
| Density | ISO 1183-1:2019 | 0.954 g/cm³ |
| Melt flow rate (190 °C, 2.16 kg) | ISO 1133-1:2022 | 2.1 g/10 min |
| Tensile modulus (1 mm/min) | ISO 527-2:2012 | 1100 MPa |
| Tensile stress at yield | ISO 527-2:2012 | 27 MPa |
| Elongation at yield | ISO 527-2:2012 | 9% |
| Charpy notched impact strength, 23 °C | ISO 179-1:2010 | 6 kJ/m² |
| Vicat softening temperature, method A50 | ISO 306:2022 | 126 °C |
| Shore D hardness | ISO 868:2003 | 62 |
On continuous extrusion blow moulding lines, barrel temperature settings from 180 °C to 220 °C are used for VL4470, with head and die zones typically maintained between 190 °C and 210 °C. Temperature settings are not uniform across barrel zones. A typical profile for a 60 mm grooved-feed extruder with 30:1 L/D is: feed zone 170–180 °C, compression zone 180–190 °C, metering zone 190–200 °C, and head 190–205 °C. Melt temperature measured at the die entry should remain between 190 °C and 210 °C for stable parison formation. If melt temperature exceeds 215 °C, die swell increases and wall thickness control becomes unstable; if melt temperature falls below 185 °C, melt fracture may appear as sharkskin. Screw speed is set to maintain melt residence time below 15 min; longer residence time increases thermomechanical degradation and shifts the MFR upward.
For moulds with pin diameters below 10 mm, the upper melt temperature should not exceed 230 °C; above this value, parison sag becomes measurable and wall-thickness variation increases. Single-screw extruders with grooved feed sections and L/D ratios from 24:1 to 30:1 provide stable output; barrier-flight screw designs reduce melt temperature heterogeneity. On shuttle machines with clamp force capacities from 50 kN to 120 kN, pinch weld integrity depends on land parallelism and surface cleanliness of the pinch-off insert. If resin has been stored at relative humidity above 60%, surface moisture can cause splay; pre-drying at 70–80 °C for 2–4 h is applied before processing.
Blow mould cooling water temperature is typically maintained at 8–12 °C to reduce cycle time. Mould surface temperature above 20 °C can extend cooling time and increase container shrinkage; below 5 °C condensation may cause surface defects. For containers with wall thickness 1.0 mm, total cycle time on shuttle machines is typically 10–14 s; increasing wall thickness to 1.5 mm raises cooling time by approximately 2–4 s. These values are equipment-dependent and should be established during process qualification.
Masterbatch addition alters rheology and should use an HDPE carrier with density within ±0.005 g/cm³ of the base resin. Letdown ratios above 5% should be validated for parison stability. Regrind from edge trim and rejected bottles can be incorporated at levels up to 30% in non-regulated packaging if the regrind is clean and dry; for food-contact applications, the use of regrind is governed by Regulation (EC) No 10/2011 and national legislation. Higher regrind levels increase the melt flow rate by chain scission and can lower intrinsic viscosity; the effect is more pronounced after multiple heat histories.
Die swell for VL4470 on long-land blow moulding heads is typically in the range of 15–30%. Swell above 30% indicates either excessive melt temperature, insufficient die land length, or contamination of the die bushing. Wall thickness correction is achieved through die gap programming rather than through temperature reduction alone; temperature reduction below 180 °C can raise melt pressure and produce sharkskin on the parison surface. Environmental stress-crack resistance is evaluated under ASTM D1693-15. In high-density polyethylene, ESCR is inversely related to density; raising density above 0.960 g/cm³ can reduce F50 ESCR by more than 50% relative to 0.954 g/cm³. VL4470 is therefore held at the 0.954 g/cm³ density plateau rather than maximized for short-term tensile modulus. Specific F50 values for this VL4470 configuration should be taken from the current manufacturer datasheet; published data for this specific configuration is limited.
