| HS Code | 681605 |
| Density | 0.958 g/cm³ |
| Specificgravity | 0.958 |
| Meltflowrate | 0.25 g/10 min (190°C/2.16 kg) |
| Highloadmeltflowrate | 25 g/10 min (190°C/21.6 kg) |
| Meltingpoint | 133 °C |
| Vicatsofteningpoint | 127 °C |
| Deflectiontemperatureat0 46mpa | 75 °C |
| Brittlenesstemperature | -70 °C |
| Tensilestrengthatyield | 28 MPa |
| Tensilestrengthatbreak | 30 MPa |
| Elongationatbreak | >600% |
| Flexuralmodulus | 1300 MPa |
| Notchedizodimpactat23c | 200 J/m |
| Environmentalstresscrackresistance | >1000 h |
| Hardnessshored | 66 |
| Comonomer | 1-Hexene |
| Waterabsorption | <0.01% |
| Thermalconductivity | 0.40 W/m·K |
As an accredited Braskem HDPE GM8250T factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Braskem HDPE GM8250T is supplied in 25 kg polyethylene-lined bags, palletized at 1,000 kg per pallet for easy handling. |
| Container Loading (20′ FCL) | 20′ FCL container loading for Braskem HDPE GM8250T: palletized 25 kg bags, securely stowed, moisture-protected, and transport-compliant. |
| Shipping | Braskem HDPE GM8250T ships under normal transport conditions as non-hazardous high-density polyethylene pellets. It is not DOT, IMDG, or IATA regulated. Typical packaging includes 25-kg bags, octabins, bulk trucks, or railcars. Keep dry, clean, and away from ignition sources, UV light, and extreme heat. No special shipping labels or placards required. |
| Storage | Store Braskem HDPE GM8250T in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep original packaging sealed to prevent moisture, dust, and contamination. Avoid extreme temperatures and prolonged UV exposure. Stack pallets securely, ensure good housekeeping, and protect bags from tearing or puncturing. Follow local fire, handling, and environmental regulations. |
| Shelf Life | Shelf life is typically 24 months from production date when stored unopened in original packaging under cool, dry, ventilated conditions. |
In thin-wall dairy and deli container molding, Braskem HDPE GM8250T is processed on high-speed accumulator-assisted injection presses with clamp forces from 2,500 kN to 5,000 kN. The grade is supplied with a nominal density of 0.958 g/cm³ under ASTM D1505 and a nominal melt flow rate of 8.0 g/10 min under ASTM D1238 at 190 °C/2.16 kg, placing it in the high-flow injection-molding segment for thin-wall rigid packaging. Melt temperature is held at 210 °C to 230 °C; mold temperature is set at 10 °C to 20 °C. Cavities with wall thickness from 0.45 mm to 0.80 mm fill through hot-runner valve gates. The narrow molecular weight distribution reduces pressure loss under high shear. Mold-fill analysis on a 32-cavity hot-runner tool shows injection pressures typically below 80 MPa at a flow-length/wall-thickness ratio of 150:1. When wall thickness drops below 0.50 mm, the melt-temperature window narrows to 215 °C ± 5 °C; below 210 °C, short shots occur at the end of flow paths, while above 240 °C the resin yellows and part-weight variation increases after 5 min residence time.
Cooling time controls total cycle time. For a 0.60 mm wall, demolding can occur at 4.5 s to 6.5 s when core cooling water is supplied at 8 °C and the part surface temperature at ejection remains below 70 °C. Regrind content is normally limited to 20 wt% for dairy-container drop-impact retention. Pre-drying is not routinely required because HDPE is not hygroscopic; only when outdoor silo storage creates surface moisture above 0.05% is a hopper dryer at 70 °C for 1 h specified. Food-contact status of the final article rests on FDA 21 CFR 177.1520(c) 3.2b and overall migration limits under EU 10/2011. The converter must validate the specific color concentrate and regrind stream because no universal compliance statement applies when recycled content is introduced. Terminal products are 250 mL to 1,000 mL dairy tubs, deli pots, and frozen-dessert containers.
Closure molding converts GM8250T into continuous-thread caps for non-carbonated and light-carbonated beverages. The process window is narrower than in tub molding because the tamper-evident band must be slit immediately after ejection without tearing. Melt temperature is set between 220 °C and 235 °C; mold temperature is held at 8 °C to 15 °C to control ovality. Typical cap wall thickness is 0.80 mm to 1.60 mm. High-cavitation tools with 48 or 64 cavities require balanced melt delivery; valve-gate hot runners with gate vestige below 0.10 mm are specified for beverage closure appearance. Cycle time is usually limited by cooling of the bridge between shell and tamper ring. At 0.90 mm nominal wall, demolding temperatures below 70 °C are required before slitting; premature slitting at higher temperature produces ragged tamper bands and latent hinge cracks.
