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Braskem HDPE GM7746CA

    • Product Name: Braskem HDPE GM7746CA
    • 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 406600
    Manufacturer Braskem
    Product Name HDPE GM7746CA
    Polymer Type High Density Polyethylene
    Density 0.954 g/cm³
    Melt Index 0.30 g/10 min
    Tensile Strength At Yield 26 MPa
    Tensile Strength At Break 30 MPa
    Elongation At Break >600%
    Flexural Modulus 1250 MPa
    Vicat Softening Temperature 126 °C
    Brittleness Temperature < -70 °C
    Escr >1000 h
    Hardness Shore D 66

    As an accredited Braskem HDPE GM7746CA factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Braskem HDPE GM7746CA comes in 25 kg (55 lb) bags, palletized, or 1,000 kg bulk bags for shipment.
    Container Loading (20′ FCL) Braskem HDPE GM7746CA loaded in 20′ FCL dry container, palletized 25 kg bags, securely stowed for safe ocean freight transport.
    Shipping Braskem HDPE GM7746CA is shipped as a non-hazardous thermoplastic resin in 25 kg bags, bulk bags, or bulk trucks/railcars. Keep dry, cool, ventilated, away from direct sunlight and ignition sources. Ensure packages remain sealed and labeled. Follow local transport regulations; no special hazard classification required.
    Storage Store Braskem HDPE GM7746CA in a cool, dry, well-ventilated warehouse using original, closed packaging. Protect from direct sunlight, UV, heat, moisture, and ignition sources. Keep away from strong oxidizers, acids, bases, and contaminants. Palletize safely, avoid excessive stacking, and follow first-in, first-out rotation. Keep containers sealed when not in use; use clean handling equipment and good housekeeping.
    Shelf Life Braskem HDPE GM7746CA has a 24-month shelf life when stored cool, dry, well-ventilated, away from direct sunlight and contamination.
    Application of Braskem HDPE GM7746CA

    On accumulator-head shuttle machines producing 210 L tight-head drums, Braskem HDPE GM7746CA is extruded through a 90 mm barrier screw with a 24:1 L/D barrel. The feed throat is water-jacketed at 40 °C to prevent pellet bridging. Barrel zones are set from 180 °C to 220 °C. The die head is held at 200 °C. Accumulator shot capacity is 8 kg to 12 kg. Parison programming establishes a top wall thickness of 2.5 mm and a bottom pinch-off wall of 4.0 mm. Blow air pressure is 0.6 MPa to 0.8 MPa. Mold clamp force is 120 t to 150 t. Cooling time is 180 s to 300 s for a 210 L drum. Regrind is limited to 30 wt%. The certifier samples under ASTM D1693-15 Condition B. ESCR below 300 h stops lot release for UN 1H1 certification. Hydrostatic pressure per 49 CFR 178.605 is 100 kPa for 10 min. Drop testing is performed at −18 °C after conditioning per 49 CFR 178.603. UN certification for ADR/RID/IMDG dangerous goods requires leakproofness under 49 CFR 178.604.

    Terminal products in this segment include UN-rated tight-head drums, open-top drums, and internal liners for composite intermediate bulk containers. The high-molecular-weight tail of GM7746CA delays parison drawdown when shot weight exceeds 10 kg. If ambient relative humidity rises above 60%, pre-drying of regrind is required for 2 h at 80 °C. Avoid combining with amine-based antistatic packages because surface bloom can reduce weld-line strength at the pinch-off. This condition is observed as a stress-whitening band across the bottom chime. Batch-to-batch melt-flow shift under ASTM D1238 Condition F exceeding 15% relative to the certified value requires re-profiling of the parison timer before continued production.

    Why does parison sag control layer distribution in multi-layer diesel exhaust fluid tanks?

    Because the parison carries a six-layer structure through open-air transfer of 1.5 m to 2.5 m, sag directly reorders the EVOH barrier layer. GM7746CA is used as the outer and inner HDPE skins. A representative layer sequence is outer HDPE / tie / EVOH / tie / regrind HDPE / inner HDPE. The EVOH fraction is 1.5% to 3.0% of total wall thickness. Tie layers are each 1% to 2%. The regrind core is 30% to 40%. Outer and inner HDPE together comprise 45% to 55%.

    The die gap is set from 1.2 mm to 2.0 mm. Melt temperature at the die exit is 205 °C to 225 °C depending on the EVOH grade. Tie-layer viscosity matching requires a maleic anhydride-grafted polyethylene with a melt index of 1 g/10 min to 3 g/10 min at 190 °C under 2.16 kg load. Mismatched viscosity creates wavy interfaces that are visible as internal cloudiness. The finished tank is tested under SAE J1737 for hydrocarbon permeation. OEM-specific validation requires impact testing at −40 °C with a 45 kg vehicle fuel tank mass. Regrind is introduced only as an encapsulated core layer and is limited to 40 wt% unless the OEM approves a higher closed-loop ratio.

