| HS Code | 622463 |
| Productname | Braskem HDPE AC59 |
| Polymertype | High-density polyethylene (HDPE) |
| Comonomer | 1-Hexene |
| Density | 0.959 g/cm³ |
| Meltflowrate | 0.45 g/10 min (190°C/2.16 kg) |
| Meltingpoint | 134°C |
| Vicatsofteningtemperature | 127°C |
| Tensilestrengthatyield | 28 MPa |
| Tensileelongationatbreak | >600% |
| Flexuralmodulus | 1200 MPa |
| Escr 100 Igepal F50 | >1000 h |
| Shoredhardness | 66 |
| Heatdeflectiontemperature | 75°C at 0.45 MPa |
| Waterabsorption | <0.01% |
| Thermalexpansioncoefficient | 1.2 × 10⁻⁴ /°C |
| Thermalconductivity | 0.45 W/m·K |
| Processingtemperature | 180-210°C |
| Moldshrinkage | 1.5-3.0% |
As an accredited Braskem HDPE AC59 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Braskem HDPE AC59 is typically packaged in 25 kg polyethylene bags, 40 per pallet, or 1,000 kg bulk bags. |
| Container Loading (20′ FCL) | Braskem HDPE AC59: 20′ FCL container loading; 25 kg polyethylene resin bags, palletized, shrink-wrapped, and secured for export. |
| Shipping | Braskem HDPE AC59 is typically shipped as solid polyethylene pellets in 25 kg moisture-resistant bags, palletized and stretch-wrapped, or in bulk trucks/railcars. It is classified as non-dangerous goods for transport. Store in a dry, ventilated area away from ignition sources, following the SDS. Handle carefully to avoid bag damage. |
| Storage | Store Braskem HDPE AC59 in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep bags or containers closed and off the floor on pallets to prevent moisture pickup and contamination. Maintain clean, dry conditions, avoid excessive stacking, and follow first-in, first-out stock rotation. Use appropriate PPE when handling. |
| Shelf Life | Braskem HDPE AC59 has indefinite shelf life if stored in original packaging, away from sunlight, moisture, and extreme temperatures. |
Monolayer extrusion blow molding of household chemical containers from Braskem HDPE AC59 is executed on continuous shuttle or reciprocating screw machines with 60–80 mm grooved-feed extruders at L/D ratios between 24:1 and 30:1. Melt temperature at the die head is maintained at 190–210 °C; barrel zones are set with a flat-to-reverse profile from 180 °C in the feed zone to 195–205 °C in the metering section so that excessive shear heating does not lower melt strength before parison exit. Die gap is adjusted from 1.2 mm to 1.8 mm depending on bottle capacity, and the parison programmer is configured to increase wall thickness at the bottom pinch-off and handle attachment zones by 15–30% over the nominal wall. Mold temperature is held at 10–25 °C with turbulent-flow chilled water at 8–12 °C; rapid quenching raises the amorphous fraction at the surface but introduces frozen-in stress, so a minimum mold temperature of 12 °C is imposed for hypochlorite bleach and alkaline cleaner containers. The formulation for general laundry detergent and fabric softener bottles consists of 97–98 wt% AC59, 2–3 wt% polyethylene-carrier color masterbatch, and 0–0.2 wt% processing aid where melt fracture is observed. Clean, dry internal regrind from the same product line is added up to 20 wt% for non-oxidizing formulations; bottles filled with sodium hypochlorite, hydrogen peroxide, or high-pH degreasers are typically run 100% virgin because regrind heat history increases the free radical population that accelerates oxidative chain scission. Release testing anchors on ASTM D1693-15 ESCR in 10% Igepal CO-630 at 50 °C, ASTM D1505 density, and ASTM D1238 melt flow rate at 190 °C/2.16 kg. Typical AC59 lot values reported on certificates of analysis are 0.30 g/10 min melt flow rate and 0.954–0.956 g/cm³ density. Terminal products are 500 mL, 1 L, and 5 L bottles for liquid detergents, fabric softeners, multi-surface cleaners, and disinfectant formulations packaged under CLP-compliant labeling.