Slip additives are introduced at 0.05 wt% to 0.15 wt% erucamide or oleamide to reduce removal torque. Overdosing above 0.20 wt% creates plate-out on cores and increases stress cracking at the hinge. Underdosing below 0.03 wt% raises removal torque above 2.0 N·m on 28 mm PCO 1881 finishes. Closure application torque on filling lines is typically 1.5 N·m to 2.5 N·m; higher torque fractures the tamper ring. Torque retention after 24 h at 23 °C is evaluated according to ASTM D2063. A torque loss above 20% indicates neck-finish dimensional mismatch or excessive slip migration. Published data for this specific grade in recycled-content closures above 25% is limited; each converter must validate torque decay under filled-product storage. Terminal parts are tamper-evident beverage caps for water, juice, and carbonated soft-drink applications.
Open-top pails from 5 L to 20 L molded from GM8250T are used for paints, lubricants, water-based coatings, and non-aggressive chemical formulations. Melt temperature is set at 220 °C to 250 °C with mold temperatures between 20 °C and 40 °C; wall thickness ranges from 1.8 mm to 3.2 mm. A 20 L pail typically requires clamp force from 8,000 kN to 12,000 kN depending on projected area and hot-runner pressure drop. Handle ears and rim are integrally molded. Rim dimensions must remain stable to allow lid seal under stacked load. Warpage is controlled by balanced cooling and by holding packing pressure at 35 MPa to 55 MPa for 5 s to 12 s after fill.
UN hazardous-material packaging requires the pail to pass pressure stacking, drop, and leakproofness testing under the applicable code. A common classification is UN 1H2/Y1.5/100 for a 1.5 relative-density liquid at 100 kPa vapor pressure. Molded pails are drop-tested at -18 °C after conditioning. Drop height is 1.2 m for packing group II and 1.5 m for packing group I when specified. This places environmental stress-cracking resistance and low-temperature impact resistance in the critical path. ESCR is characterized by ASTM D1693, condition B, in 10% Igepal CO-630. Converters should verify ESCR on the actual pail wall because orientation and cooling rate shift the failure mode from craze to crack. GM8250T is not intended for sustained outdoor UV exposure without carbon black or UV stabilizer; unstabilized pails exposed to sunlight for 12 months lose impact retention and show surface chalking. Terminal products include 5 L paint pails, 10 L lubricant containers, and 20 L industrial open-top pails.
Where storage articles require moderate impact resistance, high stiffness, and fast molding, GM8250T is converted into housewares, totes, bins, hangers, and drawer organizers. Melt temperature is set between 200 °C and 230 °C for wall thicknesses of 1.5 mm to 4.0 mm; mold temperatures of 30 °C to 50 °C are used to reduce sink marks at bosses and ribs. Regrind content can reach 25 wt% in non-load-bearing articles if the regrind is dry and free of contamination. Color concentrate addition is typically 2 wt% to 4 wt%. Loadings above 5 wt% reduce impact strength and require a letdown ratio compatibility check. Consumer goods shipped into the EU must comply with REACH EC 1907/2006 SVHC limits of 0.1 wt% per substance and RoHS 2011/65/EU restricted metals including lead at 1000 mg/kg and cadmium at 100 mg/kg. Terminal parts include stackable storage crates, utility baskets, and thin-wall hangers with flow marks controlled by high injection speed.
Decorating GM8250T parts with UV-curable ink jet on packaging lines introduces surface-energy constraints that are not present with in-mold labels. Untreated HDPE exhibits surface energy near 31 mN/m; UV ink systems generally demand 38 mN/m or higher for wetting and adhesion under ASTM D3359 tape-pull testing. Corona discharge at 0.5 kW to 1.0 kW and line speed of 15 m/min to 30 m/min raises surface energy to 42 mN/m to 48 mN/m. Treatment decays within 30 days, so parts must be decorated within the validated treatment window. Plasma treatment is specified where three-dimensional surfaces create shadow areas that corona electrodes cannot reach.
Adhesion loss is accelerated by slip additive migration. When closure or pail formulations contain erucamide above 0.10 wt%, UV ink adhesion fails at the interface after 14 days at 40 °C. The converter should either reduce slip additive concentration for decorated surfaces or select a cationic UV ink with acid-modified adhesion promoters. No post-cure annealing above 50 °C is required for HDPE, but parts must be dry. This decorating route is used for coded pails, dairy tub lids, and custom-label storage boxes.
