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Braskem HDPE 004

    • Product Name: Braskem HDPE 004
    • 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 170127
    Density 0.954 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 0.40 g/10 min
    Tensile Strength At Yield 25 MPa
    Tensile Strength At Break 30 MPa
    Elongation At Break 600%
    Flexural Modulus 1100 MPa
    Notched Izod Impact Strength 23 C 80 J/m
    Vicat Softening Temperature 125°C
    Heat Deflection Temperature 0 45 Mpa 70°C
    Shore D Hardness 65
    Melting Temperature 130°C
    Thermal Conductivity 0.45 W/m·K
    Water Absorption <0.01%
    Dielectric Constant 2.3
    Volume Resistivity >10^16 ohm·cm

    As an accredited Braskem HDPE 004 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Braskem HDPE 004 supplied in 25 kg polyethylene bags, stacked on pallets, with moisture-resistant liner for safe storage and transport.
    Container Loading (20′ FCL) Braskem HDPE 004 loaded in a 20′ FCL container as palletized, shrink-wrapped bags, securely lashed for ocean transport.
    Shipping Braskem HDPE 004 is supplied as odorless thermoplastic pellets in 25 kg bags or 1,000 kg bulk bags, palletized and stretch-wrapped. It ships in dry, clean containers, trucks, or railcars, protected from moisture, heat, and sunlight. Not classified as dangerous goods; follow local transport regulations.
    Storage Store Braskem HDPE 004 in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, and strong oxidizers. Keep original packaging closed to prevent moisture, dust, and contamination. Avoid extreme temperatures and prolonged outdoor exposure. Maintain good housekeeping, stack containers securely, and follow first-in, first-out rotation. Ensure labels remain legible. Use appropriate PPE when handling. Do not smoke near stored material.
    Shelf Life Braskem HDPE 004 has an indefinite shelf life when stored sealed, in a cool, dry place away from direct sunlight.
    Application of Braskem HDPE 004

    Containers for alkaline hypochlorite and quaternary ammonium cleaning formulations are extrusion blow molded from Braskem HDPE 004 on continuous shuttle lines having 60–80 mm barrier screws with 24:1 L/D ratios. In these lines, the critical process variable is not melt pressure but parison length stability across an 8–12 cavity setup; a variation greater than ±2 mm at 850 mm parison length shifts the pinch-off weld from the mold seam and raises reject rates above 2%. At the feed hopper, dry blending typically uses a polyolefin-based white or colored masterbatch at 2–4 wt% and, when retail display under fluorescent and ultraviolet lighting is specified, a UV stabilizer masterbatch at 0.8–1.5 wt%; let-down ratios above 5 wt% reduce melt fracture threshold at the die lip and create gel specks on the shoulder area. The die head and mold temperature control are set to keep the melt at 176–190°C and polished tool cavities at 10–20°C, with blow air supplied at 7–9 bar; cooling time for a 1 L bottle on a 10-cavity shuttle line is 14–20 s. Compliance for this segment is anchored to REACH Regulation (EC) No 1907/2006 Annex XVII, CLP Regulation (EC) No 1272/2008 for formulated substances, and Directive 94/62/EC on packaging and packaging waste; where the cleaner formulation contains sodium hypochlorite, retention of environmental stress crack resistance is evaluated under ASTM D1693 condition B after 28-day contact at 40°C. Finished goods are 760 mL trigger spray bottles with 28/410 neck finishes, 1 L and 2 L bottles with 38/400 necks, and 5 L containers with 56 mm closures. Pre-drying is not a standard requirement for HDPE 004, but surface condensation must be removed when ambient relative humidity exceeds 60%; use of post-consumer regrind above 30 wt% in this segment is not recommended because hypochlorite exposure accelerates oxidative chain scission at pinch-off welds.

    What separates cosmetic extrusion blow molded HDPE 004 from commodity household containers?