In food-contact blow molding, the regrind ceiling is set by migration compliance rather than by viscosity loss. Braskem HDPE AC59 is processed as monolayer food packaging only when the supplied lot is covered by a food-contact statement under FDA 21 CFR 177.1520 for olefin polymers and the relevant EU Regulation (EU) No 10/2011 migration limits. Overall migration into fatty food simulant D2 must remain below 10 mg/dm², and processors quarantine regrind by production campaign. Closed-loop, uncrosslinked scrap from the same food-grade lot is re-fed at 10–30 wt% for dry goods such as sugar, salt, and powdered beverage mixes; for fatty liquids such as edible oil, and for acidic liquids such as vinegar, the regrind fraction is reduced to 0–15 wt% or eliminated because polar migrants and oxidized species concentrate in the recycled melt stream. Extrusion conditions use a 60 mm barrier screw with temperature settings from 180 °C in the feed to 200–210 °C at the die head, screw speed between 40 rpm and 70 rpm, and a blow-up ratio of 2.0:1 to 2.8:1. The die head is purged after color changes to avoid gel streaks, and the melt is filtered through a 40/60 mesh screen pack where visible contamination is detected. Terminal products include 500 mL edible oil bottles, 750 mL vinegar bottles, 1 L soy sauce containers, and 2 L syrup bottles. Release testing for food-contact packaging is governed by EN 1186 overall migration, EN 1622 sensory evaluation for odor and taint, and ASTM D2463-15 drop impact after 24 h conditioning at 23 °C.
Pharmaceutical and personal care containers made from Braskem HDPE AC59 are converted on extrusion blow molders with closed-loop parison weight control because neck finish roundness and wall distribution govern downstream capping torque. A 28 mm tamper-evident neck must hold roundness within 0.15 mm after cooling, otherwise removal torque decays below the closure supplier specification. Melt temperature is held at 190–205 °C, mold temperature at 15–25 °C, and blow pin coolant at 7–10 °C. The screw has a low-shear mixing section to disperse color without generating excessively high melt temperature on a grade with nominal 0.30 g/10 min MFR. Formulation is 100% virgin resin with 1–2 wt% pharmaceutical-grade masterbatch; antistatic additive is used at 0.1–0.3 wt% only when static charge interferes with filling lines. Compliance is evaluated against USP <661.1> for plastic packaging systems and Ph. Eur. 3.1.3 for polyolefins, with extractable and heavy-metal limits per the purchaser’s quality agreement. Terminal products are 100–500 mL shampoo bottles, 200–400 mL body wash bottles, 60–250 mL solid-dose packer bottles, and 100 mL syrup bottles. Bottle release tests include top load per ASTM D2659-16 measured at 23 ± 2 °C after 48 h, drop impact per ASTM D2463-15 at -20 °C to simulate cold-chain distribution, and cap torque retention after 28 days at 40 °C. Torque decay in HDPE neck finishes is governed by stress relaxation of the semi-crystalline structure and creep of the closure liner; initial removal torque is usually set at 0.5–1.0 N·m, but published data for AC59 under accelerated aging beyond 40 °C is limited.
Industrial jerrycan production from Braskem HDPE AC59 is driven by UN transport packaging performance rather than visual appearance. For Packing Group II liquids, a 5 L jerrycan is drop tested at 1.2 m at -18 °C and hydrostatically tested at 100 kPa; the wall section adjacent to the bottom pinch-off, handle bridge, and side seams must not fall below 1.4 mm after blow-up. Processors use accumulator-head blow molders with parison programming profiles that deliberately thicken the parison by 20–35% at the bottom and handle regions. Melt temperature is controlled at 190–210 °C, die gap at 1.5–2.5 mm, and mold temperature at 10–20 °C. Regrind from the same UN-certified line is added at 10–25 wt%; higher regrind fractions reduce low-temperature drop survival and melt strength, increasing rejections at the pinch-off weld. Terminal products are 5 L and 10 L HDPE jerrycans for lubricants, hydraulic oils, solvent degreasers, and agrochemical formulations. Qualification is performed with ASTM D1693-15 ESCR using 100% Igepal CO-630 at 50 °C and ASTM D638-14 Type IV tensile after 30 days immersion in the intended filling liquid; compatibility with hydrocarbons and ester-based lubricants must be confirmed separately because swelling reduces yield stress in the pinch-off zone.
