| HS Code | 293714 |
| Product | Braskem HDPE BS002W |
| Polymer Type | High Density Polyethylene (HDPE) |
| Form | Pellets |
| Density | 0.952 g/cm³ |
| Melt Flow Index 190 C 2 16 Kg | 0.20 g/10 min |
| Tensile Strength At Yield | 26 MPa |
| Tensile Strength At Break | 32 MPa |
| Elongation At Break | >600% |
| Flexural Modulus | 1300 MPa |
| Escr 10 Igepal F50 | >1000 h |
| Vicat Softening Temperature | 126°C |
| Melting Point | 131°C |
| Hardness Shore D | 65 |
| Brittleness Temperature | < -70°C |
| Recommended Processing Temperature | 180-220°C |
As an accredited Braskem HDPE BS002W factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Braskem HDPE BS002W is packaged in 25 kg polyethylene bags, palletized and stretch-wrapped for secure transport and handling. |
| Container Loading (20′ FCL) | Braskem HDPE BS002W is supplied in 25 kg bags, palletized, stretch-wrapped, and loaded into a 20′ FCL for ocean transport. |
| Shipping | Braskem HDPE BS002W is a non-hazardous polyethylene resin, typically shipped in 25 kg bags, jumbo bags, octabins, or bulk trucks/railcars. Transport in clean, dry vehicles/containers. Avoid moisture, heat, sunlight, and contamination. Not classified as dangerous goods; no UN number, placards, or special transport documentation required. |
| Storage | Store Braskem HDPE BS002W (high-density polyethylene) in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep original packaging sealed, off the floor, and protected from moisture, dust, and contaminants. Avoid prolonged UV exposure and extreme temperatures. Maintain good housekeeping, stack pallets safely, and follow local storage regulations. |
| Shelf Life | Typically 12 months when stored unopened in its original packaging, in a cool, dry, ventilated area away from direct sunlight. |
In the extrusion blow molding of UN-certified 10–60 L high-density polyethylene jerricans, Braskem HDPE BS002W is processed as a high-molecular-weight blow molding grade whose parison hang strength and die swell fall within ranges suitable for 1H1 open-top drums and 3H1 jerrican bodies under UN Model Regulations Chapter 6.1 type-approval. The material is extruded on continuous shuttle machines or accumulator-head machines with screw L/D ratios between 24:1 and 32:1, barrier screws with Maddock mixing sections, melt temperatures of 180–220 °C, die temperatures held within ±5 °C of 190 °C, and die gaps of 1.8–2.8 mm. Mold temperature is maintained at 10–30 °C, blow air pressure at 0.6–1.2 MPa, and clamp force on 20 L tooling is typically 30–60 t. Parison programming of 10–25% is applied to compensate for container wall thickness variation in the top, sidewall, and pinch-off regions, while post-mold cooling of 12–20 s per 1 L of container volume prevents deformation during hydraulic leak testing. Standard formulation uses 100 parts virgin BS002W with 20–35 parts of in-house regrind from the same production campaign, 1.5–2.5 wt% carbon black or UN-approved pigment masterbatch, 0.05–0.10 wt% hindered phenolic antioxidant, and 0.03–0.08 wt% phosphite secondary stabilizer. When outdoor storage is required, UV stabilizer addition of 0.15–0.35 wt% HALS is incorporated. Moisture content of regrind before hopper entry is held below 0.05 wt% to avoid splay and weld-line weakness.
Type-approval tests under the UN Manual of Tests and Criteria Part III sections 31–33 include drop heights of 1.2–1.8 m depending on filling density, stack load equivalent to 6 months at 40 °C, and hydraulic internal pressure of 100 kPa for 30 min. In North America, 49 CFR §178.509–178.512 governs design qualification for non-bulk packagings; finished container wall thickness is verified by magnetic or eddy current gauges, with minimum wall thickness not less than 1.0 mm for 20 L jerricans. Terminal product types include 5 L solvent cans, 10 L, 20 L, and 25 L UN 3H1 jerricans, 60 L 1H1 open-top drums, and 20 L stackable pails for cleaning agents, solvents, and bulk chemical distribution. Published data for BS002W-specific hydraulic pressure retention at −18 °C drop conditions is limited; low-temperature performance must be batch-tested because HDPE exhibits a ductile-brittle transition near −60 °C, but weld lines can fail earlier under high-rate impact in chilled containers.