    Cosmetic containers are graded by surface energy retention after flame treatment, low-odor headspace, and absence of stress whitening at the pinch-off, rather than by top-load or drop-height performance. On production lines using polished aluminium molds at 10–20°C and post-mold flame treatment at 200–300 W·min/m², surface energy after treatment must remain above 38 mN/m before silkscreen or pressure-sensitive labeling; if antioxidant bloom from the masterbatch lowers the reading to 36 mN/m or below, label lifting appears on 1–2% of containers and the batch is reworked. Dry-blend addition ratios are typically 1–3 wt% pearlescent masterbatch, 1.5–2.5 wt% color masterbatch, and 0.5–1.5 wt% antistatic masterbatch for dust-sensitive filling lines; silica-based matting agents above 0.5 wt% are excluded because they promote die lip abrasion and reduce clarity at the shoulder. Extrusion blow molding is conducted at 175–190°C with 7–9 bar blow air and a die gap of 1.8–2.2 mm, using 64-point parison programming to maintain minimum wall thickness of 0.4 mm in the label panel; when the label panel falls below 0.4 mm, vacuum collapse during filling occurs on automated lines. Finished packaging includes 50 mL, 100 mL, 200 mL, and 500 mL bottles with 24/410 and 28/410 neck finishes for shampoos, conditioners, body washes, lotions, and hair creams. Regulatory compliance is tied to Regulation (EC) No 1223/2009 for cosmetic products, REACH Article 33 communication, Directive 94/62/EC, and Council of Europe Resolution ResAP(2002)1 where the pack is also evaluated under food-contact-equivalent migration screening. Post-consumer regrind is limited to 15 wt% in the outer layer and excluded from the inner surface when the product contains esters, ketones, or essential oils that may accelerate cracking.

    Jerrican drop-test margins, ESCR loss, and parison sag under accumulator-head processing

    In agrochemical and lubricant packaging, HDPE 004 is converted into 5–25 L UN-certified jerricans on accumulator-head blow molders where parison sag and environmental stress crack resistance pull in opposite directions. The UN design-type test imposes a minimum wall thickness after molding and a drop-height threshold that depends on packing group and density; a 25 L jerrican for packing group II is tested at a drop height of 1.2 m at ambient temperature, while packing group I raises the drop height to 1.8 m. Hydraulic pressure testing at 250 kPa for 30 min and leakproofness testing at 20 kPa under ADR/RID Chapter 6.5 are also mandatory. For these containers, the useful formulation range on the shop floor is carbon black or UV masterbatch at 2–3 wt% for exterior storage, and antistatic or conductive masterbatch at 1–2 wt% only in solvent-containing fills where flammable vapour formation is possible; fluorination or sulfonation surface treatment is a post-molding step applied to reduce hydrocarbon permeation and is not a melt-compounding additive. Regrind from HDPE 004’s own production is normally capped at 20–30 wt%, but the cap must be lowered if the jerrican is certified for PG I because impact strength and ESCR both shift below minimum values when the regrind contains degraded gel content.

    Processing conflict becomes measurable on a 90 mm accumulator-head machine with 24:1 L/D screw and a 3.2 kg shot for a 25 L jerrican. When melt temperature exceeds 195°C, parison sag of 18–22 mm across the shot cycle reduces bottom pinch-off wall thickness below 1.2 mm; below 1.2 mm, the UN drop test at -18°C can initiate a brittle crack from the pinch-off weld. To maintain wall thickness at the corners, the die gap is programmed to open 2.5–3.0 times the nominal gap at the bottom segment and close to 1.0–1.2 times at the neck segment. Mold cooling at 8–15°C and blow air at 8–10 bar produce a 20–30 L jerrican cycle of 55–75 s, with the upper limit set by cooling of the top-load-bearing sidewalls rather than by demolding. Published drop-test and ESCR data for this exact HDPE 004 jerrican configuration is limited if no certifications already exist; therefore each new tool must be qualified by a design-type test under the UN Manual of Tests and Criteria, including a -18°C drop condition, because low-temperature embrittlement and regrind content interact at the pinch-off weld.

    Finished product types in this segment are 5 L, 10 L, 20 L, and 25 L UN Type 3H1 jerricans with 42 mm, 53 mm, and 63 mm closures for emulsifiable concentrate pesticides, motor oil, chain-saw lubricant, wood preservative solvents, and liquid fertilizer packs. Operational boundaries include the need to quarantine jerricans for 48 h before stacking if mold release was used, because surface migration can interfere with cap sealing; and exclusion of amine-neutralised lubricant packages in masterbatches, which may interact with certain agrochemical actives and lower ESCR in filled storage.

