| HS Code | 637226 |
| Polymertype | High Density Polyethylene (HDPE) |
| Density | 947 kg/m³ |
| Meltflowrate | 7.5 g/10 min (190 °C/2.16 kg) |
| Tensilemodulus | 1000 MPa |
| Flexuralmodulus | 1000 MPa |
| Tensilestressatyield | 24 MPa |
| Tensilestrainatyield | 9% |
| Tensilestrainatbreak | >600% |
| Charpynotchedimpactstrengthat23c | 10 kJ/m² |
| Charpynotchedimpactstrengthatminus30c | 5 kJ/m² |
| Hardnessshored | 60 |
| Vicatsofteningtemperature | 75 °C |
| Meltingtemperature | 130 °C |
| Thermalconductivity | 0.4 W/m·K |
| Waterabsorption | <0.01% |
| Dielectricconstant | 2.3 |
| Volumeresistivity | >1E14 ohm·cm |
| Uvstabilization | Yes |
| Processingmethod | Injection moulding |
As an accredited Borealis HDPE MG7547S factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Borealis HDPE MG7547S packaging consists of 25 kg polyethylene bags, usually palletized and shrink-wrapped for safe industrial handling. |
| Container Loading (20′ FCL) | Borealis HDPE MG7547S is loaded in 25 kg bags into a 20′ FCL, palletized and secured for safe ocean transport. |
| Shipping | Borealis HDPE MG7547S is shipped as non-hazardous high-density polyethylene pellets. It is not regulated for transport (no UN number, class, or packing group). Use dry, clean, covered containers at ambient temperature. Keep original packaging sealed; avoid moisture, contamination, direct sunlight, and excessive heat. Follow local transport regulations. |
| Storage | Store Borealis HDPE MG7547S in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, flames, and strong oxidizers. Keep bags or containers tightly closed, off the floor on pallets, and protect from moisture, dust, and contamination. Use clean handling equipment and avoid prolonged UV exposure. Follow local regulations and the manufacturer’s safety data sheet for specific storage conditions. |
| Shelf Life | Borealis HDPE MG7547S has a typical shelf life of two years when stored dry, cool, and in unopened original packaging, away from sunlight. |
Borealis HDPE MG7547S is processed in high-cavitation injection moulding lines for beverage closures where the melt flow rate determined in accordance with ISO 1133-1:2022 at 190 °C/2.16 kg is specified at a nominal 7.5 g/10 min and density determined in accordance with ISO 1183-1:2019 is specified at 954 kg/m³. The grade is fed to the main hopper of a reciprocating-screw injection moulding machine with screw L/D ratios of 20:1 to 25:1, using barrel temperatures from feed to metering zone of 180–230 °C and hot-runner manifold temperatures maintained between 220 °C and 230 °C. Cavitation of 48–96 is common on rotary cube or stack-platen platforms; gate diameter is selected between 0.6 mm and 1.2 mm to prevent premature gate freeze while limiting stringing. In cap and closure production for carbonated soft drinks and still water, the compound blend is metered with a PE-carrier colour masterbatch at 1.5–2.5 wt% and a slip/antiblock masterbatch at 0.5–1.0 wt%; closed-loop regrind from sprues and rejected closures is limited to 20 wt% when food-contact migration limits apply because hot-runner residence-time distributions shift when flake bulk density differs from virgin pellets. Compliance is verified against EU Regulation (EU) No 10/2011 Annex V overall migration limit of 10 mg/dm² and FDA 21 CFR 177.1520 for polyolefin food-contact articles, with closure performance evaluated under published ISBT voluntary test methods for neck finish and tamper-evident function. Finished articles are PCO 1881 and PCO 1810 screw closures with tamper-evident bridges for carbonated soft drinks, still water, and isotonic beverages. On production lines, the principal failure mode is inconsistent tamper-evident bridge tearing when mould cooling water supply temperature exceeds 15 °C, causing dimensional shift in the undercut region and raising reject rates at post-mould vision inspection.