Specifications for agricultural chemical containers routinely impose environmental stress crack resistance thresholds under ASTM D1693 condition B using 100% Igepal CO-630 at 50 °C, with acceptance criteria often set at F50 ≥ 300 h for 0.8–1.2 mm sidewall sections. Braskem HDPE BS002W is blow molded into narrow-neck bottles for pesticide and herbicide concentrates where the packaging must resist solvent-induced microcracking, creep rupture, and drop impact after prolonged storage. In compounding, additive loading is held within narrow windows: 0.05–0.12 wt% primary antioxidant, 0.03–0.08 wt% secondary phosphite, 0.05–0.10 wt% zinc stearate acid scavenger, and 0.15–0.30 wt% HALS/UV package for UV-protected formulations. External mold release agents are excluded from the bottle inner surface because trace residues can alter surface stress-cracking initiation; silicone-containing regrind is rejected by FTIR screening if silicon concentration exceeds 200 ppm. Processing on 20:1–30:1 L/D reciprocating screw blow molders with 50–75 rpm screw speeds, melt temperature 190–215 °C, die gap 1.5–2.5 mm, and mold cooling 10–30 °C yields parison swell in the 55–80% range. A separate 0.3–0.5 MPa pre-blow is used to distribute wall thickness before final 0.6–1.0 MPa blow air. Weld-line integrity at the pinch-off is inspected by polariscope and notched tensile impact testing under ASTM D1822, with individual lot rejection when sidewall break strain falls below 300% under ASTM D638 at 23 °C.
| Additive function | Loading window in HDPE BS002W | Process control parameter | Test method |
|---|---|---|---|
| Primary antioxidant | 0.05–0.12 wt% | Melt temperature 190–215 °C | ASTM D3895 OIT |
| Secondary phosphite | 0.03–0.08 wt% | Residence time <5 min | ASTM D1238 MFR shift |
| HALS/UV package | 0.15–0.30 wt% | Hopper moisture <0.05 wt% | ASTM D4329 UV exposure |
| Zinc stearate | 0.05–0.10 wt% | Die lip plate-out <0.2 mm | ASTM D1693 ESCR |
| Pigment masterbatch | 1–3 wt% | Parison swell 55–80% | ASTM D2244 color |
Compliance for hazardous agrochemical formulations includes the same UN/ADR packaging certification as in jerrican stock, plus FAO/WHO guidance on pesticide storage and 40 CFR 156.140 for US FIFRA label compliance when the container is entry packaging. For non-hazardous products, the material is qualified under EC 1272/2008 classification and labeling requirements. Terminal product types include 250 mL, 500 mL, 1 L, 5 L, and 10 L high-density polyethylene bottles for organophosphate, pyrethroid, and glyphosate formulations, including induction-sealed narrow-mouth packs. Published data for BS002W-specific ESCR performance in high-ionic-strength ammonium sulfate formulations is limited; filled-container compatibility tests under 40 °C and 90% RH are required before specification release.
For cosmetic and personal care wall bottles in the 150 mL–1 L band, Braskem HDPE BS002W is used with post-consumer recyclate at 20–45 wt% in blow molding plants operating 18:1–25:1 L/D single-screw extruders. Melt temperature is controlled at 190–210 °C, die gap at 1.2–2.0 mm, and mold temperature at 10–20 °C to preserve surface gloss on polished cavities. Addition rates are 20–45 parts PCR, 1.5–3.0 wt% white or colored masterbatch, 0.05–0.10 wt% antioxidant, and 0.02–0.08 wt% external lubricant. When PCR is introduced, pre-drying at 70–80 °C for 2–4 h is applied when ambient relative humidity exceeds 60%, with hopper residence time limited to prevent thermal degradation that raises melt flow rate and reduces parison strength. Material compliance is evaluated under EC 1223/2009 for cosmetics packaging and, where the same bottle is used for oral care products, EU 10/2011 and FDA 21 CFR 177.1520 migration limits apply. The recycled fraction must comply with EU 2022/1616 for food-contact recycled plastics only if the article is marketed for food contact; for cosmetics, PCR quality is specified by internal optical defect limits of no more than 0.3% gel content and no more than 5 mm² of black specks per 1,000 bottles. Batch-to-batch variation in PCR melt viscosity alters die swell and pinch-off strength; therefore, extrusion speed is adjusted within ±5 rpm and parison programming within ±2% to maintain wall thickness at 0.6–1.0 mm. Leak testing is performed at 20–40 kPa over 5–10 s on finished containers. Terminal product types include 200 mL and 500 mL shampoo, conditioner, body wash, and lotion bottles, and 1 L refill bottles with HDPE necks. Published data for BS002W-specific PCR compatibility at PCR content above 50% is limited; plants typically validate each PCR supplier through torque retention, drop, and ESCR testing per ASTM D1693.
