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Braskem HDPE 6540

    • Product Name: Braskem HDPE 6540
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 954047
    Product Braskem HDPE 6540
    Polymer Type High Density Polyethylene
    Density 0.954 g/cm3
    Melt Index 0.35 g/10 min
    Melt Flow Ratio 100
    Tensile Strength At Yield 27 MPa
    Tensile Strength At Break 30 MPa
    Elongation At Break 600%
    Flexural Modulus 1100 MPa
    Vicat Softening Temperature 126 °C
    Environmental Stress Crack Resistance >1000 h
    Brittleness Temperature < -70 °C
    Hardness 65 Shore D
    Melting Point 131 °C

    As an accredited Braskem HDPE 6540 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Braskem HDPE 6540 is packaged in 25 kg polyethylene-lined bags, with 40 bags per pallet, totaling 1,000 kg.
    Container Loading (20′ FCL) Safe, secure loading of Braskem HDPE 6540 high-density polyethylene resin bags into a 20-foot FCL container for export ocean freight.
    Shipping Braskem HDPE 6540 is shipped as a non-hazardous solid polyethylene resin, typically in 25 kg bags, bulk bags, or bulk truck/rail containers. It requires dry, clean storage away from direct sunlight and ignition sources. No special DOT, IMDG, or IATA transport classification applies. Handle per good industrial hygiene practices.
    Storage Store Braskem HDPE 6540 in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep original bags or containers closed to prevent moisture, dust, and contamination. Use clean, dry pallets; stack securely to avoid bag damage. Avoid contact with strong oxidizers. Follow local regulations and the manufacturer’s safety data sheet.
    Shelf Life Braskem HDPE 6540 shelf life is typically two years when stored in original packaging under cool, dry, ventilated conditions away from sunlight.
    Application of Braskem HDPE 6540

    Continuous shuttle blow moulding lines running Braskem HDPE 6540 at melt temperatures from 175°C to 195°C produce monolayer bottles for liquid food packaging with volumes from 250 mL to 2 L. The grade has a typical density of 0.954 g/cm³ under ISO 1183-1:2019 and a melt flow rate of 0.4 g/10 min under ISO 1133-1:2022 at 190°C/2.16 kg; the low melt index is deliberate for preserving parison melt strength during vertical drop over die-to-mould lengths of 300 mm to 700 mm. Extruder barrels are profiled from 160°C at the rear zone to 185°C at the front zone, with the die head held at 185°C to 195°C, using screw L/D ratios of 24:1 to 30:1 and compression ratios of 3:1 to 3.5:1. Blow-up ratio is maintained from 2.0:1 to 2.8:1, and the die gap is set between 0.8 mm and 1.4 mm depending on bottle grammage; die gaps below 0.7 mm generate die-head pressure above 35 MPa and increase shear orientation in the parison. Mould temperature is held at 10°C to 20°C, and blow pressure is set from 0.6 MPa to 0.8 MPa; blow pressure below 0.5 MPa produces incomplete mould detail at pinch-offs and handle recesses. Food-contact compliance relies on FDA 21 CFR 177.1520(c) 3.2b and EU Commission Regulation 10/2011, with overall migration tested under EN 1186-1:2002 at a maximum of 10 mg/dm² after 10 days at 40°C. Terminal articles include 500 mL milk bottles, 1 L edible oil bottles, 750 mL vinegar bottles, and 2 L refrigerated dairy dispensers.

    Regulation / StandardMethod / ClauseApplication Condition
    FDA 21 CFR177.1520(c) 3.2bHigh-density ethylene polymer for food contact
    EU Regulation 10/2011EN 1186-1:2002Overall migration ≤ 10 mg/dm²
    Ph. Eur. 3.1.3Polyolefin packagingPharmaceutical containers
    USP 661.1Plastic packaging systemsFinished drug product extraction
    ADR 6.1.5.349 CFR 178.600Hazardous goods containers

    Does Parison Programming Overcome ESCR-Critical Wall Distribution in 5-L Chemical Bottles?