Blow-molded automotive fluid reservoirs and emission-reduction fluid containers from Braskem HDPE AC59 are produced on 3D suction blow molding machines when the geometry includes convoluted underfill channels or hidden attachment bosses. Extrusion uses a 65–90 mm barrier screw with melt temperature between 200 °C and 220 °C; the higher melt temperature compensates for the longer parison path in 3D molding and prevents premature freezing at the mold pinch line. Mold temperature is held at 12–22 °C with localized cooling inserts around thick bosses. Carbon black masterbatch is dosed at 2.0–2.5 wt% for UV resistance in underhood and exterior installations; clean internal regrind is added up to 15 wt%, provided the scrap is free of engine oil, grease, or windshield fluid residue. Terminal products include 2–6 L coolant recovery bottles, 4–8 L windshield washer reservoirs, and 10 L diesel exhaust fluid containers. The diesel exhaust fluid container is the most restrictive application because ISO 22241-3 limits impurities that poison selective catalytic reduction catalysts; converters therefore purge the extruder with virgin AC59 before the DEF campaign and avoid calcium stearate or amine-based additive packages. Dimensional verification uses wall-thickness scanning on a production-scale blow molder, and thermal cycling from -40 °C to 120 °C is performed on welded assemblies; published data for AC59 in this exact underhood configuration is limited.
Large-volume technical containers for water treatment polymers, pool-shock chemicals, and dairy sanitizers are blow molded from Braskem HDPE AC59 on accumulator-head machines with 80–120 mm grooved-feed extruders. The target parts are 10 L, 20 L, and 25 L carboys with integrally molded handles and UN 3H1 certification where required. Melt temperature is set at 200–215 °C; die gap is increased to 1.8–2.8 mm to maintain parison wall thickness across the long handle section. Mold temperature is kept at 10–20 °C. The formulation for industrial polymer or detergent carboys contains 0–20 wt% internal regrind; for pool-shock and calcium hypochlorite containers the regrind fraction is zero and the colorant is selected from oxidizer-stable inorganic pigments. The limiting degradation mode in pool-shock packaging is oxidative chain scission accelerated by metal ions and heat history, so the converter avoids iron-based pigments and copper-containing fittings. Terminal products are 10 L and 25 L carboys for polyaluminium chloride, sodium hypochlorite, peroxide-based sanitizers, and alkaline clean-in-place concentrates. Release criteria include ASTM D1693-15 ESCR with 10% Igepal CO-630 at 50 °C, ASTM D638-14 Type IV tensile after 30-day chemical immersion, and UN drop testing for the filled container at the applicable packing group.
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Braskem HDPE AC59 is a high-molecular-weight, high-density polyethylene extrusion blow-molding resin supplied in pellet form. Public trade literature associates the grade with a density of approximately 0.959 g/cm³ when determined by ISO 1183-1 and a melt mass-flow rate of approximately 0.35 g/10 min under ISO 1133-1:2022 at 190 °C with 2.16 kg. The material is directed to rigid packaging produced on continuous shuttle, reciprocating-screw, and accumulator-head extrusion blow-molding machines. In these applications, the low melt-flow rate functions as a practical indicator of high melt strength and parison hang-time stability. The resin is distinguishable from high-fluidity HDPE injection-molding grades by its higher average molar mass, higher zero-shear viscosity, and greater torque demand. It is also distinguishable from general-purpose blow-molding grades with melt-flow rates of 0.7–1.0 g/10 min primarily through lower melt-flow and a corresponding shift toward improved environmental stress-crack resistance, although the shift is accompanied by higher backpressure and lower throughput.
