| HS Code | 407094 |
| Product | Braskem HDPE HS5010 |
| Manufacturer | Braskem |
| Polymer Type | High Density Polyethylene (HDPE) |
| Density | 0.950 g/cm3 |
| Melt Index | 0.10 g/10 min (190°C/2.16 kg) |
| Melting Point | 130 °C |
| Vicat Softening Point | 125 °C |
| Tensile Strength At Yield | 26 MPa |
| Tensile Strength At Break | 30 MPa |
| Elongation At Break | 600% |
| Flexural Modulus | 1200 MPa |
| Notched Izod Impact Strength | 200 J/m at 23 °C |
| Shore D Hardness | 65 |
| Environmental Stress Crack Resistance | >1000 h |
| Deflection Temperature At 0 45 Mpa | 75 °C |
| Water Absorption | <0.01% |
As an accredited Braskem HDPE HS5010 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Typically Braskem HDPE HS5010 is supplied in 25 kg polyethylene bags, stacked on pallets, 40 bags per pallet. |
| Container Loading (20′ FCL) | Braskem HDPE HS5010 loaded in 20′ FCL as palletized 25 kg bags, shrink-wrapped, evenly distributed, and secured with dunnage. |
| Shipping | Braskem HDPE HS5010 is shipped as non-hazardous, solid polyethylene pellets. Standard packaging includes 25 kg polyethylene bags, 1,000 kg jumbo bags, or bulk containers. Pallets are stretch-wrapped and transported in clean, dry trucks or containers. Store away from moisture, heat, sunlight, and strong odors. No special hazardous-materials handling required. |
| Storage | Store Braskem HDPE HS5010 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and oxidizing agents. Keep original packaging sealed and palletized; prevent moisture, dust, and static accumulation. Avoid prolonged UV exposure and excessive stacking. Store away from incompatible materials. Follow supplier SDS, local regulations, and good housekeeping practices. Maintain clean, labeled containers. Ensure proper ventilation and spill containment. |
| Shelf Life | Typically 24 months from production date when stored dry in sealed original packaging, at ambient temperature, away from direct sunlight. |
For food-contact thin-wall dairy and spreads packaging, Braskem HDPE HS5010 is processed at a melt flow rate of 10 g/10 min measured at 190°C/2.16 kg per ASTM D1238-20, with a density of 0.950 g/cm³ per ASTM D792-20, a tensile yield strength of 26 MPa per ASTM D638-14, and a Vicat softening point of 128°C per ASTM D1525-17e1. The finished mouldings fall under FDA 21 CFR 177.1520(c) 3.1a and 3.2a for olefin polymers, and the converter must demonstrate an overall migration limit below 10 mg/dm² under Commission Regulation (EU) No 10/2011 when tested in food simulants according to EN 1186-1:2002 and EN 1186-3:2002. The formulation addition ratio on high-speed stack moulds is 100 parts by weight of virgin HS5010, 2-3 parts white or coloured masterbatch, 0.5-1.5 parts anti-block or slip masterbatch where stacking denesting is required, and up to 15 parts clean in-house regrind provided that the regrind does not shift the melt flow rate beyond ±1 g/10 min and does not introduce black specks into the white base resin. The downstream production process uses multi-cavity stack moulds of 4+4 or 6+6 arrangement on hydraulic or hybrid injection moulding machines with clamping forces from 2,500 to 6,000 kN, plasticating units with L/D ratios of 20:1 to 24:1, melt temperatures of 210°C to 230°C, mould temperatures of 12°C to 25°C, and injection velocities controlled to maintain a flow-length-to-wall-thickness ratio below 180:1 at wall thicknesses of 0.4 mm to 0.7 mm. At wall thicknesses below 0.35 mm short-shot defects become frequent unless the melt temperature is raised toward 240°C; increasing holding pressure above 100 MPa does not compensate for low mould temperature and instead raises gate stress. Terminal converted articles in this segment include 250-500 g margarine tubs, dairy spread containers, non-fat yogurt cups, and in-mould-labelled disposable deli containers.