    In household and industrial chemical packaging, Braskem HDPE 6540 is blow-moulded into 1 L to 5 L containers with nominal wall thickness from 0.9 mm to 1.5 mm and target weights from 35 g to 145 g. Die swell and parison hang strength permit a 10-point radial wall-thickness programme on accumulator or continuous shuttle machines; top-load-bearing pinch-off walls are typically programmed 30% thicker than the centre body at 1.3 mm to 1.6 mm, while the body remains at 0.8 mm to 1.0 mm to reduce polymer consumption. Melt temperature is kept at 178°C to 195°C; below 175°C, unplasticised gel particles from the high-molecular-weight fraction cause visible fish-eyes on the bottle shoulder, and above 200°C, parison draw-down exceeds 12% over a 600 mm drop. Container compression strength under ISO 12048:2000 is targeted above 1,200 N for 5 L formats after 24 h conditioning at 23°C/50% RH; moulds with pinch-off insert clearances above 0.05 mm produce weld-line tail flash that reduces top-load by 7% to 10%. Environmental stress cracking resistance is evaluated under ASTM D1693-21 condition B in 100% Igepal CO-630 at 50°C; formulations for bleach and detergent bottles require ESCR above 60 h, while industrial acid and alkali bottles require 150 h minimum. The base HDPE 6540 grade is therefore used with 0.1 wt% to 0.3 wt% antioxidant masterbatch and UV stabiliser only when outdoor storage is specified; additive loading above 0.5 wt% reduces parison melt strength and increases fold-line cracking at the pinch-off. Compliance for transportation of dangerous goods is verified under ADR 6.1.5.3, IMDG Chapter 6.1, and 49 CFR 178.600 for corrosives and alkaline products. Terminal articles include bleach bottles, liquid detergent bottles, drain cleaner containers, and 5 L industrial detergent canisters with handle and tamper-evident closure.

    When Solvent-Based Crop Protection Formulations Demand Barrier Coextrusion with EVOH

    Agricultural chemical packaging in South American and Southeast Asian markets uses Braskem HDPE 6540 as the structural layer in monolayer and coextruded bottles from 250 mL to 5 L. For solvent-based pesticide formulations containing xylene, cyclohexanone, or paraffinic carriers above 20 wt%, monolayer HDPE 6540 shows weight gain above 1.5% under ASTM D543-21 immersion at 23°C for 30 days; in such cases, a six-layer coextrusion structure is specified with EVOH layer thickness between 3% and 6% of total wall thickness and adhesive tie layers at 2% to 3% of total wall thickness. The HDPE 6540 outer and inner layers are processed at 180°C to 195°C, while the EVOH layer is held at 190°C to 210°C in a separate extruder with low-shear screws of L/D 24:1; die-head coextrusion is carried out through a spiral mandrel head with layer sequence HDPE/tie/EVOH/tie/regrind/HDPE. Regrind from coextruded bottles, comprising HDPE, tie and EVOH, is limited to 15 wt% in the regrind layer to avoid gel formation and loss of interlayer adhesion. Container testing for agrochemical formulations includes UN certification under ADR 6.1.5.3 and 49 CFR 178.600 with stack load of 3.0 m for 28 days at 40°C, drop impact from 1.2 m at −18°C, and hydraulic leakproofness at 20 kPa internal pressure for 10 min. Published data for specific active ingredient and solvent combinations with HDPE 6540 is limited, so permeation tests are required per ASTM E96-22 and ASTM D814-95 before commercial lot release. Terminal articles include 500 mL and 1 L crop protection bottles, 5 L glyphosate canisters, and 250 mL plant growth regulator bottles with child-resistant caps.

    In cosmetic and personal care packaging cells, Braskem HDPE 6540 is run on single-station shuttle machines and two-station wheel lines producing tottles, squeeze tubes, and lotion bottles from 30 mL to 1 L. Mould temperature is set at 12°C to 18°C to achieve a high-gloss surface on polished cavity steel; blow pressure of 0.55 MPa to 0.75 MPa is combined with pre-blow delay below 0.3 s to avoid venting lines on the bottle shoulder. The grade’s density of 0.954 g/cm³ and flexural modulus of approximately 1,100 MPa under ISO 178:2019 provide body stiffness without excessive squeeze force, while the melt flow rate of 0.4 g/10 min under ASTM D1238-23 allows control of parison wall thickness through electronic programming from 0.4 mm to 1.0 mm. Bottles with neck finishes calibrated at 24/415 and 28/410 require neck insert ovality below 0.15 mm after calibration; polypropylene flip-top closures are used with neck finish dimensions controlled under ISO 10642:2019 and torque retention tested at 0.8 N·m to 1.2 N·m. For cosmetic pack compatibility, migration of packaging constituents into the cosmetic formula is evaluated according to EU Regulation 1223/2009, with analytical limits for heavy metals under EN 71-3:2019 when bright colour masterbatch is used. Titanium dioxide white or pastel masterbatch loadings are limited to 3 wt%; higher loadings above 4 wt% reduce parison melt strength and cause visible swirl marks at the gate area. Terminal articles include 200 mL shampoo tottles, 500 mL body lotion bottles with flat front/back panels, and 75 mL facial cream squeeze bottles with silk-screened decoration.