    Downstream segmentRegulatory / material complianceMechanical and ESCR test anchorProcess validation basis
    Household cleaning bottlesREACH Annex XVII, CLP 1272/2008, 94/62/ECASTM D1693 condition B, top-load testShuttle blow molding parison length control
    Cosmetic bottlesEC 1223/2009, REACH Article 33, ResAP(2002)1ASTM D638, ISO 180, surface energy testFlame treatment and label adhesion
    UN jerricansADR/RID 6.5, UN Manual of Tests and CriteriaASTM D1693, drop test 1.2–1.8 mHydraulic 250 kPa/30 min, leakproofness 20 kPa
    Pharmaceutical bottlesUSP <661.1>, Ph. Eur. 3.1.3, 21 CFR 177.1520USP <661.1> extraction, particulate evaluationISO Class 8 cleanroom blow molding
    Food portion packsEU 10/2011, FDA 177.1520, EC 2023/2006Overall migration 10 mg/dm², organoleptic panelTaste-and-odour screening, regrind QA
    Automotive washer reservoirsOEM DVP&R, ISO 1183-1, ISO 1133-1ISO 180, ASTM D638, leak decay 0.5 bar/60 sThermal cycling -40°C to 80°C

    In cleanroom extrusion blow molding lines rated at ISO Class 8, HDPE 004 is converted into oral solid dose tablet and nutraceutical bottles only when the resin handling system excludes regrind and dedicated food-contact-grade screw coatings are used. The addition ratio is 1–2 wt% TiO₂ white masterbatch; antistatic, slip, and mold-release additives are excluded unless the masterbatch supplier provides USP <661.1> extractables data under 70°C for 24 h and Ph. Eur. 3.1.3 compliance. Extrusion blow molding at 170–185°C uses HEPA-filtered blow air at 6–8 bar, polished stainless steel mold cavities at 10–18°C, and no silicone spray; any silicone migrated to the bottle surface can alter USP <661.1> extraction profiles. Finished bottles are 25 mL to 500 mL continuous-thread containers with induction-sealed caps, desiccant canisters, and child-resistant closures where required. Regulatory anchor is FDA 21 CFR 177.1520 for olefin polymers, EU Regulation (EU) No 10/2011 for plastic food-contact materials, USP <661.1> for plastic packaging systems, and Ph. Eur. 3.1.3 for polyethylene containers; when the product is a nutraceutical, the converter must also separate production campaigns from non-food HDPE lines to avoid cross-contamination with post-consumer flakes. Pre-drying is only required if visible surface moisture is present or relative humidity exceeds 60%; however, purging with HDPE 004-compatible polyolefin purge compound is mandatory after color changes, because gel specks from previous masterbatches can appear in the sidewall and fail visual inspection under USP <661.1> particulate evaluation.

    When HDPE 004 replaces virgin food-contact HDPE in mono-layer portion packs

    Food-grade extrusion blow molded bottles from HDPE 004 are used for edible oil, UHT milk, vinegar, and juice portion packs only after the converter has demonstrated organoleptic neutrality and migration compliance under frozen and ambient distribution. Dry-blend addition is generally limited to 2–4 wt% food-contact white masterbatch; closed-loop regrind from the same production campaigns up to 30 wt% is permitted if the site operates EU 10/2011 Article 17 quality assurance and the regrind is not contaminated by print ink or adhesive. No post-consumer recycled HDPE is introduced into the inner layer unless the material has a positive EFSA opinion or FDA letter of no objection; even then, the inner layer usually remains virgin HDPE 004 to keep migration of unknown contaminants below detection limits. Extrusion blow molding for this segment uses 175–190°C melt temperature, 7–9 bar blow air, and mold cooling at 10–15°C; the tooling for 250 mL to 2 L bottles is polished to reduce thread microcracks and uses vented dies for odour removal. Compliance is anchored to FDA 21 CFR 177.1520, EU Regulation (EU) No 10/2011 with overall migration limit of 10 mg/dm², and EU Regulation (EC) No 2023/2006 on good manufacturing practice for food contact materials. The finished products include 250 mL and 500 mL UHT milk bottles, 1 L edible oil bottles, and 500 mL vinegar squeeze packs; these containers are subject to taste-and-odour panel screening before commercial approval. Operational boundaries are that the melt must not exceed 200°C because off-taste precursors from antioxidant conversion can be generated during extrusion, and regrind fractions above 30 wt% may increase gel opacity and reduce burst strength of the pinch-off weld.