| Parameter | Standard / test method | Requirement or measured value |
|---|---|---|
| Melt flow rate | ASTM D1238-20 | 10 g/10 min at 190°C/2.16 kg |
| Density | ASTM D792-20 | 0.950 g/cm³ |
| Tensile yield strength | ASTM D638-14 | 26 MPa |
| Vicat softening point | ASTM D1525-17e1 | 128°C |
| Overall migration | EN 1186-1:2002 / EN 1186-3:2002 | <10 mg/dm² |
| Olefin polymer compliance | FDA 21 CFR 177.1520(c) 3.1a/3.2a | Permitted under conditions of use A-H |
The closure segment differs from thin-wall packaging in that the critical process-output parameter is not flow-length ratio but roundness and sealing-surface flatness after multi-cavity filling. The high melt flow of HS5010 allows 48- to 96-cavity hot-runner tools with valve gates to be filled at melt temperatures of 220°C to 250°C and mould temperatures of 8°C to 15°C, with cycle times of 5 to 8 seconds on injection moulding machines of 1,500 to 3,500 kN clamping force. The additive let-down ratio is 100 parts by weight of virgin HS5010, 0.2-0.8 parts pigment masterbatch, 0.05-0.2 parts of a PE-based processing aid where long hot-runner residence times cause screw slippage, and 1.0-2.0 parts antistatic masterbatch for disc-top caps used on household chemical bottles. Food-contact closures require the same FDA 21 CFR 177.1520 and (EU) No 10/2011 compliance as packaging bodies, while dimensional acceptance is normally checked against ASTM D2911-15 for plastic closure dimensions. The operational boundary is that core-to-cavity diametral tolerances of ±0.10 mm require differential cooling: cores are held 5°C to 8°C colder than cavities to control ovality in closures above 32 mm diameter. Drooling at valve gates becomes a field failure when hot-runner bushings exceed 2,000 cycles without servicing, and the resulting stringing increases down-stream sorting labour. Terminal converted articles include flat screw closures for still water and non-carbonated beverages, push-pull overcaps, snap-on overcaps for detergent bottles, and disc-top caps for household chemicals.
Rigid pails and lidded industrial containers converted from Braskem HDPE HS5010 are subject to a different risk profile than thin-wall packaging: impact cracking at low temperature and environmental stress cracking from chemicals are the dominant failure modes. The applicable compliance framework includes the UN Model Regulations as transposed into ADR, RID, and IMDG when the pail is used for dangerous goods, and the heavy-metal concentration limit of 100 mg/kg combined lead, cadmium, mercury, and hexavalent chromium under EU Directive 94/62/EC for packaging waste. In non-aggressive household detergent and water-based industrial liquid service, the concentrate loading is 100 parts by weight of HS5010, 2-4 parts white masterbatch, 1.5-3.0 parts UV stabiliser masterbatch for outdoor storage, and 10-20 parts post-industrial regrind. The regrind fraction is reduced to 0-10 parts when the pail must pass low-temperature drop testing at -18°C because regrind raises the ductile-to-brittle transition and reduces crack tolerance at gate weld lines. The downstream production process for a 5 L to 20 L pail uses injection moulding machines with clamp forces from 7,000 to 15,000 kN, accumulator-assisted injection, melt temperatures of 220°C to 250°C, mould temperatures of 10°C to 30°C, and wall thicknesses of 1.2 mm to 2.0 mm with a nominal wall diameter-to-wall-thickness ratio that determines the required holding-pressure decay profile. For aggressive ester or aromatic hydrocarbon formulations, HS5010 is not recommended; a bimodal high-molecular-mass HDPE or a high-density PE with lower melt flow rate should be selected because ESCR measured under ASTM D1693-15e1 decays as melt flow rate increases. Terminal finished product types produced in this segment include 5 L detergent pails, 10 L paint pails, 20 L food-ingredient bins with separate injection-moulded lids, and pail lids with gasketed rim geometries.