The matrix below consolidates the controlling standards and operational limits applied across the above application tracks.
| End-use track | Controlling standard | Critical control point | Typical limiting value |
|---|---|---|---|
| Thin-wall dairy containers | FDA 21 CFR 177.1520(c) 3.2b; EU 10/2011 | Melt temperature | 210 °C–230 °C |
| Tamper-evident closures | ASTM D2063 | Slip additive content | 0.05–0.15 wt% |
| Industrial pails | UN 1H2/Y1.5/100; ASTM D1693 | Drop test temperature | -18 °C |
| Housewares | REACH EC 1907/2006; RoHS 2011/65/EU | SVHC content | 0.1 wt% |
| UV ink jet decoration | ASTM D3359 | Surface energy | 38 mN/m |
| Masterbatch carrier | EN 13900-5 | Filter pressure value | 2.5 MPa/g |
GM8250T is also consumed as a carrier resin in color and additive masterbatches where a high-flow HDPE matrix is required for pigment wetting and rapid pelletizing. The carrier is compounded on twin-screw extruders with L/D ratios from 32:1 to 44:1 at barrel temperatures between 160 °C and 190 °C. Pigment loading is typically 40 wt% to 60 wt% for inorganic systems such as titanium dioxide and iron oxide; organic pigments are loaded at 20 wt% to 40 wt% with wax dispersants at 5 wt% to 15 wt%. Dispersion quality is checked by filter pressure rise per EN 13900-5. A filter pressure value below 2.5 MPa/g is a common acceptance target for injection and film letdowns. The grade’s thermal stability above 250 °C is limited, so compounding zones are not run in high-shear conditions beyond 190 °C.
Recyclate integration into injection-molded HDPE parts is constrained by the grade’s melt flow stability. Post-consumer HDPE with a melt flow rate below 4 g/10 min can increase injection pressure and enlarge part weight variation when added above 15 wt%. Blends with 20 wt% clean post-industrial regrind are generally used only after melt filtration at 120 µm and a melt temperature of 220 °C. Food-contact containers require a positive list and functional barrier assessment under EU 10/2011 if recycled content is used. Terminal products include masterbatch pellets and industrial components with conservative recycled-content ratios.
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Braskem HDPE GM8250T is specified as a high-molecular-weight high-density polyethylene copolymer intended for extrusion blow moulding of large-volume containers, automotive fuel tanks, and industrial packaging. The product is polymerised by a suspension process; technical bulletins list density at 0.956 g/cm³ under ASTM D792 and melt flow rate at 0.25 g/10 min at 190 °C/2.16 kg under ASTM D1238. Reported mechanical data from compression-moulded specimens include tensile yield strength of 28 MPa under ASTM D638, elongation at break exceeding 800% under ASTM D638, flexural modulus of 1400 MPa under ASTM D790, and notched Izod impact of 9 kJ/m² at 23 °C under ASTM D256. Vicat softening temperature is reported at 128 °C under ASTM D1525 and Shore D hardness at 63 under ASTM D2240. These values define a stiff HDPE with ductile failure under impact; however, published data for this specific configuration is limited to producer datasheet ranges, and converters should request certified lot-specific values before tooling design.
| Property | Typical value | Test standard |
|---|---|---|
| Density | 0.956 g/cm³ | ASTM D792 |
| Melt flow rate | 0.25 g/10 min | ASTM D1238, 190 °C/2.16 kg |
| Tensile strength at yield | 28 MPa | ASTM D638 |
| Elongation at break | >800% | ASTM D638 |
| Flexural modulus | 1400 MPa | ASTM D790 |
| Notched Izod impact at 23 °C | 9 kJ/m² | ASTM D256 |
| Vicat softening temperature | 128 °C | ASTM D1525 |
| Shore D hardness | 63 | ASTM D2240 |
| Environmental stress crack resistance | Producer certificate required | ASTM D1693 condition B |
| Melt temperature, DSC | 134 °C | ASTM D3418 |
Compared with higher-melt-index HDPE blow moulding grades in the 0.7 g/10 min to 1.0 g/10 min MFI band, GM8250T displays lower melt fluidity and higher zero-shear viscosity. This leads to higher extruder torque and lower output per screw revolution. In a 90 mm single-screw extruder with 24:1 L/D, processors often observe a 15–25% reduction in throughput compared with a 0.7 g/10 min grade at equal screw speed and barrel settings. The higher melt strength resists parison sag, so the grade is suited to containers above 60 L; a lower-viscosity grade may show unacceptable top-to-bottom wall thinning under the same die gap and clamp cycle. The molecular architecture also shifts failure response: high molecular mass and controlled comonomer placement reduce slow crack growth under ASTM D1693 condition B, whereas lower-molecular-mass grades often show shorter F50 times in identical moulded plaques. The trade-off includes lower melt fluidity, potentially higher die swell, and increased susceptibility to melt fracture if the die lip shear rate exceeds 1,000 s⁻¹. Published quantitative ESCR data for this specific configuration is limited and should be obtained from the producer for the target wall thickness and container size.