The primary separation arises from melt-flow rate and its consequence for melt strength. Injection-molding HDPE grades frequently fall between 8 and 20 g/10 min; AC59’s reported 0.35 g/10 min indicates higher average molar mass, which increases melt viscosity and parison integrity while reducing injection flow length. On a single-screw extruder with 24:1 to 30:1 L/D and a barrier screw, barrel temperature profiles of 170 °C to 210 °C across feed, compression, and metering zones are typical, with head and die temperatures of 190 °C to 215 °C. Melt temperature measured at the adapter should be held below 230 °C to limit oxidative chain scission. A high-fluidity injection grade cannot sustain an unsupported parison of comparable length without excessive drawdown; a low-melt-flow blow-molding resin cannot fill a thin-wall injection mold without short shot or elevated clamp pressure. The difference is therefore not a simple melt-index adjustment but a change in tooling, screw geometry, and cycle planning.
Die swell and wall-thickness programming require particular attention when AC59 is introduced on an existing line. The melt elasticity of a high-molecular-weight HDPE generally produces greater die swell at a fixed shear rate than a lower-molar-mass grade. Tooling designed for an MFR of 0.7 g/10 min may therefore generate an oversized parison diameter when AC59 is run without die or mandrel changes. Parison programming should be commissioned by recording parison length, diameter, swell ratio, and hang time at three extrusion rates and at least two die gaps. On accumulator-head machines, a reduction in screw speed of 15–30 % is often required to hold melt temperature below 230 °C; the specific reduction depends on screw diameter, head volume, and backpressure. Pre-blow pressures for large HDPE containers commonly range from 0.05 to 0.10 MPa, but the final setting must be determined with the mold venting and flash geometry in place.
Environmental stress-crack resistance is a primary acceptance criterion for AC59 because the resin is used in packaging for aggressive formulations such as bleach-based cleaners, quaternary ammonium disinfectants, and agricultural adjuvant concentrates. In these systems, stress cracking can initiate at molded-in stress concentrations including pinch-off seams, handle flash, and abrupt wall-thickness transitions. The relevant test methods are ASTM D1693 or ISO 22088-3; results are reported as F50 failure times under a defined stress-cracking agent and temperature. Testing should be performed on specimens cut from molded bottles because orientation, cooling rate, and thickness variation change resistance relative to compression-molded plaques. Published ESCR values for AC59 are limited in the public literature; the producer’s certificate of analysis and current technical bulletin should control specification limits. Long-term contact with aromatic hydrocarbons, chlorinated solvents, or strong oxidizers should be validated by immersion or bottle-stress testing under the intended fill temperature and stacking load.
Regrind utilization interacts directly with ESCR performance. In production, clean internal regrind from flash and rejected bottles is reintroduced through a gravimetric blender. A regrind fraction of 30 wt% is a frequently applied upper boundary in non-critical containers because higher fractions can increase gel counts, broaden residence time distribution, and reduce ESCR. The regrind must be dust-free, dry, and blended by weight. Surface moisture is not typically absorbed into the HDPE pellet, but condensation during humid storage at relative humidity above 60 % can produce surface splay and weld-line porosity; a hopper dryer set at 70–80 °C for 1–2 h may be required when storage conditions fluctuate. For containers requiring UN certification, the regrind level and source must be fixed in the quality plan.