    Pharmaceutical and Nutraceutical Bottle Specifications for HDPE 6540

    Oral solid and liquid pharmaceutical containers blow-moulded from Braskem HDPE 6540 include syrup bottles from 100 mL to 500 mL, desiccant canisters from 50 g to 200 g, and effervescent tablet tubes with wall thickness from 0.8 mm to 1.2 mm. Processing takes place in ISO Class 8 cleanrooms with extruder head and mould surfaces cleaned with silicone-free detergents; melt temperature is held at 180°C to 195°C and the parison transfer path is kept below 250 mm to reduce microbial accumulation on the internal surface. A validated leak test is performed on every cavity using pressure decay at 10 kPa for 3 s; defective bottles with leak rates above 0.2 cm³/min under ISO 12818:2013 are rejected. The base resin is manufactured in compliance with FDA 21 CFR 177.1520(c) 3.2b and EU Regulation 10/2011, but finished drug product packaging systems must meet USP 661.1 plastic packaging system extraction requirements under the applicable dosage form; the resin vendor’s certificate does not substitute for drug stability protocols. For dry oral dosage forms, moisture vapour transmission of HDPE 6540 at 0.8 mm wall thickness is approximately 0.5 g/m²/day at 38°C/90% RH under ASTM F1249-20; bottles requiring moisture protection below 0.2 g/m²/day require foil induction seals or a coextruded desiccant layer. Organoleptic requirements are tested under Ph. Eur. 3.1.3 and USP 661.1; amber and opaque white masterbatch loadings are limited to 2 wt% to avoid contamination of the closure seats. Terminal articles include 200 mL paediatric syrup bottles, 100 mL veterinary oral solution bottles, and 75 g effervescent tablet tubes with tamper-evident closures.

    When flash recycle exceeds 15 wt% in closed-loop blow moulding of automotive fluids and industrial lubricant containers, Braskem HDPE 6540 requires stricter lot homogenisation because the incoming melt flow rate of 0.4 g/10 min under ISO 1133-1:2022 drifts upward by 0.02 g/10 min to 0.08 g/10 min per regrind pass at 190°C/2.16 kg. Automotive aftermarket bottles are produced in sizes from 500 mL to 5 L with wall thickness from 1.0 mm to 1.8 mm; black masterbatch loading of 2 wt% to 3 wt% carbon black is used for UV resistance and shelf-life marking contrast. Process temperatures are set from 175°C to 190°C; barrel residence time above 6 min is avoided because carbon black accelerates oxidation and increases melt flow rate drift to 0.15 g/10 min per pass. Leakproofness for oil-filled bottles is verified with pressure decay at 15 kPa for 5 s under ISO 12818:2013; bottles for engine oil and hydraulic fluids are additionally tested for compatibility with 10W-40 motor oil, DOT 4 brake fluid, and phosphate ester hydraulic fluid under ASTM D543-21 immersion at 50°C for 72 h. For brake fluid applications, HDPE 6540 is preferred only for ambient temperature units, because glycol ether formulations at elevated service temperatures above 60°C cause weight gain above 1.5% and loss of top-load. UN certified containers for liquid lubricants must pass ADR 6.1.5.3 with stack load of 3 m at 40°C for 28 days. Terminal articles include 1 L gear oil bottles with extended necks, 4 L windshield washer fluid jugs, and 5 L diesel exhaust fluid containers with tamper-evident closures.

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    Certification & Compliance
    More Introduction

    Braskem HDPE 6540 is a high-density polyethylene injection-molding grade supplied in pellet form. Manufacturer-published nominal data identify a melt flow rate of 40 g/10 min at 190 °C/2.16 kg (ASTM D1238 / ISO 1133-1) and a solid-state density of 0.956 g/cm³ at 23 °C (ASTM D1505 / ISO 1183-1). The high melt fluidity relative to general-purpose blow-molding and extrusion grades allows reduced injection pressure during filling of thin wall sections, but it also establishes an inverse relationship with melt strength and slow crack growth resistance. The grade is therefore positioned for thin-wall rigid packaging, caps and closures, housewares, and disposable technical components where the production requirement is short dry-cycle time rather than sustained hydrostatic pressure or aggressive environmental stress-crack exposure.

    Nominal property profile reported for Braskem HDPE 6540.