    Windshield washer reservoirs: low-temperature weld-line integrity under 0.5 bar leak test

    Automotive windshield washer reservoirs blow molded from HDPE 004 must withstand internal pump vibration, methanol-containing washer fluid at -20°C, and underbonnet thermal spikes to 80°C without cracking at pinch-off welds or leaking at pump grommet interfaces. The production process is extrusion blow molding with vertical clamp force of 150–400 t for 2.5–5 L parts, an 80 mm barrier screw with 24:1 L/D, mold cooling at 8–12°C, and blow air at 8–10 bar. Parison programming is used to lay extra material around the filler neck, the washer pump grommet hole, and the mounting bosses; if the grommet hole wall thickness falls below 1.5 mm, the 0.5 bar leak test for 60 s after grommet insertion fails due to local creep. Addition ratio is 2–3 wt% carbon black masterbatch for UV stabilization; mixed automotive post-consumer regrind is excluded because olefinic cross-contamination and impact-modified PP reduce weld-line strength below OEM thermal cycling requirements. Compliance for this segment is defined less by a single ISO standard than by the OEM design verification plan, which typically includes leak decay at 0.5 bar for 60 s, thermal cycling from -40°C to 80°C for 200 cycles, and low-temperature drop or stone chip tests; incoming resin QC is anchored to ISO 1183-1 for density and ISO 1133-1 for melt flow rate, while mechanical evaluation uses ISO 180 or ASTM D256 for notched impact and ASTM D638 for tensile yield. Finished product types are 2.5 L, 3 L, 4 L, and 5 L windshield washer reservoirs with integrated filler necks, pump grommet openings, and snap-fit mounting bosses. Published data for this specific HDPE 004 configuration is limited to OEM internal validation reports; therefore a new reservoir must be tested on the exact blow molder intended for production because wall-thickness profile, mold temperature, and clamp force affect the -40°C impact behavior more than the resin’s datasheet Izod value suggests.

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    Certification & Compliance
    More Introduction

    Braskem HDPE 004, also listed in some regional product data sheets as HDPE 004/1, is a high-density polyethylene resin supplied as white pellets for extrusion blow moulding and thick-sheet thermoforming. The resin is manufactured under an ISO 9001 quality management system, with lot-release documentation that includes melt flow rate and density. The 004 designation corresponds to a nominal melt flow rate category of 0.40 g/10 min measured at 190 °C under 2.16 kg load using ASTM D1238-20 or ISO 1133-1:2022. Density at 23 °C is 0.955 g/cm³ according to ASTM D1505-18 or ISO 1183-1:2019. These values place the grade in the higher-density, mid-viscosity segment of the Braskem HDPE product family. The datasheet values are typical lot averages rather than specification limits; a certificate of analysis should be consulted for batch-specific acceptance.

    PropertyStandardRepresentative value
    Melt flow rate, 190 °C/2.16 kgASTM D1238-20 / ISO 1133-1:20220.40 g/10 min
    Density, 23 °CASTM D1505-18 / ISO 1183-1:20190.955 g/cm³
    Tensile strength at yield, 50 mm/minASTM D638-22 / ISO 527-2:201228 MPa
    Tensile elongation at breakASTM D638-22 / ISO 527-2:2012>800%
    Flexural modulus, 1% secantASTM D790-17 / ISO 178:20191,300 MPa
    Vicat softening temperature, 10 NASTM D1525-17 / ISO 306:2022127 °C
    Shore D hardnessASTM D2240-15 / ISO 868:200363

    The combination of 0.955 g/cm³ density and 0.40 g/10 min melt flow rate produces a balance between melt strength during parison formation and stiffness in the finished container. HDPE 004 is therefore used in extrusion blow moulding of rigid packaging for household chemicals, personal care products, industrial containers, and certain sheet applications where top-load resistance and stress crack resistance are required. It is not a thin-wall injection moulding grade; the low melt flow rate would require high injection pressures and would be difficult to fill multi-cavity tools with long flow paths. For injection moulding applications, higher-flow HDPE grades should be selected.

    What Distinguishes the 004 Melt Flow Category from Higher-Flow Injection Moulding Grades?

    The 0.40 g/10 min melt flow rate of Braskem HDPE 004 is approximately one order of magnitude lower than the 7–20 g/10 min range typical of high-density polyethylene grades intended for thin-wall injection moulding. The lower flow rate corresponds to higher average molecular weight and higher zero-shear viscosity. In extrusion blow moulding, this viscosity is advantageous because it reduces gravitational sag of the extruded parison before mould closing. In injection moulding, the same viscosity becomes a processing constraint: it requires higher injection pressures, limits flow length-to-wall-thickness ratios, and increases the risk of weld-line weakness in multi-gate tools. The material should not be substituted into injection moulding applications without a mould-filling simulation using measured viscosity data at the relevant shear rate. Published spiral-flow data for Braskem HDPE 004 is limited; therefore, processors should establish machine-specific filling behaviour using a spiral mould or short-shot study rather than extrapolating from melt flow rate alone.