Small blow-moulded containers for personal care, cosmetics, and pharmaceutical liquids are primary application areas. Containers with wall thickness from 0.5 mm to 1.2 mm have been produced on single-station shuttle machines at cycle times between 8 s and 20 s, depending on part weight and mould cooling. Drop-impact performance is specified according to ASTM D5276-19, with pass criteria dependent on fill volume and closure design. Injection blow moulding of bottles with neck finishes requiring dimensional stability is feasible when melt temperature is held at the lower end of the range to avoid gate stringing; dimensional checks are performed after conditioning at 23 °C and 50% RH under ISO 291. In closure applications on injection moulding machines with clamp force from 150 kN to 400 kN, VL4470 can be used for overcaps and secondary closures where cycle time is not the primary constraint. For high-speed closure manufacturing, a higher MFR HDPE grade may be specified if fill speed and cycle time dominate.
Compared with lower-density HDPE blow-moulding grades in the 0.944–0.948 g/cm³ range, VL4470 provides higher top load and greater modulus at equal wall thickness, with a reduction in ESCR that remains acceptable for many small-container applications. Top-load resistance is measured at 10 mm/min crosshead speed under ISO 12048 for complete containers, with peak force values dependent on wall thickness and closure geometry. Compared with bimodal HDPE grades used for large-volume drums or industrial containers, the melt flow rate of 2.1 g/10 min is higher and the material is optimized for thin-wall forming rather than long parison hang time. Compared with high-flow HDPE grades with MFR above 4 g/10 min, VL4470 trades cycle-time advantage for improved ESCR and melt strength. These differences are grade-selection criteria, not universal superiority; they must be assessed against part geometry, closure torque requirements, and filling temperature.
In food and pharmaceutical packaging, organoleptic neutrality is assessed by sensory panels and by migration testing under Regulation (EC) No 10/2011. For polyethylene, the relevant authorisation in the United States is often based on FDA 21 CFR 177.1520; in the European Union, Regulation (EC) No 10/2011 applies. VL4470 is positioned where low taste and odour contribution is required; however, the final package must be tested in the intended food simulant because migration behaviour is affected by wall thickness, surface-to-volume ratio, closure components, and processing history. Suppliers may provide a declaration of compliance for the resin, but this declaration does not automatically cover the converted article. For pharmaceutical packaging, compendial testing may include USP <661.1> or Ph. Eur. plastic container monographs; published data for this specific VL4470 formulation should be obtained from the supplier before dossier submission.
| Requirement | Scope | Application to converted articles |
|---|---|---|
| Regulation (EC) No 10/2011 | Plastic food contact materials | Supplier compliance statement required; final article testing in intended simulant is necessary |
| FDA 21 CFR 177.1520 | Olefin polymers for food contact | Applicable subject to conditions of use and food type |
| REACH Regulation (EC) No 1907/2006 | SVHC declaration and restrictions | No SVHC above 0.1% w/w per current safety data sheet |
| RoHS Directive 2011/65/EU | Hazardous substances in EEE | Not applicable to packaging unless the component is incorporated into EEE; declarations available on request |
Incoming resin evaluation typically includes melt flow rate by ISO 1133-1:2022, density by ISO 1183-1:2019, and visual pellet cleanliness. Batch-to-batch variance is controlled within supplier specification; for conversion processes with tight wall-thickness tolerances, lot-to-lot MFR shifts above ±0.2 g/10 min may require adjustment of die gap or screw speed. Moisture content is not routinely specified because bulk HDPE is not hygroscopic; surface moisture is managed as described above.
Operational boundaries include continuous service temperatures not exceeding 80 °C in load-bearing packaging, avoidance of strong oxidizing acids, and use of UV stabilization for prolonged outdoor exposure. The resin is incompatible with aromatic hydrocarbons, chlorinated solvents, and some ester-based plasticizers; these agents cause swelling and reduce mechanical strength. Blending with amine-based processing aids or high levels of metal stearates should be validated for surface adhesion and colour effects. Welding and thermal oxidation can generate low-molecular-weight species and black specks; purging with a polyethylene purge resin is recommended before shutdown. Gas-assisted injection moulding is not preferred unless injection pressure is sufficient and wall thickness exceeds 2 mm.