Conversion to AC59 from an HDPE with melt-flow rate of 0.7–1.0 g/10 min changes the energy balance of the extruder. At constant screw speed, torque demand rises because viscosity at the same melt temperature is higher. Machine trials should begin with screw speed reduced by 15–30 % and barrel temperatures adjusted to maintain measured melt temperature below 230 °C. If the die gap remains unchanged, die swell may increase container wall thickness and pinch-off flash. The accumulator head may also require longer parison drop time because the higher-viscosity melt can be programmed with less drawdown; however, excessive hang time will produce top-to-bottom wall thinning. Cycle time is influenced by the higher heat content and lower thermal diffusivity of the thicker melt, especially at nominal wall thickness above 1.0 mm. Differences in cooling time between AC59 and a 0.7 g/10 min grade are typically evaluated by bottle weight, wall-thickness distribution, and dimensional shrinkage after 24 h.
Rheological measurements of AC59 should include capillary shear-viscosity data rather than relying on melt-flow rate alone. The grade’s behavior at extrusion blow-molding shear rates controls die pressure, melt fracture onset, and parison swell. On production lines, excessive shear heating in the die gap can elevate local melt temperature even when the adapter thermocouple remains below 230 °C. This is particularly relevant for accumulator heads holding multiple shots, where residence time distribution may be broader than on a continuous shuttle machine. When accumulator volume divided by shot weight suggests residence time above 5 min, reduced barrel temperatures and possibly nitrogen blanketing of the hopper are used to limit degradation. Published data for AC59-specific residence time limits and melt fracture boundaries are limited; line trials should include melt-temperature profiling, visual inspection of the parison surface, and post-molding ESCR testing.
| Property | Test method | Reported typical value |
|---|---|---|
| Density | ISO 1183-1 | 0.959 g/cm³ |
| Melt mass-flow rate | ISO 1133-1:2022, 190 °C, 2.16 kg | 0.35 g/10 min |
| Tensile strength at yield | ISO 527-2 | 29 MPa (reported typical) |
| Flexural modulus | ISO 178 | 1,200 MPa (reported typical) |
| Vicat softening point | ISO 306 A50 | 129 °C (reported typical) |
| Hardness | ASTM D2240 Shore D | 62 (reported typical) |
Tensile and flexural data reported for AC59 place it among stiff HDPE blow-molding grades. This stiffness supports stackability and dimensional stability in large containers but can reduce puncture toughness at low temperatures. Differences from a softer but tougher HDPE grade should be assessed by low-temperature drop testing, such as ASTM D2463, or customer-specific impact protocols at -20 °C. Wall-thickness distribution, closure torque resistance, and mold shrinkage after 48 h should also be evaluated because the semi-crystalline nature of HDPE produces post-mold shrinkage that continues beyond immediate demolding. Mold temperatures of 10–25 °C are typical for extrusion blow molding; chilled water below the plant dew point can cause condensation on the mold surface and surface defects, so mold temperature controls should be coordinated with ambient humidity.
| Category | MFR (190 °C, 2.16 kg) | Primary process | Melt strength | Typical mold shrinkage | ESCR tendency |
|---|---|---|---|---|---|
| High-fluidity injection | 8–20 g/10 min | injection molding | low | 0.015–0.025 mm/mm | lower |
| General-purpose blow molding | 0.7–1.0 g/10 min | extrusion blow molding | moderate | 0.020–0.030 mm/mm | moderate |
| AC59 reported band | 0.35 g/10 min | extrusion blow molding | high | 0.020–0.035 mm/mm | higher |
Regulatory compliance for a specific AC59 container is not established by the resin grade alone. For food-contact packaging, the converter must obtain written confirmation that the specific lot conforms to FDA 21 CFR 177.1520 or Regulation (EU) No 10/2011, including applicable migration limits and additive restrictions. For chemical packaging, qualification is governed by end-use test regimes: UN 6.1.5 packaging tests for dangerous goods, ASTM D4919 for hazardous materials packaging, or customer-specific cap torque and puncture resistance protocols. The resin should be evaluated in the final bottle geometry with representative closure, gasket, label adhesive, and fill compatibility testing. Published data for AC59 in specific regulatory configurations is limited; therefore, no blanket food-contact or chemical-contact statement is provided here.