| HS Code | 784846 |
| Density | 0.952 g/cm³ |
| Meltflowrate | 0.35 g/10 min (190°C/2.16 kg) |
| Meltflowratio | 95 |
| Tensilestrengthatyield | 25 MPa |
| Tensilestrengthatbreak | 30 MPa |
| Elongationatbreak | 600% |
| Flexuralmodulus | 1200 MPa |
| Notchedizodimpactat23c | 200 J/m |
| Notchedizodimpactatminus40c | 100 J/m |
| Vicatsofteningtemperature | 126°C |
| Brittlenesstemperature | -70°C |
| Environmentalstresscrackresistance | >1000 h (10% Igepal) |
| Shoredhardness | 65 |
| Waterabsorption | <0.01% |
| Thermalconductivity | 0.45 W/m·K |
| Coefficientoflinearthermalexpansion | 1.2E-4 /°C |
| Dielectricconstant | 2.3 |
| Volumeresistivity | >1E15 ohm·cm |
As an accredited Braskem HDPE GF5250 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Braskem HDPE GF5250 is supplied in 25 kg polyethylene-lined paper bags, stacked on 1,000 kg pallets for safe handling. |
| Container Loading (20′ FCL) | Container Loading (20′ FCL): Braskem HDPE GF5250 in 25 kg bags, palletized, securely stowed and braced; max payload approx. 22 MT. |
| Shipping | Braskem HDPE GF5250 is a non-hazardous polyethylene resin in pellet form. It typically ships in 25 kg bags, 1,000 kg bulk bags, or bulk trucks/railcars. Store dry, away from excessive heat and UV. No special dangerous-goods classification applies; secure pallets and follow standard cargo handling during transport. |
| Storage | Store Braskem HDPE GF5250 indoors in a cool, dry, well-ventilated area, away from direct sunlight, heat, flames, and ignition sources. Keep containers closed, clean, and undamaged to prevent moisture, dust, or contamination. Maintain ambient temperatures and avoid prolonged UV exposure. Use first-in, first-out stock rotation. Do not store near strong oxidizers or incompatible materials. Protect bags from punctures and stacking damage. |
| Shelf Life | Braskem HDPE GF5250 has indefinite shelf life when stored dry, in original packaging, away from heat, sunlight, moisture, and contaminants. |
Braskem HDPE GF5250 is positioned in downstream injection molding lines where a nominal melt flow rate of 25 g/10 min at 190°C/2.16 kg and a nominal density of 0.952 g/cm³ must align with rapid cycling, thin-wall flow length, and dimensional repeatability. The application scope below is restricted to sectors with documented industrial use of high-flow HDPE injection molding resins: thin-wall food containers, caps and closures, housewares and storage, open-head industrial pails, cosmetic primary packaging, and toys. For each sector, compliance standards, addition ratios, downstream processing parameters, and terminal article types are stated separately. The processing data refer to single-stage injection molding with reciprocating screws of 20–40 D length-to-diameter ratio and general-purpose polyolefin screws with compression ratio 2.5–3.0:1; published data for some article-specific configurations remain limited.