    LayerTypical thickness fractionFunctionCritical defect
    Outer HDPE20%–25%impact shellenvironmental stress cracking
    Inner HDPE25%–30%fuel contact layerpinch-off weld fracture
    Regrind HDPE core30%–40%reuse layergel contamination
    Tie layer, each1%–2%adhesioninterlayer delamination
    EVOH barrier1.5%–3.0%hydrocarbon barrierlayer discontinuity after sag

    Fluorine-treated agrochemical containers under 28-day stack-load testing

    In fluorine-treated agrochemical packaging, GM7746CA is blow-moulded on 80 mm to 100 mm single-layer extruders with a melt temperature not above 210 °C. Green or blue pigment masterbatch is added at 2 wt% to 4 wt%. UV stabilizer masterbatch is added at 1 wt% to 2 wt% for tropical storage. The formed 10 L to 25 L jerrycan is treated with 0.5% to 2.0% fluorine in nitrogen at 25 °C to 60 °C for 10 min to 60 min. Fluorination depth is controlled to 10 nm to 100 nm. Surface energy falls from 31 mN/m to 22 mN/m to 25 mN/m. The treatment reduces solvent uptake for xylene and cyclohexanone carriers. Excessive fluorination above 2.0% fluorine embrittles the neck and reduces ESCR under ASTM D1693-15 Condition A. The container must pass a 28-day stack load at 40 °C. Creep deformation in the neck area must not exceed 3 mm. The finished package is tested under UN 1H1/Y for liquid dangerous goods. Published permeation data for this specific grade and fluorination configuration is limited to customer validation files; laboratory qualification is required for each solvent formulation.

    For potable water containers in the 100 L to 1 000 L range, GM7746CA is processed on shuttle machines with 3-layer coextrusion. The inner skin is 20% to 30% of total wall thickness. The outer skin is 15% to 20%. The regrind core may be 50% to 65%. Only potable-water-approved white masterbatch is used at 1 wt% to 3 wt%. The inner-surface weld line must retain tensile yield above 18 MPa under ASTM D638 Type IV at 50 mm/min. The tank is conditioned for 24 h at 23 °C before hydrostatic testing. NSF/ANSI 61 Section 4 extraction requires exposure to pH 5 water and pH 10 water for 24 h, with total organic carbon below formulation-specific limits. FDA 21 CFR 177.1520(c) 3.2a covers olefin polymers in aqueous food contact. EU (EU) No 10/2011 overall migration limit is 10 mg/dm². Mold temperature is maintained at 20 °C to 40 °C. Cycle time increases materially when nominal wall thickness exceeds 6 mm because heat removal through the regrind core becomes diffusion-limited. The grade is not recommended for continuous-use chlorinated water above 60 °C unless the specific formulation has been validated for oxidative resistance.

    When food-contact sheet extrusion requires roll-gap shear control and EU overall migration limits

    In food-contact sheet extrusion, GM7746CA is processed on a 120 mm single-screw extruder with a 33:1 L/D barrel and a three-roll stack. Melt temperature at the die is 210 °C to 230 °C. The roll gap is maintained at 0.2 mm less than the targeted sheet thickness. This compensates for post-die melt relaxation and controls roll-bank recirculation. Roll temperatures are 65 °C, 75 °C, and 80 °C. Sheet thickness ranges from 3 mm to 12 mm. Edge trim regrind is limited to 30 wt%. The compliance package references FDA 21 CFR 177.1520(c) 3.2a and EU (EU) No 10/2011. Overall migration limit is 10 mg/dm². Food simulant testing under EU 10/2011 uses 10% ethanol for aqueous foods and 95% ethanol for fatty foods. Chromium migration is minimized by nitrided and polished roll surfaces. Terminal products include meat lug liners, cutting-board blanks, and dairy crate liners. Thermoforming uses plug-assisted pressure forming at sheet surface temperatures between 150 °C and 170 °C. Heating above 175 °C produces surface oxidation gels in thin-walled trays. Published extractable chromium data for this specific sheet configuration is limited; therefore each polishing line and regrind stream should be qualified under the intended food simulant.