    When Regrind Ratios Exceed 30% in Continuous Extrusion Blow Moulding

    Addition of post-industrial grind, bottle tails, and start-up purgings alters the molecular weight distribution and can reduce the sag resistance of the virgin resin. A 30 wt% regrind level is commonly used in container production, but lot-to-lot variability in regrind particle size and contamination changes melt pressure at the die. Extruder head pressure should be monitored: an increase above 18 MPa at a constant screw speed of 80 min⁻¹ on a 24:1 L/D grooved-feed extruder indicates screen pack plugging or excessive densified regrind. In such cases, the screen pack should be inspected and the regrind fraction reduced or re-sieved. Predrying at 80 °C for 2 h in a dehumidifying hopper is recommended only when surface moisture or wet regrind is present; the base resin is not hygroscopic, but free moisture leads to splay and voids in the parison. Plant relative humidity above 60% and outdoor storage of regrind increase the probability of surface moisture defects.

    Parison programming is the primary method for compensating wall-thickness distribution in containers blown from HDPE 004. On a typical shuttle machine with a 24:1 L/D grooved-feed extruder, the die gap is programmed from 2.5 mm at the neck and tail to 1.8 mm at the centre of the parison. This programming produces a wall thickness of approximately 1.1–1.3 mm after blow ratio is applied. The high melt viscosity of the grade maintains the programmed thickness profile during transfer, but hang times above 5 s allow sag-induced thinning. Published data for this specific die configuration is limited; processors should validate wall distribution by sectioning containers rather than relying on parison position alone.

    Density-Stiffness-ESCR Trade Surface in Rigid Packaging

    The 0.955 g/cm³ density of Braskem HDPE 004 places it in the higher-density portion of the polyethylene spectrum, where flexural modulus increases with density because the crystalline volume fraction increases. The representative flexural modulus of 1,300 MPa provides higher top-load resistance than medium-density polyethylene at 0.941 g/cm³, but environmental stress crack resistance is generally lower at higher density. For containers holding aggressive household chemicals, the grade should be evaluated using ASTM D1693-15, Condition A or B, with the actual filling liquid or a standard stress-cracking solution. Published ESCR values for Braskem HDPE 004 are not available for all filling formulations; laboratory screening is required for bleach, surfactant-based cleaners, and solvent-containing formulations. The limitation is not unique to this grade but follows the density-ESCR trade-off common to high-density polyethylene. In applications where ESCR is the dominant requirement, a lower-density grade or a bimodal copolymer with increased tie molecule populations may be required.

    Cycle time in blow moulding is dominated by conduction through the mould wall and the thermal diffusivity of HDPE. For a part wall thickness of 1.2 mm, cooling time can be estimated from Fourier number calculations, but production validation should use mould thermocouples and ejection temperature measurement. Mould coolant at 10 °C is typical for Braskem HDPE 004 when short cycles are required; lower coolant temperatures may cause surface condensation on the tool and must be balanced against dew point control in the plant. The use of chilled water below the plant air dew point can produce surface defects if tooling and plant humidity are not controlled. Thermal stabiliser consumption is accelerated when melt temperature exceeds 220 °C; sustained operation above 240 °C can cause chain scission, colour shift, and loss of parison integrity.

    Regulatory areaApplicable referenceCondition
    Food contact, United States21 CFR 177.1520(c)Finished article must meet applicable extractives and end-use limits.
    Food contact, European UnionRegulation (EU) No 10/2011Overall migration limit 10 mg/dm² or 60 mg/kg, depending on food simulant.
    RoHSDirective 2011/65/EU, Annex IILead, mercury, hexavalent chromium, PBB, PBDE each 0.1 wt%; cadmium 0.01 wt%.
    REACHEC No 1907/2006SVHC communication obligations apply above 0.1 wt% in article.

    The grade is not designed for long-term exposure to strong oxidisers, aromatic solvents, or ketones at elevated temperature; such environments can reduce molecular weight and lead to stress cracking. For packaging of oxidising or flammable liquids, compatibility testing per ASTM D543-20 or internal permeation protocols is required. External gaskets, adhesives, and labelling systems should not be assumed to be inert; their components can migrate into the polymer and alter surface properties. Published data for Braskem HDPE 004 in these specific chemical configurations is limited. Finished article compliance with the cited regulatory limits must be confirmed by extraction testing on the actual container geometry.

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