Extrusion blow moulding of GM8250T is performed on single-screw extruders with 24:1 to 30:1 L/D and compression ratios of 2.5:1 to 3.5:1. Barrel temperature profiles from feed to metering are typically set at 170 °C, 180 °C, 190 °C, 200 °C, and 210 °C; die head zones are held at 190–220 °C. Melt temperature at the die entry should remain within 180–220 °C. Screw speed is adjusted to maintain melt pressure at the adapter between 20 MPa and 35 MPa; higher head pressure may indicate underheated feed or insufficient decompression. Blow-up ratio is normally 2:1 to 3:1, mould temperature 15–40 °C, and blowing pressure 0.7–1.0 MPa. Accumulator-head machines are preferred for large parts because they deliver a pre-weighted shot via a plunger and reduce melt holdup time. Wall-thickness programming is required above 60 L; parison profiles should compensate for die swell and parison sag, and wall-thickness variation is monitored by ultrasonic scanning with 0.01 mm resolution. Back pressure below 20 MPa is recommended to control shear heating. If pellet surface moisture exceeds 0.1% by Karl Fischer titration, drying at 80 °C for 1 h is applied; open-silo storage at relative humidity above 60% can introduce surface condensation. Regrind addition up to 30 wt% is typical in industrial blow moulding; higher regrind fractions increase gel and black-spec frequency and reduce ESCR.
For applications involving aggressive hydrocarbons, surfactants, or acidic drum contents, ESCR is the controlling property. GM8250T’s high molecular weight and comonomer distribution are intended to shift failure from brittle crack propagation to ductile yielding under ASTM D1693 condition B or C. However, ESCR is not an intrinsic resin property alone; it depends on moulded-in stress, pinch-off weld cooling history, wall thickness, and test temperature. Converters should commission plaque tests at the intended wall thickness and specified stress level. The grade is also susceptible to oxidative degradation if combined with amine-based processing stabilisers in non-compatible additive masterbatches; such additives may accelerate surface yellowing and reduce slow crack resistance. The use of phenolic/phosphite stabiliser systems is standard, but the final stabiliser package must be confirmed with the producer. In large-part fuel tank tooling, melt flow after pinch-off is limited; weld lines should be interrogated by cut-out tensile tests and drop impact at −20 °C to ensure the part exceeds the minimum specified energy.
Pinch-off weld integrity in large containers is governed by melt temperature at the moment of mould closure, clamp tonnage, and pinch-off insert geometry. In production-scale accumulator blow moulding, the clamp force must exceed the mould surface area multiplied by the internal blowing pressure, typically 0.7–1.0 MPa; insufficient clamp force opens the mould and produces flash at the parting line. The pinch-off insert angle is generally machined to 30–45° to induce a localised high-pressure zone without severing the parison too early. GM8250T’s high molecular weight increases melt elasticity and can cause the pinch-off weld to remain below the melting temperature if the mould temperature is kept below 15 °C; this generates a semicrystalline seam with lower ESCR. Therefore, mould temperature 20–40 °C is preferred for large parts. Weld integrity is quantifiable by cutting ASTM D638 Type IV tensile bars from the pinch-off seam and comparing yield strength to the parent wall; retention below 80% indicates excessive cooling or insufficient melt temperature.
Compliance of GM8250T with food-contact requirements can be declared under FDA 21 CFR 177.1520 when the finished article is produced within the producer’s recommended conversion window; however, overall migration testing under EC 10/2011 or FDA protocols remains the responsibility of the converter because end-use contact time and temperature alter extractives. The grade is not supplied with a UV stabiliser package; unprotected outdoor exposure leads to surface chalking and tensile impact loss in accelerated weathering under ASTM G154. For black parts, carbon black masterbatch addition at 2–3 wt% is typically required to achieve service life beyond 12 months in direct sunlight. RoHS and REACH statements are document-controlled and available from Braskem technical service. The product should not be blended with polypropylene or heterogeneous plastomers in regrind streams without melt compatibility trials because phase separation at the blow moulding die can generate weld-line delamination.