    PropertyTest methodNominal value
    Melt flow rate, 190 °C/2.16 kgASTM D1238 / ISO 1133-140 g/10 min
    Density, 23 °CASTM D1505 / ISO 1183-10.956 g/cm³
    Tensile strength at yieldASTM D63825–28 MPa
    Elongation at breakASTM D638>100 %
    Flexural modulus, 1 % secantASTM D7901,000–1,200 MPa
    Notched Izod impact at 23 °CASTM D25630–40 J/m
    Vicat softening temperatureASTM D1525123–126 °C
    Shore D hardnessASTM D224063–65

    These values are generated under standardized specimen preparation and are not processing guarantees. Lot-specific certificate-of-analysis data must be used for incoming inspection.

    Melt Flow and Density Establish the Primary Processing Window

    In injection molding, the 40 g/10 min melt flow rate reduces apparent melt viscosity relative to lower-flow high-density polyethylene grades. Under high-shear injection conditions the material enters the shear-thinning region, allowing filling of wall sections from 0.5 mm to 1.5 mm without exceeding a practical injection pressure of 80–120 MPa on hydraulic machines. Processing profiles commonly applied to this melt-flow class set the melt temperature between 200 °C and 250 °C, with 220 °C to 240 °C preferred for high-speed thin-wall tools. Mold temperatures are typically held at 10 °C to 40 °C to shorten cooling time; lower mold temperatures improve cycle economy but increase the risk of sink marks and frozen-in orientation in thick-to-thin transitions.

    Clamp force demand scales with projected area and injection pressure. On a multicavity closure tool with 16 cavities and 0.8 mm nominal wall, a machine clamp force of 1,000–1,500 kN is typical, but the exact value must be calculated from gate geometry, flow length, and cavity pressure transducer data. The use of valve-gated hot runners is preferred over cold-runner sprues when regrind ratios must remain below 20 % to limit molecular weight degradation.

    Melt residence time is a critical threshold. At barrel set-points above 250 °C or with screw recovery times exceeding 5 min, high-flow grades can exhibit chain scission, yellowing, and loss of notched impact toughness. Barrel temperature profiles should ascend from a rear zone of 180–190 °C to a front zone of 230–240 °C, with check-ring and nozzle set at the front-zone value. Back pressure is maintained at 5–10 bar hydraulic for homogeneous melt quality; excessive back pressure adds shear energy and can reduce cycle capacity.

    Drying is generally unnecessary for pellet supplied in sealed railcar or bulk-pack conditions. If storage relative humidity exceeds 60 % or condensation is visible on pellet surfaces, a desiccant dryer at 70 °C for 1–2 h may be applied. Forced hot-air hopper drying above 80 °C should be avoided because pellet surface oxidation can form gels or black specks in molded parts.

    What Boundary Conditions Govern Thin-Wall Injection Molding of HDPE 6540?

    The principal boundary condition in thin-wall applications is the interaction between cavity pressure and mold venting. HDPE 6540 at 40 g/10 min fills rapidly, but gas entrapment at flow fronts can produce burn marks if vents are not machined to 0.02–0.05 mm depth. Vent lands should be located at the last-filled region of each cavity and maintained with a preventive tool-cleaning interval. Gas-driven short shots are not corrected solely by increasing melt temperature; a temperature increase above 245 °C may reduce melt viscosity but also increases flash tendency in low-clamp-force machines.

    Packing pressure and time are threshold-sensitive. In a side-gated rectangular container with 0.8 mm wall, a packing pressure of 30–50 MPa maintained for 0.5–1.0 s is normally sufficient to minimize sink marks at the gate area. Packing times beyond 1.5 s add cycle time without measurable density increase, whereas packing pressures above 60 MPa can overpack the gate, raise demolding forces, and generate stress whitening at the gate. Part mass is a more reliable process monitor than cushion distance for this grade because high melt compressibility shifts with barrel wear.

    Mold shrinkage occurs in the range of 1.5–2.5 % depending on wall thickness, melt temperature, and packing. For round closures with an internal diameter of 28 mm, a shrinkage allowance of 0.5–0.7 mm on the forming core is typical, but dimensional certification should be confirmed with a capability study under ISO 13485 or equivalent quality-system requirements if the component is used in medical packaging. Post-mold dimensional drift continues for 24–48 h as crystallinity reaches equilibrium; measurement before 24 h may overstate final part size.