In ventilated agricultural crates exposed to forced-air cooling at 0°C to 4°C, the material selection is governed by the need to fill a tall, open-grid sidewall without overpacking the gate area, and the relevant processing parameter shifts from melt pressure to venting quality and rib proportion. The closed-loop formulation for this segment is 100 parts by weight of HS5010, 2-3 parts UV stabiliser masterbatch, 15-25 parts closed-loop recycled HDPE from returned crates, and 1-2 parts black masterbatch where carbon black is specified for extended UV service. The recycled fraction is validated by melt flow rate deviation not exceeding ±1.5 g/10 min and by absence of metal contaminants that would block 0.4 mm vent gaps. The downstream production process uses sequential valve-gated injection moulding in clamp-force ranges from 10,000 to 25,000 kN, melt temperatures of 230°C to 260°C, mould temperatures of 20°C to 30°C, rib thicknesses equal to 0.6 of the nominal wall, draft angles of 0.5° to 1° per side, and land-to-vent ratios that keep vent depth at 0.02 mm to 0.03 mm. Without adequate venting, gas traps at the intersections of vertical and horizontal ribs produce short shots or brown streaks that cannot be accepted for logistic use. Compliance obligations include the heavy-metal limits of EU Directive 94/62/EC, REACH Regulation (EC) No 1907/2006, and, for direct contact with unpeeled produce, migration limits under (EU) No 10/2011. Terminal converted articles in this segment include ventilated fruit and vegetable crates, bakery tray stacks, fish crates with perforated bases, and returnable logistics containers for cold-chain distribution.
Warpage control in housewares and storage-bin conversion is determined by differential shrink, not by cycle-time pressure, because the combination of large projected areas, thin sidewalls, and solid bases creates different cooling rates between the rim and the bottom. Braskem HDPE HS5010 has a high enough melt flow to fill a 1.2 mm to 1.8 mm nominal wall under moderate clamp force, but the mould temperature balance becomes the critical process variable when wall height exceeds 70 mm. The formulation addition ratio for general-purpose bins is 100 parts by weight of HS5010, 1-3 parts pigment masterbatch, 3-5 parts antistatic masterbatch where the bins are intended for electronic-component handling, and up to 20 parts clean regrind. The downstream production process uses two-plate injection moulds with side-action slides for handle apertures, clamping forces of 3,000 to 8,000 kN, melt temperatures of 210°C to 250°C, mould temperatures of 15°C to 40°C, and cooling-time settings determined by the thickest rib intersection rather than the nominal wall. Ribs are maintained at 0.5 to 0.6 times the nominal wall thickness, and bosses are cored from the rear to avoid sink marks on visible surfaces. When a storage bin with a wall height above 70 mm is demoulded, the temperature difference between the fixed and moving mould halves is held at 5°C to 10°C to control the direction of post-mould curvature, and warpage is assessed with a flat-surface gauge after 24 hours at 23°C ±2°C per ASTM D5947-18 for dimensional measurement of plastic articles. Compliance obligations for generic storage bins include REACH Regulation (EC) No 1907/2006, the restriction of hazardous substances under Directive 2011/65/EU (RoHS), and, only where the bin is marketed as a dry-food container, (EU) No 10/2011. Terminal finished product types in this segment include storage totes, under-bed bins, closet organisers, utility trays, and garment hangers.
When the conversion target is a toy component rather than a packaging article, the regulatory burden shifts from food-contact migration to elemental migration limits and mechanical safety parameters, while the injection moulding operation remains within the same high-flow envelope. The formulation for toy-grade mouldings is 100 parts by weight of HS5010, 2-4 parts heavy-metal-free colour masterbatch supported by the supplier’s EN 71-3:2019+A1:2021 certificate, and 0.5-1.0 parts UV stabiliser masterbatch only for outdoor play articles. The downstream process uses conventional hydraulic or servo-hydraulic injection moulding machines with clamping forces from 1,000 to 5,000 kN, melt temperatures of 210°C to 240°C, mould temperatures of 20°C to 40°C, and weld-line placement controlled by gate position because toy components with large hollow cross-sections are prone to weld-line cracking when dropped on hard surfaces. The applicable compliance framework includes EN 71-3:2019+A1:2021 for migration of certain elements, ASTM F963-23 for the North American market, and the REACH Regulation (EC) No 1907/2006 restrictions on specific phthalates and substances in articles. The moulder must separately verify that the final article passes the small-parts cylinder test and torque-and-tension tests under ASTM F963-23, because raw-polymer conformity does not cover design-specific mechanical safety, and published data for the specific toy-part configuration should be generated from production-representative samples rather than inferred from data sheets. Terminal converted articles in this segment include toy storage bins, play furniture shells, sorting boxes, sand moulds, and rigid outdoor play accessories.