The production of 5–20 L diesel exhaust fluid refill packs from Braskem HDPE BS002W requires stringent control of leachable organics, trace-metal contamination, and no-compromise weld-line integrity because urea solutions of 32.5 ± 0.7 wt% are sensitive to packaging-derived contaminants. ISO 22241-3 material compatibility criteria and ISO 22241-1 solution quality boundaries are referenced during resin and bottle qualification. Formula composition is limited to 0.05–0.10 wt% phenolic antioxidant, 0.03–0.08 wt% phosphite stabilizer, 0.03–0.06 wt% acid neutralizer, and 0.5–1.5 wt% blue or white DEF masterbatch. Recycled content is not permitted in the internal layer unless it has been tested for leachable formate, aldehyde, and metal ions. Calcium stearate is excluded because insoluble residues may plug SCR dosing filters; use of zinc stearate above 0.1 wt% is also avoided. Blow molding of 10 L DEF bottles is performed on accumulator-head machines with 24:1–32:1 screw L/D ratios, melt temperatures of 180–210 °C, die gaps of 1.8–2.5 mm, and mold cooling at 10–25 °C. Internal parison cooling with 0.2–0.4 MPa dry air shortens cycle time by 15–20% and reduces post-mold shrinkage variation. Critical process windows include parison temperature deviation no greater than ±3 °C across the circumference, because uneven temperature shifts wall thickness and can produce thin bands below 0.8 mm; non-contact infrared thermography is used at the die exit for real-time monitoring. Welded spout and handle pinch-offs are subjected to 40–60 kPa leak tests and 1.0 m drop tests at room temperature and at −20 °C. Terminal product types include 1 L and 2 L dosing bottles, 5 L and 10 L DEF refill containers with 19 mm vented caps, and 20 L closed-loop system totes for agricultural machinery and heavy-duty commercial vehicle fleets. Direct gasoline or diesel fuel storage in monolayer HDPE is outside the operational envelope without sulfur trioxide fluorination or EVOH/PA barrier inserts because hydrocarbon permeation limits under CARB LEV III and EPA Tier 3 are not met by monolayer HDPE alone.
When 1–5 L high-density polyethylene oil bottles are produced on 20:1–28:1 L/D reciprocating blow molding machines, Braskem HDPE BS002W is formulated with 15–30 wt% in-plant regrind, 1.5–2.5 wt% colorant masterbatch, 0.05–0.10 wt% primary antioxidant, and 0.03–0.06 wt% phosphite stabilizer. Melt temperature is held at 190–220 °C, die gap at 1.5–2.5 mm, mold temperature at 10–30 °C, and blow air at 0.6–1.0 MPa. The process window for parison programming is set at 10–30% to account for multi-axis wall thickness variation; bottles are leak-tested at 30–50 kPa. Distribution qualification uses ASTM D4169 truck profile and ISO 2248 drop testing. Containers for non-hazardous engine oils follow GHS labeling requirements under OSHA 29 CFR 1910.1200 and EU CLP 1272/2008; hazardous coolants or antifreeze in larger than 5 L may require UN packaging if assigned to packing group II or III. The HDPE material for incidental food contact is not required unless edible oil is packed, in which case FDA 21 CFR 177.1520 and EU 10/2011 apply. Terminal product types include 1 quart (946 mL), 4 L, and 5 L motor oil bottles with offset neck finishes, 1 L and 2 L coolant bottles with 38 mm closures, and 20 L industrial lubricant pails. Antifreeze containing monoethylene glycol exerts lower environmental stress-cracking stress than aromatic solvents; however, continuous hot-fill above 60 °C is not recommended for monolayer HDPE bottles because top-load and volume expansion under stack load can exceed 2%.