| Downstream sector | Compliance anchor | Qualification method | Numerical boundary |
|---|---|---|---|
| Thin-wall food packaging | FDA 21 CFR 177.1520(c) | EN 1186-1 overall migration | 10 mg/dm² |
| Caps and closures | ASTM D2063-13 | torque retention fixture | gate vestige <0.10 mm |
| Housewares and storage | REACH (EC) No 1907/2006 | ASTM D1693 Condition B | regrind 15–25 wt% |
| Industrial pails | 49 CFR 178.509 | UN 1H2 stack/drop | regrind ≤30 wt% |
| Cosmetic primary packaging | EU 1223/2009 | ISO 22715:2006 | pre-dry 60°C/2 h if RH >60% |
| Toys and consumer goods | EN 71-3:2019+A1:2021 | ASTM F963-17 | filler <5 wt% |
High-cavitation thin-wall injection molding of dairy tubs and food storage containers from GF5250 is executed on electric toggle-clamp machines with clamp force between 1,500 kN and 4,500 kN and injection speed capability above 200 mm/s. Melt temperature is maintained at 190–230°C, while chilled-water mold temperature is held at 10–30°C to force rapid solidification; wall thicknesses in this sector range from 0.45 mm to 0.80 mm, producing flow length-to-wall thickness ratios between 150:1 and 250:1. On production lines, hesitation at the last cavity is the dominant failure mode when first-stage injection pressure drops below 90 MPa; valve-pin delay of 0.2–0.4 s or sequential wall-thickness grading compensates for the melt’s high-flow but fast-freezing character. Holding pressure is maintained at 60–80% of first-stage injection pressure for 0.4–1.2 s to reduce post-mold wall-thickness variation. Food-contact compliance for finished articles is assessed under FDA 21 CFR 177.1520(c) for olefin polymers and Commission Regulation (EU) No 10/2011, with overall migration limit 10 mg/dm² and specific migration verification according to EN 1186-1 and Annex III of the EU measure. The formulation addition ratio for compliant thin-wall stock is typically 2.0–4.0 wt% white or custom color concentrate, 0.5–1.0 wt% slip/antiblock masterbatch containing amide slip agents at active concentrations of 500–1,000 mg/kg, and internal regrind from the same certified feedstock at 10–20 wt%, with regrind limited to 2 heat histories to avoid viscosity shift beyond ±5% of virgin melt flow rate. Terminal finished article types include dairy tubs, deli containers, thin-wall portion cups, and reusable food storage containers.
In closure tooling with 24 to 96 valve-gated cavities, the limiting process variable is not cavity fill but thread-geometry drift caused by non-uniform shrinkage around the cap skirt. Torque retention on 26 mm and 28 mm beverage caps is measured by rotational torque fixtures following ASTM D2063-13; child-resistant closures require additional classification under ASTM D3475-17. Compliance for food-contact closures falls under FDA 21 CFR 177.1520, and pharmaceutical or nutraceutical closures are screened for physicochemical suitability using USP <661.1> plastic material testing where customer specifications require it. Formulation for closure stock includes slip masterbatch at 0.3–0.8 wt% with erucamide active content 5–10%, color concentrate at 1.5–2.5 wt%, antioxidant masterbatch at 0.10–0.25 wt%, and regrind from cold-runner or post-gate waste at up to 20 wt% after grinding through a 60–80 mesh screen. Injection parameters are set at melt temperature 200–230°C, hot-runner manifold temperature 210–240°C, mold temperature 15–25°C, injection velocity 30–80 cm³/s, and holding pressure 40–60 MPa until gate freeze at 0.8–2.5 s. A production-line failure mode is gate vestige height above 0.10 mm, which creates a stress riser and cap skirt cracking under top-load; gate geometry and decompression are adjusted to keep vestige below this threshold. Terminal finished articles include two-piece HDPE beverage caps in 26 mm, 28 mm, and 38 mm dimensions, dairy closure plugs, detergent caps, and pharmaceutical bottle caps.
When GF5250 is used in housewares and storage products, the limiting factors are living hinge durability under repeated thermal cycling and environmental stress-crack resistance in contact with surfactants from dishwasher detergents. Housewares injection molding is characterized by thicker nominal walls from 1.5 mm to 3.0 mm and clamp forces between 1,500 kN and 5,000 kN, depending on shot weight and cavitation. Melt temperature is set at 210–250°C, mold temperature at 20–50°C, and back pressure at 0.5–1.0 MPa to maintain color dispersion without excessive shear heating. Living hinge regions require mold surface temperature near the high end of the range, because demolding below 70°C surface temperature produces stress whitening and reduced hinge flex life. Regulatory compliance for food-contact storage rests on FDA 21 CFR 177.1520 and EU Regulation No 10/2011; for general housewares, REACH Regulation (EC) No 1907/2006 Annex XVII and SVHC screening apply. Addition ratios are 2.0–4.0 wt% color concentrate for opaque goods, 0.2–0.5 wt% UV stabilizer masterbatch for outdoor storage boxes, and 1.0–2.0 wt% antistatic masterbatch where dust adhesion must be reduced; regrind levels of 15–25 wt% are common after in-house grinding and density verification. ESCR performance is routinely assessed by ASTM D1693 condition B at 100% Igepal; published data for GF5250 in end-use color concentrates is limited and must be generated on production sampling. Terminal product types include opaque storage containers, drawer organizers, household baskets, and hangers.