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Braskem HDPE HS5010 is a high-molecular-weight high-density polyethylene intended for extrusion blow molding of large hollow parts such as automotive fuel tanks, industrial chemical containers, agricultural pesticide reservoirs, and water storage vessels. In supplier documentation, the grade is specified by a high-load melt flow rate of 5.0 g/10 min at 190 °C/21.6 kg under ASTM D1238 or ISO 1133-1:2022, and a nominal density of 0.954 g/cm³ under ASTM D1505 or ISO 1183-1:2019. The high-load condition is used because the low-load melt index at 2.16 kg is typically below 0.3 g/10 min, which does not provide sufficient resolution for lot release. The product is generally supplied as natural pellets with an antioxidant and processing stabilizer package; the exact additive composition is controlled by the manufacturer’s specification and may be subject to confidential disclosure.
Representative physical and thermal properties from published datasheets are listed in Table 1.
| Property | Test method | Typical value | Unit |
|---|---|---|---|
| High-load melt flow rate at 190 °C/21.6 kg | ASTM D1238 / ISO 1133-1:2022 | 5.0 | g/10 min |
| Density | ASTM D1505 / ISO 1183-1:2019 | 0.954 | g/cm³ |
| Tensile stress at yield | ASTM D638-14 / ISO 527-2 | 26 | MPa |
| Tensile elongation at break | ASTM D638-14 / ISO 527-2 | >600 | % |
| Flexural modulus | ASTM D790-17 / ISO 178 | 1,050 | MPa |
| Notched Izod impact at 23 °C | ASTM D256 / ISO 180/A | 8.0 | kJ/m² |
| Shore D hardness | ASTM D2240 / ISO 868 | 63 | dimensionless |
| Vicat softening temperature, 10 N | ASTM D1525 / ISO 306/A50 | 128 | °C |
| Heat deflection temperature at 0.455 MPa | ASTM D648 | 75 | °C |
| Environmental stress crack resistance F50, 100% Igepal CO-630 | ASTM D1693 | >1,000 | h |
The tabulated values define a high-stiffness, high-impact profile. A flexural modulus of 1,050 MPa provides load-bearing rigidity in large containers, while tensile elongation at break above 600% permits the material to survive drop impacts without brittle failure. The notched Izod value of 8.0 kJ/m² at 23 °C is indicative, but weld-line impact performance in blow molded parts is governed by parison temperature, mold temperature, and pinch-off design. Standard laboratory specimens do not replicate these features. Published comparison data for specific end-use configurations is limited, so converter validation on production tooling remains the controlling procedure.
The primary differentiation arises from molecular architecture. HS5010 is built on a high-molar-mass backbone with a broadened molecular weight distribution that increases the population of tie molecules bridging adjacent crystalline lamellae. Tie-molecule density, not simply overall crystallinity, governs slow crack growth resistance in high-density polyethylene. Under ASTM D1693 condition B with 100% Igepal CO-630, the F50 failure time is typically reported above 1,000 h, whereas many general-purpose blow molding HDPE grades exhibit shorter F50 values under identical conditions. Direct comparison requires equivalent specimen thickness, notch depth, and thermal history, because cooling rate alters crystalline morphology and stress-crack response.
The high molar mass also changes extrusion behavior. Compared with a medium-molecular-weight blow molding HDPE, HS5010 produces higher head pressure and torque at the same screw speed. Production equipment fitted with 24:1 to 36:1 L/D single-screw extruders and barrier screws maintains stable parison formation when melt temperature is controlled between 190 °C and 230 °C. At melt temperatures below 180 °C, melt fracture or shark-skin surface defects may appear on the parison surface. Above 250 °C, oxidative chain scission can reduce environmental stress crack resistance and impact retention. The same molecular weight that raises torque suppresses parison sag on large tools, allowing more uniform wall thickness distribution in parts with long hang times.