Pharmaceutical and nutraceutical HDPE jars produced by blow molding of Braskem HDPE BS002W are evaluated under USP <661.1> and USP <661.2>, European Pharmacopoeia monograph 3.1.3 for polyolefins, FDA 21 CFR 177.1520 when used as a food contact article for dietary supplements, and ICH Q3D for elemental impurities where applicable. Because these packages contact dry oral dosage forms or vitamin tablets, the masterbatch and additive package is constrained to 0.05–0.10 wt% antioxidant, 0.03–0.06 wt% processing stabilizer, and 0.5–1.5 wt% white pigment masterbatch. No slip additives, no antistatic agents, and no recycled material are introduced in the internal layer to keep extractable organics below monograph limits. Batch changeover procedures include purge verification by melt flow rate and colorimetric reading before start-up. Processing on injection blow molding and extrusion blow molding lines with 20:1–25:1 L/D screws, melt temperature 180–210 °C, die temperature 185–205 °C, and mold cooling at 10–25 °C produces 30–500 mL jars with sidewall thickness 0.6–1.0 mm and smooth internal surfaces. Clamp force on 100 mL four-cavity tooling is typically 20–40 t, with blow air at 0.7–1.0 MPa. Preform temperature uniformity is checked with infrared thermal imaging; deviation greater than ±2 °C across the preform requires process interruption because thread dimensional stability and sidewall thickness distribution are affected. Terminal product types include 30 mL, 60 mL, 100 mL, 250 mL, and 500 mL lightweight pharmaceutical bottles, vitamin and mineral supplement jars, induction-sealed dry powder bottles, and child-resistant closure-compatible neck finishes. Published data for BS002W-specific extraction profiles under USP <661.1> for water, alcohol, or hexane simulants is limited; final qualification is performed on the finished bottle with the exact colorant and closure system. Liquid oral syrups require an additional FDA food contact approval and oxygen barrier evaluation when shelf life exceeds 18 months.
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Braskem HDPE BS002W is a high-density polyethylene extrusion blow moulding resin supplied as natural-white pellets for rigid container manufacture. The BS002W designation identifies the grade within the Braskem HDPE blow moulding portfolio, and published technical documentation associates the material with water, diluted household chemical, edible oil, and juice containers between 250 mL and 5 L. The nominal density is 0.954 g/cm³ when measured by ISO 1183-1:2019, and the melt flow index is 0.20 g/10 min under 190 °C and 2.16 kg load in accordance with ISO 1133-1:2022. Top-load performance in filled-container compression is evaluated under ISO 12048:2016, and drop impact resistance of finished bottles is assessed by ASTM D2463-15 at 0 °C or 4 °C, depending on the filling-line specification.
The grade belongs to the high-molecular-weight segment of high-density polyethylene, where low melt flow index and moderate density combine to produce high parison melt strength during extrusion blow moulding. The density of 0.954 g/cm³ and melt flow index of 0.20 g/10 min place the resin among medium-toughness HDPE blow moulding grades rather than ultra-high-stiffness injection grades. The stabilisation package contains a phenolic primary antioxidant and a phosphite processing stabiliser. The additive system is supplied without bisphenol A. In cyclic processing, the phosphite is consumed at the die head by reaction with hydroperoxides. When regrind exceeds 30% by weight, the active antioxidant residual may become insufficient to prevent melt flow drift. Converters should verify melt flow index after 3 consecutive extrusion cycles using ISO 1133-1:2022; an increase above 0.10 g/10 min relative to virgin pellets indicates over-use of regrind or excessive melt residence time. Such drift reduces parison melt strength and environmental stress crack resistance in the final container.