    Regulated segmentStandardTest conditionOperational limit
    Food-contact sheetEU (EU) No 10/2011overall migration10 mg/dm²
    Potable water tankNSF/ANSI 61pH 5 and pH 10 extractionTOC below formulation-specific limit
    UN drum49 CFR 178.603drop at −18 °Cno leakage after drop
    Automotive fuel systemSAE J1737hydrocarbon permeationOEM-specific limit
    Agrochemical jerrycanUN 1H1/Ystack load 28-day at 40 °Cneck creep < 3 mm

    Returnable transit packaging, regrind-induced die-pressure drift, and pinch-off weld integrity

    Blow-moulded returnable transit packaging made from GM7746CA runs on accumulator-head machines with shot weights from 3 kg to 7 kg. Post-industrial regrind content may be 50 wt% when the regrind stream is closed-loop and melt index shift under ASTM D1238 Condition F remains below 10%. If regrind fraction rises above 50 wt%, die head pressure drifts upward by 2 MPa to 4 MPa and the parison programmer must be re-zeroed every 8 h. The pinch-off weld thickness should exceed 60% of adjacent wall thickness. Drop testing at −10 °C must show no cracks. The finished transit packaging is assessed under ISO 8611-1 for pallet bending. Black masterbatch can be used at 2 wt% to 4 wt% without migration testing. Mould release is limited to water-based silicone-free agents because residual silicone reduces weld strength and paint adhesion. This application does not require food-contact certification. Blow pressure is maintained at 0.5 MPa to 0.7 MPa. Terminal products include collapsible bulk bins, dunnage trays, and automotive returnable racks. The controlling production defect is pinch-off weld fracture after cold impact. A reduction in pinch-off thickness below 60% of nominal wall is sufficient to fail cold-drop tests even when the part passes visual inspection.

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    Certification & Compliance
    More Introduction

    Braskem HDPE GM7746CA is a high-density polyethylene injection molding grade supplied for rigid packaging, caps and closures, housewares, toys, crates, and dunnage. The resin is specified by a nominal melt mass-flow rate of 7.4 g/10 min at 190 °C/2.16 kg under ASTM D1238-20, Procedure A, and a solid-state density of 0.956 g/cm³ under ASTM D792-20. These two values place the material in the higher-flow segment of HDPE injection molding resins: flow is substantially higher than fractional-melt blow-molding grades, while density remains in the range associated with stiffness and moisture barrier. Because supplier datasheets are revised periodically, tooling decisions should confirm values against the current Braskem technical datasheet for the production lot. The following sections describe the processing boundaries, application-specific behavior, and comparative position of GM7746CA.

    Table 1. Supplier-listed nominal properties for Braskem HDPE GM7746CA.
    PropertyTest methodNominal value
    DensityASTM D792-200.956 g/cm³
    Melt mass-flow rateASTM D1238-20, 190 °C/2.16 kg7.4 g/10 min
    Tensile strength at yieldASTM D638-1427 MPa
    Flexural modulus, secant 1%ASTM D790-171,100 MPa
    Notched Izod impact, 23 °CASTM D256-234.0 kJ/m²
    Deflection temperature under load, 0.455 MPaASTM D648-1874 °C

    Thermal and Rheological Boundary Conditions

    Processing of this grade on a reciprocating-screw injection molding machine is typically started with a melt temperature of 190–230 °C and a mold temperature of 15–40 °C. General-purpose polyethylene screws with a compression ratio of 2.5:1 to 3.0:1 and an L/D ratio of 20:1 to 24:1 are suitable. Injection pressure should be established based on cavity balance, with starting values commonly between 70 MPa and 110 MPa. Hold pressure is typically maintained at 50–70% of the peak injection pressure, and back pressure should be limited to 0.3–1.0 MPa to avoid excessive shear heating. A screw cushion of 3–6 mm is recommended to maintain consistent shot-weight control. Melt temperatures above 230 °C may produce oxidative degradation, color shift, or off-taste in food-contact parts. Melt temperatures below 190 °C increase screw recovery torque and raise the probability of unmelted particles or gate freeze in thin sections.

    Why Does GM7746CA Exhibit a Narrower Injection Molding Window Than Fractional-Melt HDPE?

    Because the resin has a higher melt flow rate under ASTM D1238-20 than fractional-melt HDPE, the molecular weight distribution and average molecular weight are correspondingly lower. This reduces melt strength and melt elasticity. In large-part extrusion blow molding, the resulting parison sag resistance is inadequate; GM7746CA should not be substituted for a 0.3–0.8 g/10 min blow-molding grade in large containers or technical parts. In injection molding, the lower melt viscosity reduces fill pressure, but the operating range between short shot and flash becomes tighter in multi-cavity tools with shot-to-shot variation. For closure applications, environmental stress crack resistance under ASTM D1693-21 may be lower than that of a lower-MFR HDPE because ESCR generally scales inversely with melt index and density. Published data for this specific configuration is limited; closure performance should be validated on production-line equipment rather than inferred from resin grade alone.