The solidification rate of a 0.30–0.45 mm sidewall governs cycle time in thin-wall dairy cup moulding. HDPE MG7547S is processed on accumulator-assisted high-speed injection moulding machines with clamp force between 2500 kN and 3500 kN, screw diameters selected to maintain cushion at 3–6 mm, and injection speeds of 400–800 mm/s to fill the cavity before the melt front freezes. Melt temperature is held between 200 °C and 230 °C; mould coolant inlet temperature is maintained at 8–12 °C with turbulent flow at Reynolds numbers above 4000 in conformal cooling circuits. White pigmentation for dairy containers is achieved with a PE-carrier titanium dioxide masterbatch at 4.0–6.0 wt%, because thin sidewalls require higher pigment loading to reach the required opacity after wall thickness reduction; a processing aid/slip masterbatch is added at 0.5–1.0 wt% only when demoulding force measured by ejection force sensors exceeds 120 N per cavity. Food-contact compliance is tested by the converter under EU Regulation (EU) No 10/2011 with 50% ethanol and 3% acetic acid simulants for dairy and acidic food categories, with overall migration below 10 mg/dm²; FDA 21 CFR 177.1520 conditions of use A through H apply. Terminal products are stackable round or rectangular dairy cups used for yoghurt, dessert, and cream cheese, typically paired with aluminum-foil or PE-laminated lid stock. In production, flow hesitation at the base-to-corner transition is observed when the injection velocity profile is decelerated too early; this produces weld-line grooves and reduces top-load strength in subsequent stack compression tests.
| Downstream article | Standard / regulation | Test condition or method | Threshold or verification point |
|---|---|---|---|
| Beverage closures | EU Regulation (EU) No 10/2011 | Overall migration, Annex V food simulants | 10 mg/dm² |
| Beverage closures | FDA 21 CFR 177.1520 | Condition of use for olefin polymers | Compliance with specification |
| Thin-wall dairy cups | EU Regulation (EU) No 10/2011 | 50% ethanol and 3% acetic acid | 10 mg/dm² |
| Thin-wall dairy cups | ISO 1133-1:2022 | MFR at 190 °C/2.16 kg | Batch certificate value |
| Industrial pails | ISO 2248:1985 | Vertical impact drop test, filled package | No leak or rupture at specified fill |
| Industrial pails, dangerous goods | ADR/RID/IMDG Chapter 6.1.5 | UN performance testing | Package type approval |
| Storage boxes, child-appealing | EN 71-3:2019+A1:2021 | Migration of certain toxic elements | Element-specific limits |
| Laboratory packaging | USP <661.1>, Ph. Eur. 3.1.3 | Extractables after autoclave extraction | Total organic carbon and turbidity limits |
Where organoleptic neutrality and environmental stress cracking resistance are evaluated for flip-top dispensing closures used with shampoos, body washes, and lotions, HDPE MG7547S is moulded on 16–32-cavity hot-runner tools with valve gates to reduce gate vestige. The melt temperature is set between 210 °C and 230 °C, holding pressure is limited to 50–70 MPa hydraulic equivalent, and mould cooling is held at 10–15 °C. Colour masterbatch addition is 1.0–2.0 wt%; a UV stabilizer masterbatch is added at 0.2–0.5 wt% when closures are exposed to retail lighting in transparent secondary packaging. Slip/anti-static masterbatch at 0.5–1.0 wt% is introduced only after hinge flexure tests indicate surface blocking during automated cap assembly, because excessive slip migration can compromise hinge durability after repeated flexing. Environmental stress cracking resistance is evaluated under ASTM D1693-15 with 10 wt% Igepal CO-630 at 50 °C; compliance for the finished package is assessed under REACH 1907/2006 substance restrictions and, for cosmetic packaging integrity, EC No 1223/2009 Article 17 compatibility. The converter is responsible for compatibility testing with surfactant systems because thread and hinge regions are under residual moulded-in stress. Terminal products are flip-top dispensing closures, disc-top caps, and push-pull closures for personal care and household liquid products.