Replacement of lower-melt-flow HDPE with GF5250 in 20–30 L open-head pails shifts the critical risk from short shot to stack-load deformation and handle-latch tearing, because the 25 g/10 min melt flow reduces melt strength in thick bosses. Processing is performed on large injection molding machines with clamp force from 6,500 kN to 12,000 kN, shot weight 600–1,200 g, melt temperature 220–250°C, and mold temperature 15–35°C. Injection pressure is set at 80–120 MPa, with holding pressure at 60–80 MPa maintained until the central gate is sealed; premature holding-pressure release leaves a soft gate zone that fails compression testing under ASTM D642-20 or the UN stack test. Cycle times on production lines are 30–45 s. Formulation addition ratios include UV stabilizer masterbatch at 0.5–1.0 wt% for outdoor storage, color concentrate at 2.0–4.0 wt%, and internal regrind up to 30 wt% only when the regrind’s melt flow rate is measured and confirmed within ±10% of virgin material after drying. Dangerous goods packaging requires certification under UN 1H2 for plastics drums and jerricans, with design qualification according to 49 CFR 178.509 and modal performance tests under ADR 6.1 or the IMDG Code; closure test, drop, leakproofness, hydraulic pressure, and stack tests are conducted on finished pails. A specific operating limitation is that handle-latch and metal-handle bosses in 1.5–2.5 mm wall sections can tear if demolded above 80°C; delayed cooling or post-mold fixturing is required when cycle time is shortened below 30 s. Terminal finished types include 1H2-certified open-head pails for paints, coatings, solvents, food ingredients, and industrial chemicals.
For cosmetic and personal care primary packaging, GF5250 is converted into injection molded jars, compacts, and overcaps where the dominant tests are stress-crack resistance against perfume oils, ethanol-water systems, and silicone emollients. Packaging safety is assessed under EU Regulation (EC) No 1223/2009 for cosmetic products and ISO 22715:2006 for packaging labeling and information; material conformity additionally falls under REACH Regulation (EC) No 1907/2006 Article 33 SVHC communication and FDA 21 CFR 177.1520 for incidental food or mouth contact. Formulation addition ratios are 1.0–2.0 wt% color masterbatch, 1.5–3.0 wt% pearlescent or effect masterbatch, 0.2–0.5 wt% UV absorber masterbatch, and 0.3–0.8 wt% slip/anti-scratch masterbatch; recycled material is excluded from the layer that contacts the cosmetic formulation to control odor and migration. Injection molding for cosmetic articles uses high-gloss mold surfaces from SPI A-1 to SPI B-1, mold temperature 30–60°C to reduce flow marks on thick bosses, melt temperature 200–230°C, injection velocity 20–50 cm³/s, and holding pressure 45–65 MPa. Moisture in effect pigment masterbatches causes splay on the surface if not predried at 60°C for 2 h when ambient RH exceeds 60%; the same limitation applies to cold granulate moved from unheated warehouses into high-humidity molding rooms. Terminal product types include cream jars, compact cases, overcaps for fragrance pumps, and lotion jar caps.
Because toy conversion with GF5250 is constrained less by flow than by trace-element migration and mechanical hazard requirements, production lots must be screened before molding: color masterbatch variation is the primary source of migratable heavy metals in olefin-based toy compounds. Compliance is anchored to EN 71-3:2019+A1:2021 for migration limits of 19 elements, ASTM F963-17 for mechanical and physical safety, and CPSIA Section 101 for lead and phthalate restrictions. Addition ratio for toy stock is 1.5–3.0 wt% color masterbatch, 0.1–0.3 wt% antistatic additive where dust deposition affects visible quality, and 0.05–0.15 wt% nucleating/clarifying masterbatch only when cycle-time reduction is required; fillers are excluded from standard formulations because published comparative data for filled GF5250 under EN 71 impact testing is limited and any mineral filler level above 5 wt% requires end-product verification under the relevant mechanical test. Injection molding uses clamp force 500–2,500 kN, melt temperature 190–220°C, mold temperature 20–40°C, and wall thickness 1.0–2.5 mm. Process limitations include the need to purge conveying zones after colored regrind containing unknown masterbatch sources; production facilities separate virgin toy-grade feedstock from general-purpose regrind to maintain documentation under EN 71 lot traceability. Terminal finished product types include construction blocks, ride-on toy components, outdoor play components, and consumer storage items not intended for food contact.