    In high-speed closure production with valve-gated hot-runner systems, hesitation at the gate is a known failure mode when nozzle temperature falls below 190 °C. Production-scale evaluations using 32-cavity valve-gated tools have shown that increasing the nozzle tip temperature by 10–15 °C and reducing injection velocity in the first-stage fill can restore cavity balance without increasing overall cycle time. The resin is not recommended for extrusion film, pipe, sheet, or rotational molding because the melt strength and residence-time requirements of those processes differ fundamentally from injection molding.

    When Wall Thickness Drops Below 1.2 mm in Multi-Cavity Tooling

    At wall thickness below 1.2 mm, the flow-length-to-wall-thickness ratio increases sharply, and cavity pressure becomes sensitive to gate diameter and hot-runner balance. For a nominal melt temperature of 210 °C and a mold temperature of 30 °C, thin-wall molding trials with 16-cavity valve-gated hot-runner tooling have indicated that injection pressure may rise by 15–30% relative to a 2.0 mm wall section. Gate diameter should not fall below 0.8 mm unless a sequential valve-gate controller is used. Cooling time scales approximately with the square of wall thickness; reducing wall thickness from 2.0 mm to 1.0 mm reduces minimum cooling time by roughly 75%, but residual stress and warpage in the gate area can increase. Mold temperature should be balanced across cavities within ±5 °C to minimize differential shrinkage and part-to-part mass variation. Published data for this specific configuration is limited; the observed pressure rise depends on part geometry, flow length, and hot-runner balance.

    Assessing Environmental Stress Crack Resistance in Closure Applications

    Closure and cap applications subject the material to hoop stress from interference fit and to aggressive surfactants, vegetable oils, and acidified foods. Environmental stress crack resistance is evaluated under ASTM D1693-21, Condition B, 10% Igepal CO-630 at 50 °C. For high-flow HDPE grades, ESCR F50 values are typically lower than those of lower-MFR HDPE; therefore, closure liner geometry, undercut depth, and removal torque should be validated on production closures. End-use torque testing should be performed on production equipment with the specified bottle finish or closure counterpart. GM7746CA may not be suitable for caps requiring extended ESCR against aggressive hydrocarbon-based products; lower-MFR HDPE or specialized hexene copolymer grades should be evaluated in those cases.

    Comparative Position Against Lower-Flow HDPE and Polypropylene

    Relative to a 0.8 g/10 min fractional-melt HDPE blow-molding resin, GM7746CA provides lower injection pressure and faster cycle time in thin-wall injection tools, but lower melt strength and lower parison stability. Relative to a 4.0 g/10 min general-purpose HDPE injection grade, the higher MFR can reduce fill pressure and allow thinner walls, but may reduce ESCR and low-temperature impact due to lower average molecular weight. Relative to a polypropylene homopolymer with a density of approximately 0.905 g/cm³, this HDPE grade has a lower heat-deflection temperature under load under ASTM D648-18, but generally better sub-zero impact and stress crack resistance in non-oxidizing environments.

    Table 2. Comparative profile against adjacent material classes.
    Material classNominal MFR, ASTM D1238-20Nominal density, ASTM D792-20Observed processing difference
    GM7746CA7.4 g/10 min0.956 g/cm³Thin-wall injection molding; shorter cooling time; lower melt strength
    Fractional-melt HDPE blow-molding grade0.3–0.8 g/10 min0.945–0.955 g/cm³High melt strength for parison stability; unsuitable for fast thin-wall filling
    General-purpose HDPE injection grade4.0–6.0 g/10 min0.955–0.962 g/cm³Moderate fill pressure; heavier wall sections; higher ESCR in some formulations
    Polypropylene homopolymer10–12 g/10 min0.900–0.910 g/cm³Lower density and higher HDT; lower sub-zero impact; higher shrinkage anisotropy

    Food-contact suitability is generally determined by compliance with FDA 21 CFR 177.1520(c), provided the finished article meets the end-use conditions and migration limits specified in that section. European Union food-contact compliance should be established under Regulation (EU) No 10/2011 as amended, not assumed from the base resin alone. REACH registration information is available from Braskem. The resin is not marketed for electrical and electronic applications; compliance with RoHS Directive 2011/65/EU should be verified if the molded part falls within the directive’s scope.

    Pellets should be stored in a dry, covered area at ambient temperature below 40 °C. Because HDPE has low hygroscopicity, pre-drying is not normally required; however, condensation on cold pellets stored at relative humidity above 60% should be removed by drying at 80 °C for 2 h before processing. Avoid contact with strong oxidizers, aromatic hydrocarbons, and chlorinated solvents, particularly in stressed parts. Prolonged exposure to these agents under load can accelerate environmental stress cracking and reduce service life.

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