At closed-loop regrind fractions above 25 wt%, the melt viscosity distribution of HDPE MG7547S broadens because regrind from sprues, flash, and rejected pails carries reduced molecular weight from prior residence time and re-extrusion shear history. On injection moulding machines with clamping force between 4500 kN and 8000 kN, this viscosity shift is controlled by increasing the metering zone temperature from 220 °C to 240 °C, reducing screw back pressure from 10 MPa to 6 MPa, and selecting a screw with a compression ratio of 2.2:1–2.8:1 to limit additional shear heating. Carbon black masterbatch is metered at 2.0–3.0 wt%; UV stabilizer masterbatch is metered at 0.3–0.8 wt% for outdoor or warehouse exposure. The finished pail walls are specified between 1.8 mm and 2.5 mm with base corner radii above 1.5 mm to reduce stress concentration. Drop-impact performance is tested according to ISO 2248:1985 at −18 °C, 23 °C, and 40 °C after filling with water or a standard test medium; stack compression is measured according to ISO 12048:1994. For pails used to pack dangerous goods, the filled package must additionally pass UN performance testing under ADR/RID/IMDG Chapter 6.1.5; resin compliance alone does not confer UN certification. Terminal products are 5–25 L open-head or tight-head pails for paints, lubricants, detergents, and water-based industrial liquids. When regrind levels exceed 30 wt%, batch-to-batch fill-time variation and top-rim ovality should be monitored against the converter’s process capability baseline because published data for this specific configuration is limited.
Optional mould-filling pressure for thin-gauge storage boxes is established with cavity pressure transducers sampled at 100 Hz. Packing pressure is transitioned when cavity pressure reaches 50–65 MPa; holding time is set at gate seal time plus 0.2 s. Wall thickness is specified at 1.2–2.5 mm with rib-to-nominal-wall ratio between 0.5 and 0.7 to avoid sink marks on visible surfaces. Colour masterbatch is dosed at 1.0–3.0 wt%; process regrind is limited to 15 wt% when surface streak rejection is not permitted. If UV exposure is required, a hindered amine light stabilizer masterbatch is added at 0.2–0.4 wt%. Regulatory compliance for housewares is anchored to REACH 1907/2006; for storage articles marketed as toys or child-appealing items, EN 71-3:2019+A1:2021 migration limits for certain toxic elements apply. General household storage boxes are not automatically classified as toys, but many retailers require EN 71-3:2019+A1:2021 test reports as a condition of listing. HDPE MG7547S is processed at melt temperatures of 190–230 °C; moulds are cooled with water at 10–15 °C. Terminal products are modular storage boxes, stackable caddies, and drawer organizers. The predominant production defect is top-load buckling after moulding when the box is ejected too hot; forced air at 15 °C reduces post-ejection distortion but can shift surface gloss variation outside the approved colour-matching tolerance.
Autoclave sterilization of laboratory-grade specimen containers and diagnostic reagent closures exposes HDPE MG7547S to saturated steam at 121 °C for 15–30 min, which approaches the upper service temperature of unpigmented high-density polyethylene. Parts are injection moulded on small-cavitation tools with core-and-cavity dimensions compensated for post-mould shrinkage of 1.8–2.5%. Natural, unpigmented material is used to avoid extractable colourant additives; silicone-free mold release is specified when mould surface release agents are required. No regrind is introduced into laboratory-grade runs, and virgin material is purged with 5–10 kg of resin before start of production. If colour-coded closures are required, a PE-carrier masterbatch is added at 0.5–1.5 wt% and validated for the same extractables acceptance limits. Compliance is assessed by the converter under USP <661.1> and Ph. Eur. 3.1.3 for polyolefin containers and closures, with total organic carbon and turbidity limits measured after autoclave extraction. The grade itself is not certified as a medical device material; the moulder must qualify the finished article for the intended use. Terminal products are specimen containers, reagent bottle closures, and diagnostic kit reagent reservoirs.