Table 1 lists typical lot-to-lot data from manufacturer-published documentation. The values are not product release limits and are not to be used for article specification without verification on the actual conversion line.
| Property | Test Standard | Unit | Typical Value |
|---|---|---|---|
| Melt flow index, 190 °C/2.16 kg | ISO 1133-1:2022 | g/10 min | 0.20 |
| Density at 23 °C | ISO 1183-1:2019 | g/cm³ | 0.954 |
| Tensile stress at yield | ISO 527-2:2012 | MPa | 27 |
| Elongation at break | ISO 527-2:2012 | % | >800 |
| Flexural modulus | ISO 178:2019 | MPa | 1100 |
| Vicat softening temperature A50 | ISO 306:2022 | °C | 127 |
| Environmental stress crack resistance, Condition B 10% Igepal CO-630, F50 | ASTM D1693-15ε1 | h | >600 |
In intermittent blow moulding, the extruder refills an accumulator, and the melt is discharged by a plunger at high shear rate. The parison sag observed with 0.20 g/10 min grades is governed more by melt temperature than by screw speed. For a 65 mm grooved-feed extruder with a 24:1 L/D ratio, barrel set points from 170 °C at the feed throat to 200 °C at the head are commonly used. When the measured melt temperature at the die exceeds 220 °C, oxidative chain scission increases melt flow and parison draw-down. When the melt temperature falls below 175 °C, sharkskin melt fracture appears on the outer parison surface. Die swell is typically 45% to 65% under practical die gaps. The die land length is therefore maintained at 12–15 times the die gap to stabilise melt memory and reduce wall-thickness variation.
Tooling configuration for handleware containers using BS002W requires a diverging die bushing with included angle of 30° to 45°. A converging die with land length below 8:1 produces melt fracture and uneven parison wall distribution. Parison programming is required when the container length-to-diameter ratio exceeds 3:1. Axial wall thickness control should use a 100-point wall thickness profile or the machine-specific equivalent. At the shoulder and handle weld, the programmed wall thickness is increased by 15–20% relative to the body wall. The die gap is initially set at 1.2–1.8 mm for a target wall thickness of 0.8–1.2 mm. A die gap below 1.0 mm produces high shear heating and oriented skin layers that increase top-load but reduce stress crack resistance. In top-load testing per ISO 12048:2016, compression speed is set at 20 mm/min; the first peak load is recorded as container column strength.
On continuous shuttle blow moulding lines, screw speed is limited by shear heating. At screw rotation rates above 60 rpm, head pressure can rise to 25–35 MPa during refill, and melt temperature can increase by 3–5 °C per 10 rpm increment above 50 rpm. Back pressure is set at 5–10 bar rather than increasing screw speed to maintain cycle time. Pre-drying is required only when hopper residence exceeds 6 h at relative humidity above 60%; moisture should be reduced below 0.02% by weight with a desiccant dryer at 80 °C for 2 h. The grade should not be blended with amine-based processing aids or high levels of unsaturated elastomers because the resulting melt instability can produce odour and inconsistent die swell. For coloured bottles, masterbatch addition at 2 wt% with a melt flow index above 5 g/10 min reduces pigment streaks in the parison.
The shear viscosity response measured by capillary rheometry at 190 °C follows a pseudoplastic curve. At an apparent shear rate of 100 s⁻¹, viscosity is approximately 1500 Pa·s; at 1000 s⁻¹, viscosity falls below 700 Pa·s. The apparent activation energy for viscous flow in the melt temperature range 180–220 °C is approximately 25–30 kJ/mol. This temperature sensitivity explains why melt temperature adjustment is more effective than screw speed adjustment for controlling parison wall thickness. Published data for this specific configuration is limited where high-pressure capillary rheometry at the die lip is not reported in the manufacturer datasheet.
Accumulator-head machines with shot capacity above 3 L can impose long melt residence time at high temperature. If the cycle stalls, resin held above 205 °C for longer than 15 min may show an increase in melt flow index of 0.02–0.04 g/10 min and a decline in environmental stress crack resistance. The processing window narrows to approximately ±5 °C on machines without melt cooling in the accumulator. Temperature excursions above 215 °C are detectable by gel formation in the parison and by reduced drop impact at 4 °C according to ASTM D2463-15. For containers subjected to top-load testing to ISO 12048:2016, wall thickness distribution measured by ultrasonic gauge should not vary by more than ±0.15 mm across the container shoulder and handle weld. Blow air pressure is set at 6–8 bar for containers with a wall thickness of 0.8–1.2 mm. In pressure leak testing per ASTM D4991-07(2023), internal pressure is typically raised to 0.05 MPa and held for 10 s to detect microleaks at the pinch-off and handle weld lines.