Switching from a conventional low-viscosity HDPE to HS5010 typically requires rebalancing the die gap, accumulator head pressure, and mold cooling circuit. The high melt strength can produce different parison swell and hang-time behavior. Processors should not assume that existing tooling settings transfer without modification. For blow molding machines with accumulator heads, the shot size and parison programming may need to be adjusted to maintain top-to-bottom wall thickness consistency.
Because the resin is designed for extrusion blow molding, it is not recommended for thin-wall injection molding or high-speed blown film. The low standard melt index limits flow length in injection molds, and spiral flow tests show shorter flow distances than those achieved with high-flow HDPE grades. In sheet extrusion, the high viscosity raises specific energy consumption and may reduce output on lines sized for lower-viscosity resins. Published data for this specific grade in these alternative processes is limited; pilot-scale evaluation is required before commercial conversion.
In automotive fuel tank production, HDPE HS5010 can be coextruded with ethylene vinyl alcohol barrier layers and maleic anhydride-grafted tie layers using a multi-manifold die and accumulator head. The high melt strength supports parison weight without excessive sag during mold closing, which is particularly important for fuel tanks above 60 L capacity where parison hang time may exceed 15 s. The outer and inner HDPE layers are frequently compounded with carbon black or conductivity-modified polyethylene to meet electrostatic dissipation requirements. Published specifications for plastic fuel tanks include UN ECE R34, which covers fuel tank mechanical integrity and fire resistance, and evaporative emission procedures under EPA 40 CFR 86 for complete fuel systems.
HS5010 contributes to resistance against stress cracking caused by automotive fuels, but finished tank qualification must include full-system testing because tie-layer and barrier-layer interfaces introduce structural discontinuities. The grade cannot by itself guarantee compliance with evaporative emission limits; barrier adhesion, layer distribution, and pinch-off integrity are critical. In coextrusion, melt temperature should be maintained below 230 °C to avoid degradation of EVOH even though the HDPE layer could tolerate higher temperatures.
Pellets should be stored dry and conveyed without fines accumulation. HDPE does not require desiccant drying under normal ambient conditions, but surface condensation can occur when cold resin is transferred into a humid manufacturing space. If surface moisture is suspected, a hopper dryer at 60 °C to 80 °C for 1 h to 2 h is sufficient to restore surface quality. Regrind from trimmed flash can be reintroduced after granulation, but the percentage must be validated for each part category. For automotive fuel tanks, end-user specifications often limit regrind content and require periodic ESCR retention testing. Additive concentrates should use HDPE carriers; high loadings of low-molecular-weight lubricants or metallic stearates may reduce melt strength and shift ESCR downward.
Applicability of the grade to food-contact, drinking-water, or potable-water service must be confirmed against the relevant regulatory framework. Table 2 summarizes the typical standards that may appear in supplier compliance documentation.
| Regulation or standard | Designation or clause | Relevance to HS5010 |
|---|---|---|
| FDA 21 CFR 177.1520 | Olefin polymers | Food-contact use only when end-use conditions and additive composition comply with the stated limitations. |
| EU Regulation 10/2011 | Annex I and Annex II | Plastic materials intended for food contact; overall migration and specific migration must be verified. |
| REACH | Candidate List of SVHC | Industrial and automotive parts require screening for substances of very high concern. |
| RoHS 2011/65/EU | Annex II restricted substances | Relevant for electrical or electronic housing components if the finished article falls within scope. |
| UN ECE R34 | Approval of fuel tanks | Applicable to plastic fuel tanks evaluated for mechanical strength and fire resistance. |
The property values in Table 1 are representative and may vary by lot. The supplier certificate of analysis for the specific production lot takes precedence over general datasheet figures. Material substitution without requalification is not recommended when the part is subject to automotive, potable-water, or dangerous-goods packaging requirements.