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Borealis HDPE MG7547S is a high-density polyethylene pellet grade supplied for injection-moulded rigid packaging, with primary use in thin-walled closures, caps, overcaps, and tamper-evident systems. The grade is differentiated within the Borealis HDPE range by its elevated melt flow rate of 7.5 g/10 min when determined according to ISO 1133-1 at 190 °C with 2.16 kg load, and a nominal density of 0.954 g/cm³ determined according to ISO 1183-1. These two values position the resin for high-speed multicavity injection moulding rather than extrusion blow moulding or sheet extrusion. The stabilisation package associated with the S suffix is intended for closure production where low taste and odour contribution is required, although the converter must confirm the specific organoleptic and migration behaviour under the intended food-contact conditions. The product is typically controlled by melt flow rate, density, tensile yield stress, flexural modulus, and Charpy notched impact, with certificates of analysis controlling lot-to-lot variation rather than nominal datasheet values.
Injection moulding of MG7547S on high-cavitation tooling is governed by the interaction between melt viscosity, cavity-fill pressure, and cooling rate. On standard three-zone screws with L/D ratios from 20:1 to 25:1 and compression ratios of 2.5:1 to 3.0:1, a rising barrel-temperature profile from 180 °C in the feed zone to 220–250 °C in the metering zone is used. The nozzle temperature is normally maintained between 230 °C and 250 °C. Mold temperatures of 10–30 °C are sufficient for dimensional stability in thin-wall closures; higher mold temperatures up to 40 °C may be required for thicker sections or for improved surface gloss, but they extend cooling time. Injection speed should be medium to high, with fill times below 0.3 s for wall sections of 0.6–1.2 mm on closure walls and tamper-evident bands. Typical clamp force requirements range from 180 to 300 metric tonnes for 64-cavity tools, depending on projected area and part design.
The maximum processing temperature is limited by the onset of oxidative degradation. At metering-zone temperatures above 280 °C, the polymer can undergo chain scission and form gels, especially if residence time exceeds 5 min under high shear. At the lower boundary, melt temperatures below 200 °C may produce short shots, gate blush, or excessive orientation near the gate seal area. The processing window is therefore narrower than for lower-flow HDPE grades; holding pressure and backpressure must be adjusted to prevent sink marks while avoiding overpacking of the gate area. Because HDPE is not hygroscopic, pre-drying is generally unnecessary when pellets are stored in dry conditions. If condensation is observed after storage at relative humidity above 60% or after temperature cycling from cold storage, the pellets should be dried at 70–80 °C for 1–2 h in a desiccant dryer with a dew point below -20 °C. Drying above 90 °C for extended periods can induce oxidation and raise yellowness index.
In beverage closure production, MG7547S is used for one-piece and two-piece closures, tamper-evident bands, and overcaps with wall thicknesses that typically fall between 0.6 mm and 1.5 mm. The high melt flow rate permits multicavity filling with reduced injection pressure, which is particularly relevant on high-cavitation tools with 32 to 96 cavities where cavity-to-cavity imbalance can cause torque variability. Torque retention is evaluated on production capping equipment, and closure designs based on this resin must be qualified against ISO 8317 or manufacturer-specific torque tests for child-resistant closures. Environmental stress crack resistance is a critical limitation in closures exposed to detergents, oils, or aggressive beverage constituents; published data for this specific configuration is limited, so ESCR should be measured according to ASTM D1693 or ISO 22088-3 on finished parts under the intended stress and environment rather than on compression-moulded plaques alone. The resin is not intended for extrusion blow moulding because its low melt strength can cause parison sag and poor wall-thickness distribution. In injection-compression moulding, however, the grade can be used for flat lids and overcaps where lower clamp force is needed.