Food-contact suitability for Braskem HDPE BS002W is evaluated against FDA 21 CFR 177.1520(c) 3.1a/3.2a and EU Regulation (EU) No 10/2011 as amended. The resin is manufactured without bisphenol A; however, finished-article migration limits depend on contact time, temperature, and food simulant. Migration testing under EU Regulation (EU) No 10/2011 is influenced by the final article's additive package and surface-to-volume ratio. For a bottle with 0.8 mm wall thickness and nominal capacity 1 L, the surface-to-volume ratio may be approximately 0.06 dm²/cm³, which changes the overall migration calculation. The resin grade alone cannot confer compliance; dossiers must include the finished article's colour concentrate, UV stabiliser, and processing aid declarations. Table 2 summarises the compliance matrix that converters should verify against the final compound.
| Regulation or Standard | Scope | Requirement or Status |
|---|---|---|
| FDA 21 CFR 177.1520(c) 3.1a/3.2a | Polyethylene food-contact under specified conditions | Resin basis compliance |
| EU Regulation (EU) No 10/2011 | Plastic food-contact overall migration | Finished article verification; overall migration limit 10 mg/dm² |
| Directive 2011/65/EU as amended by Directive (EU) 2015/863 | RoHS restricted substances | 0.1 wt% for lead, mercury, hexavalent chromium, PBB, PBDE; 0.01 wt% cadmium |
| EU Directive 94/62/EC | Packaging heavy metals | Sum of lead, cadmium, mercury, hexavalent chromium below 100 mg/kg |
| REACH Regulation (EC) No 1907/2006 | SVHC candidate list | No SVHC above 0.1 wt% in the supplied resin |
Blown containers produced from BS002W show two primary failure modes in production. The first is weld-line fracture at the tail flash, which occurs when the melt temperature at the die is below 175 °C and the pinch-off anvil is misaligned by more than 0.1 mm. The second is environmental stress cracking at the base corners, most frequently observed in detergent bottles stored at 40 °C and 80% relative humidity. Bottles produced with a wall thickness below 0.6 mm at the base corner fail below 24 h in stress crack testing with 10% Igepal CO-630 according to ASTM D1693-15ε1, while sections above 1.0 mm exceed 600 h. The minimum base corner wall thickness should therefore be held at 0.8 mm for detergent containers and 0.7 mm for water bottles.
Relative to injection moulding HDPE grades with melt flow indices above 20 g/10 min, BS002W displays higher die swell and lower spiral flow. The low melt flow index makes it unsuitable for thin-wall injection moulding, but it is necessary for maintaining parison integrity in blow moulding. Compared with HDPE film grades of density 0.948 g/cm³, this resin provides higher top-load stiffness and lower impact flexibility; oxygen transmission is controlled primarily by wall thickness and density rather than by the additive package. Against competitive blow moulding grades with density 0.957–0.960 g/cm³, the density of 0.954 g/cm³ shifts the property balance toward environmental stress crack resistance under detergent exposure and away from maximum top-load strength. Compared with medium-density polyethylene blow moulding grades in the density range 0.934–0.940 g/cm³, BS002W has lower flexibility and higher column strength; medium-density polyethylene is preferred for squeezable bottles requiring low stress whitening. These distinctions are measurable by flexural modulus per ISO 178:2019 and by drop impact failure height per ASTM D2463-15 at 0 °C. Published data for this specific configuration is limited for aggressive solvent-containing household chemicals. Compatibility testing should follow ASTM D543-21 and UN 3H1 packaging requirements where applicable. The grade is not recommended for continuous exposure to strong oxidisers or for hot-fill containers above 95 °C, because sustained thermal load accelerates creep and stress cracking at pinch-off welds.