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Braskem HDPE GF5250 is a high-density polyethylene copolymer supplied as pelletized resin and assigned to blown film, sheet extrusion, and extrusion blow molding. The nominal melt flow rate is 0.25 g/10 min at 190 °C under 2.16 kg as measured by ISO 1133-1:2022; nominal density is 0.952 g/cm³ as measured by ISO 1183-1:2019. Representative mechanical values from current manufacturer data include tensile yield stress of 27 MPa at 23 °C determined by ISO 527-2, flexural modulus of 1,100 MPa determined by ISO 178, and notched Charpy impact of 6.0 kJ/m² at 23 °C determined by ISO 179-1/1eA. The Vicat softening temperature A50 is 128 °C by ISO 306.
The molecular architecture of GF5250 creates a broad molecular weight distribution; the low-molecular-weight fraction limits viscosity at high shear while the high-molecular-weight fraction contributes to extensional strain hardening. The melt flow ratio, interpreted as the ratio of melt flow rate at 21.6 kg to melt flow rate at 2.16 kg at 190 °C, is generally above 18 for this class of material. This shear sensitivity appears as lower backpressure at screw speeds above 60 rpm but stable parison hang time during extrusion blow molding. Published data for the exact molecular weight distribution shape is limited.
Above 230 °C, the high-molecular-weight fraction in GF5250 is susceptible to thermal-oxidative degradation. The practical defect is not gross yellowing but the generation of oxidized gel particles visible as fisheyes in film below 25 µm. Dry-air conveying with a dew point below -40 °C and nitrogen-blanketed hoppers reduce melt-phase oxidation. When melt temperature exceeds 230 °C for more than 3 min, a pressure drop of 5–10 % at the die may indicate chain scission; the affected melt should be purged and the line restarted after lowering barrel temperatures to 215 °C.
On a grooved-feed single-screw extruder with L/D 30:1 and 60 mm screw diameter, GF5250 is processed with zone settings from 160 °C to 220 °C. Feed throat cooling below 45 °C prevents pellet bridging in the grooved section. Screen packs of 60/80/100 mesh create head pressures between 20 MPa and 35 MPa; the melt temperature measured at the adaptor is held at 195–215 °C. Residence time above 220 °C is kept below 5 min to suppress gel formation and molecular weight reduction.
Compared with a medium-melt-index HDPE at 0.45–1.0 g/10 min, GF5250 at 0.25 g/10 min generates higher extruder backpressure and requires a wider die gap for equivalent output. The higher extensional viscosity permits down-gauging from 25 µm to 15 µm with retained tear resistance. On chill-roll sheet lines, lower melt flow reduces wet-out; roll temperatures of 70–90 °C may be required to prevent surface haze. In extrusion blow molding, parison hang strength is higher than grades with melt flow rate above 0.5 g/10 min, which supports integrally blow-molded handles with reduced weld-line thinning.
Blown film lines running GF5250 at a blow-up ratio of 2.5:1 and a frost line height of 8 die diameters produce a stable bubble with thickness variation below ±5 % when die gap is set to 1.2 mm. The melt strength allows draw-down ratios from 15:1 to 25:1 without bubble chatter. Increasing the frost line height to 10 die diameters or raising the die lip temperature above 215 °C reduces orientation but may increase blocking in film wound at high tension. Corona treatment at 40–45 mN/m surface energy is required for lamination or printing adhesion.
| Property | Test method | Representative value | Unit |
|---|---|---|---|
| Melt flow rate, 190 °C/2.16 kg | ISO 1133-1:2022 | 0.25 | g/10 min |
| Density | ISO 1183-1:2019 | 0.952 | g/cm³ |
| Tensile stress at yield | ISO 527-2 | 27 | MPa |
| Tensile strain at break | ISO 527-2 | >600 | % |
| Flexural modulus | ISO 178 | 1,100 | MPa |
| Notched Charpy impact, 23 °C | ISO 179-1/1eA | 6.0 | kJ/m² |
| Vicat softening temperature A50 | ISO 306 | 128 | °C |
For extrusion blow molding, accumulator-head machines with tooling designed for high-molecular-weight HDPE are preferred. A 5 L container requires clamp force of 15–20 t. Because parison swell is higher than for a grade with melt flow rate of 1.0 g/10 min, die pin and bushing diameters are typically reduced by 10–15 %. Melt temperature is maintained at 200–210 °C, and blow pressure is set between 0.6 MPa and 0.8 MPa. Pinch-off flash thickness below 1.5 mm prevents tail fracture and improves weld-line integrity.