Three classes of olefin resins compete for closure applications: high-flow injection-moulding HDPE such as MG7547S, low-flow blow-moulding HDPE, and polypropylene random copolymers. The fundamental difference between MG7547S and blow-moulding HDPE is the melt flow rate. Blow-moulding grades are normally supplied with MFR values below 1.0 g/10 min at 190 °C / 2.16 kg to provide parison melt strength; MG7547S, with a higher MFR, cannot maintain a stable parison and is therefore restricted to injection processes. Conversely, the lower melt flow rate of blow-moulding HDPE makes thin-wall injection filling difficult and extends cycle time. Compared with polypropylene random copolymers, MG7547S offers lower flexural modulus and generally lower torque retention; however, HDPE closure resins can show better environmental stress crack resistance in certain fatty or oily environments and can offer lower deformation at ambient and freezer temperatures. The density of MG7547S, at 0.954 g/cm³, is above that of polypropylene random copolymers but below that of many high-density blow-moulding grades at 0.958–0.963 g/cm³, which affects part weight per cavity and top-load performance.
Representative nominal property values for Borealis HDPE MG7547S are listed below; they should not be read as specifications, and lot-specific certificates of analysis remain determinative for acceptance.
| Property | Test method | Nominal value |
|---|---|---|
| Density | ISO 1183-1 | 0.954 g/cm³ |
| Melt flow rate | ISO 1133-1, 190 °C, 2.16 kg | 7.5 g/10 min |
| Tensile stress at yield | ISO 527-2, type 1A, speed 50 mm/min | 25 MPa |
| Tensile elongation at yield | ISO 527-2, type 1A, speed 50 mm/min | 8% |
| Flexural modulus | ISO 178 | 1100 MPa |
| Charpy notched impact at 23 °C | ISO 179-1/1eA | 5 kJ/m² |
| Vicat softening temperature, A50 | ISO 306 | 127 °C |
| Shore D hardness | ISO 868 | 63 |
The short-term mechanical response of MG7547S is typical of high-density polyethylene with moderate crystallinity. A tensile yield stress of 25 MPa according to ISO 527-2 and a flexural modulus of 1100 MPa according to ISO 178 provide sufficient top-load strength for snap-on and tamper-evident closures, but the grade is not a high-modulus engineering resin. Notched Charpy impact at 23 °C is in the range 4–6 kJ/m² according to ISO 179-1/1eA, which supports crack tolerance during demoulding and capping. At temperatures below 0 °C, impact resistance declines and design features such as sharp corners in tamper-evident bridges should be stress-relieved or radiused to reduce brittle failure.
Continuous stress-crack resistance under environmental exposure is not adequately predicted by short-term impact data. Finished closures exposed to nonylphenol ethoxylates, terpenes, or surfactant-containing detergents should be tested under static stress using methodology adapted from ISO 22088-3 or ASTM D1693 condition B. Published data for this specific configuration is limited; users should not extrapolate plaque ESCR to moulded closure failure without component-level validation on production tooling. The grade is not recommended for continuous exposure to strong oxidising agents or for service involving aromatic hydrocarbon immersion.
For food-contact articles produced from MG7547S, compliance is governed by the final article and the converter’s manufacturing process. For the European Union, migration testing is conducted under Regulation (EU) No 10/2011 with food simulants assigned to the intended contact category; for the United States, the base polymer must meet 21 CFR 177.1520 for olefin polymers. Additional requirements under REACH, RoHS Directive 2011/65/EU, and applicable national packaging regulations apply. Migration kinetics of low-molecular-weight species follow diffusion-controlled release and are temperature dependent, so converter validation must include the intended hot-fill or pasteurisation exposure. The resin supplier’s product stewardship declaration should be requested for each lot, because lot-specific catalyst residues and additive levels can influence migration, colour, and odour.