    Comparative Position Against Lower-Flow HDPE Grades

    A comparison with lower-flow high-density polyethylene grades, such as those with melt flow rates from 0.3 g/10 min to 4.0 g/10 min, establishes the product boundary. Low-flow blow-molding grades retain higher molecular weight and greater melt strength, permitting parison stability in extrusion blow molding and higher environmental stress crack resistance in bottle applications. HDPE 6540 is not a direct substitute for those grades in extrusion blow molding because the 40 g/10 min melt cannot support a continuous parison over the same diameter-to-wall ratio. The lower melt strength results in parison sag and wall-thickness variability that cannot be corrected economically by die-gap adjustment. Published data for this specific configuration is limited when attempts are made to run HDPE 6540 on shuttle or reciprocating blow-molding machines with parison drop lengths above 300 mm.

    In injection-molding productivity, the difference is reversed. A lower-flow grade with an MFR of 4 g/10 min may require 15–25 % higher injection pressure at the same wall section, increasing clamp-force demand and cycle time. HDPE 6540 can often run at a screw-recovery delay 2–3 s shorter than such grades in thin-wall applications. The trade-off is lower notched Izod impact and lower tensile elongation in the molded part, which must be evaluated against ASTM D256 and ASTM D638 acceptance values.

    Comparative profile of Braskem HDPE 6540 and a representative lower-flow injection-molding HDPE.

    ParameterBraskem HDPE 6540Lower-flow injection HDPE
    Melt flow rate, 190 °C/2.16 kg40 g/10 min4 g/10 min
    Density0.956 g/cm³0.950–0.960 g/cm³
    Minimum practical wall section0.5–1.5 mm1.0 mm or greater
    Injection pressure at 1.0 mm wall80–100 MPa100–130 MPa
    Notched Izod impact at 23 °C30–40 J/m40–60 J/m
    Environmental stress crack resistanceModerateHigher

    The comparative ranges are representative and must not replace a direct molding trial on the target tool. Tool-specific cavity pressure data supersede tabulated processing estimates.

    Food-contact suitability is governed by the converter’s final formulation and by the supplier’s certificate of compliance. For a natural, unfilled high-density polyethylene, compliance with FDA 21 CFR 177.1520 may be cited for olefin polymers in contact with food, provided the finished article meets extraction limits and end-use temperature restrictions. European food-contact evaluation may require demonstration of compliance with Regulation (EU) No 10/2011 and its amendments, including overall migration testing under EN 1186 and specific migration support in the supply chain. No universal food-contact approval should be inferred without lot-specific documentation.

    Chemical resistance follows the general hierarchy for high-density polyethylene: good resistance to dilute acids, bases, and aqueous salt solutions at ambient temperature; limited resistance to aromatic hydrocarbons, chlorinated solvents, and strong oxidizing acids at elevated temperature. Environmental stress cracking can develop under low external load when molded parts are exposed to alcohols, surfactants, essential oils, or aggressive agricultural chemicals. Bottles or closures under hoop stress should be tested with the specific chemical package using ASTM D1693 (bent-strip ESCR) or ISO 22088-2 as applicable; a single ESCR pass at 50 °C does not guarantee field performance at 60 °C.

    When HDPE 6540 Replaces Polypropylene in Rigid Packaging

    Substitution of polypropylene homopolymer by HDPE 6540 requires re-evaluation of density, thermal resistance, and mold shrinkage. The density of 0.956 g/cm³ is higher than polypropylene homopolymer at 0.90 g/cm³, therefore a direct translation of part mass is not possible. The lower flexural modulus of high-density polyethylene relative to polypropylene generally requires an increase in wall section or rib design to maintain top-load performance in pails and caps. Top-load testing should be conducted under ASTM D2659 or an equivalent load-at-deflection protocol.

    Thermal resistance is lower. Polypropylene homopolymer can withstand continuous service temperatures of 90–100 °C, whereas high-density polyethylene under sustained load is usually limited to 60–70 °C; HDPE 6540 softens near 123–126 °C as measured by Vicat. Hot-fill, microwave, and steam-sterilization applications that are possible with polypropylene are outside the boundary of this grade. Steam autoclave at 121 °C produces dimensional distortion. The processing advantage of HDPE 6540 over polypropylene is lower melt temperature and lower orientation in thick sections, but the creep resistance of polyethylene under continuous top load is inferior.

    Mold shrinkage differs sufficiently to require tool recutting. A polypropylene tool designed for 1.0–1.5 % shrinkage may not produce acceptable dimensions when filled with HDPE 6540 at 1.5–2.5 % shrinkage. Dimensional stability of an existing mold should be verified through a short-shot and pressure-loss study before production transfer. No substitution should be made in a living-hinge design because high-density polyethylene has lower flexural fatigue resistance than polypropylene; hinge failure occurs after repeated flexure.

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