Environmental stress cracking resistance measured by ASTM D1693 condition B with 100 % Igepal CO-630 is reported above 50 h for this molecular weight class. This property supports service in detergent bottles, agricultural chemical packages, and geomembrane liners, but no single ESCR value transfers across all pack contents; aggressive aromatic hydrocarbons or ester-based solvents require specific compatibility testing in the filled state.
Sheet extrusion through a polished three-roll stack at 70–90 °C yields sheets with thickness from 0.5 mm to 3.0 mm. Thermoforming of GF5250 sheet is feasible at core temperatures of 125–135 °C; heating below 125 °C causes residual stress and edge tearing, while heating above 135 °C may cause sheet sag. Mold temperature should be maintained at 20–40 °C to avoid post-forming shrinkage above 2 %.
| Parameter | Recommended range | Unit |
|---|---|---|
| Barrel zone settings | 160–220 | °C |
| Adapter and die temperature | 190–210 | °C |
| Melt temperature at adaptor | 195–215 | °C |
| Die gap | 1.0–2.0 | mm |
| Blow-up ratio | 2.0–4.0 | — |
| Frost line height | 6–10 | die diameters |
| Screw speed, 60 mm extruder | 40–80 | rpm |
Although GF5250 is not a primary injection molding grade, it can be injected on machines with accumulator-assisted or screw-injection units when nozzle orifice diameters exceed 2.0 mm. Melt temperature is set at 200–220 °C and mold temperature at 10–30 °C. The low melt flow limits flow length to wall thickness ratios below 200:1 for simple geometries. Published data for thin-wall injection of this specific configuration is limited.
Regrind addition up to 30 % by weight is acceptable if the regrind is dry and free of foreign polymers; higher levels reduce extrudate uniformity and may shift the melt flow rate above 0.30 g/10 min. For applications requiring tight lot-to-lot color consistency, pellet-level homogenization and feed blending are recommended because broad molecular weight distribution can interact with high-shear channels.
Incoming resin inspection should include melt flow rate by ISO 1133-1, density by ISO 1183-1, and moisture content by Karl Fischer titration. A melt flow rate outside 0.22–0.28 g/10 min or density outside 0.950–0.954 g/cm³ indicates off-spec or cross-contaminated material. The lot certificate should also report the yield stress to confirm that no low-viscosity fraction has been introduced.
Film produced at 20 µm thickness shows typical machine-direction tensile strength at break of 50–55 MPa and transverse-direction tensile strength at break of 48–53 MPa according to ASTM D882. Elmendorf tear values are strongly dependent on orientation and film gauge; published data for this specific grade is limited, but high-molecular-weight HDPE generally exhibits machine-direction tear resistance between 0.5 N and 2.0 N at 25 µm.
HDPE GF5250 resists dilute acids, alkalis, and aqueous salt solutions at temperatures up to 60 °C. Strong oxidizing acids, chlorine above 10 ppm, and aliphatic or aromatic hydrocarbons can reduce molecular weight and initiate stress cracking. Containers for bleach or aggressive agricultural formulations should undergo storage tests for at least 90 days at 40 °C using the filled product.
If outdoor storage raises pellet moisture above 300 ppm, drying at 80 °C for 2 h in a dehumidifying hopper dryer is required before extrusion. Direct contact with copper or brass screens at temperatures above 230 °C is avoided to reduce oxidative degradation. Purging with low-viscosity metallocene linear low-density polyethylene can produce channeling; instead, a fractional-melt-index HDPE purge with matched viscosity is recommended. Food-contact compliance should be verified under FDA 21 CFR 177.1520 and EU Regulation 10/2011; published data for repeat-use applications above 70 °C is limited.