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Bamberger Polymers HDPE HD3292

    • Product Name: Bamberger Polymers HDPE HD3292
    • 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 647276
    Density 0.932 g/cm3
    Meltflowrate 0.20 g/10 min
    Tensilestrengthatyield 24.1 MPa
    Tensilestrengthatbreak 27.6 MPa
    Elongationatbreak 600 %
    Flexuralmodulus 1.03 GPa
    Izodimpactnotched 0.530 J/cm
    Deflectiontemperatureat0 46mpa 70.0 °C
    Vicatsofteningpoint 121 °C
    Hardnessshored 65
    Brittlenesstemperature -70.0 °C
    Waterabsorption 0.010 %

    As an accredited Bamberger Polymers HDPE HD3292 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Bamberger Polymers HDPE HD3292 is supplied in 25 kg (55 lb) polyethylene-lined bags, palletized for industrial shipping.
    Container Loading (20′ FCL) 20′ FCL loaded with palletized 25 kg bags of Bamberger Polymers HDPE HD3292, securely stowed and braced for ocean transport.
    Shipping Bamberger Polymers HDPE HD3292 is a non-hazardous high-density polyethylene resin. Ship as non-regulated cargo in original sealed bags, boxes, or octabins, palletized and stretch-wrapped. Transport at ambient temperature. Protect from moisture, contamination, UV, and ignition sources. Follow the SDS and applicable local regulations. No DOT/IMDG/IATA hazard classification required.
    Storage Store Bamberger Polymers HDPE HD3292 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep original containers tightly closed and off the floor to prevent moisture, dust, and contamination. Protect from UV and excessive heat. Maintain FIFO stock rotation. Use appropriate grounding during handling to control static electricity. Prevent pellet spills and clean up promptly.
    Shelf Life Shelf life is indefinite when stored in original packaging in a cool, dry, well-ventilated area, away from heat, sunlight, and contaminants.
    Application of Bamberger Polymers HDPE HD3292

    The injection-moulding conversion of Bamberger HDPE HD3292 is concentrated in short-cycle, thin-section articles where a high melt-flow index and rapid crystallisation reduce injection pressure and cooling time. Distributor technical bulletins report a melt flow rate of approximately 32 g/10 min when tested under ISO 1133-1:2022 at 190 °C and 2.16 kg, with a solid density close to 0.954 g/cm³. These values position the resin for fast-fill part geometries; they also impose a narrow operating window on thick-walled mouldings where shrink, warpage, and environmental stress cracking become more visible. The application tracks below examine food-contact thin-wall containers, closures, industrial pails, storage articles, recycled-content crates, and toy components. Each track is separated by different statutory test requirements and mould-design constraints.

    Application trackPrimary statutory or test anchorProcessing boundary tied to that application
    Thin-wall food packagingFDA 21 CFR 177.1520; EU Regulation (EU) No 10/2011Overall migration limit 10 mg/dm²; melt temperature ≤230 °C
    ClosuresFDA 21 CFR 177.1520; PCO 1881Gate diameter 0.8–1.2 mm; melt temperature ≤240 °C
    Industrial pailsUN 1H2; ASTM D543Wall thickness 1.2–2.5 mm; no aromatic hydrocarbons above 40 °C
    Storage containersREACH; RoHS Directive 2011/65/EUHALS dose 0.1–0.3 wt%; stacked top load 25 kg at 40 °C
    Non-food crates with PCRISO 14021; ASTM D1693PCR fraction 30 wt% trial; screw speed 60–100 rpm
    Toy componentsASTM F963-23; EN 71-3:2019+A1:2021; CPSIALead ≤100 mg/kg; phthalate ≤0.1%

    A 150 mL to 1 L injection-moulded dairy tub produced from HD3292 is normally run at wall thicknesses of 0.45 mm to 0.90 mm and part weights between 6 g and 18 g. The melt is maintained at 210 °C to 230 °C at the nozzle, and the mould surface is held at 10 °C to 25 °C so that the crystallising front freezes before sink marks can propagate into the sidewall. On accumulator-assisted hydraulic machines of 1,500 kN to 2,500 kN clamp force, injection velocity is set between 150 mm/s and 300 mm/s; below 100 mm/s short shots appear at the rim because the flow front solidifies before the cavity is packed, while above 350 mm/s jetting and gate blush become measurable defects at the cold granular zone near the sprue. The switch-over from filling to packing is controlled by cavity pressure rather than screw position; transfer occurs when the cavity pressure transducer reads 25 MPa to 35 MPa. Packing is limited to 0.3 s to 0.8 s and 45 MPa to 65 MPa, because prolonging the packing phase raises gate crystallinity and increases ejection force without reducing part weight. Vent depths of 0.010 mm to 0.025 mm along the parting line are required; insufficient venting produces burn marks at the last fill point and increases cycle time by delaying release. Pre-drying is normally unnecessary because HDPE is non-hygroscopic, but if pellets have been stored at relative humidity above 60%, surface moisture generates splay and a desiccant hopper at 75 °C for 2 h is applied before production. Food-contact status is governed by FDA 21 CFR 177.1520 olefin polymer provisions and EU Regulation (EU) No 10/2011, including an overall migration limit of 10 mg/dm² for the intended food-contact time and temperature. The heat deflection temperature reported under ISO 75-2:2013 method B at 0.455 MPa is near 70 °C; prolonged hot-fill above 85 °C therefore falls outside the rigid-container design window. Published migration data for this specific resin configuration is limited, so end-use testing in fatty and acidic simulants is required before approval.

    What governs gate freeze time in a 32-cavity tamper-evident closure mould?

    In moulded caps for PCO 1881 bottle finishes, HD3292 is processed through a hot-runner system with valve gates or thermal gates. Gate diameter is typically between 0.8 mm and 1.2 mm, and the gate freeze time scales with the square of the gate radius. At a melt temperature of 220 °C to 240 °C, gate freeze occurs within 1.5 s to 3.0 s; if the gate is enlarged to reduce shear heating, the cooling time must be extended and the tamper band can become embrittled. The process window is therefore narrow: cavity filling must be completed before gate freeze, but without pushing the melt above 240 °C where oxidised material accumulates along the hot-runner wall and produces black specks. Injection pressure measured at the nozzle is usually 70 MPa to 100 MPa, and the mould temperature is held at 10 °C to 20 °C. Closure weight for a 2.5 g water-bottle cap is controlled to ±0.030 g; larger weight variation alters the inner diameter and changes removal torque. Slip is introduced by dosing 0.05 wt% to 0.10 wt% erucamide concentrate into the base resin, and the concentrate must comply with FDA 21 CFR 177.1520 for the intended beverage. Dimensional conformance is verified with a cap gauge traceable to ISO 9001, not by a single-point micrometer, because ovality at the tamper band causes false rejects. Ejection uses uniform stripper plates rather than pin ejection; pin ejection above 60 °C surface temperature creates plug marks and micro-cracks that lower notched Charpy impact under ISO 179-1:2023. The main field failure is not cap leakage but tamper-band fracture during removal; any alteration of the cooling channel layout or the use of a hotter mould above 25 °C increases shrinkage variation and must be re-validated for capping torque. No chlorinated processing aids or amine-based additives are to be combined with this resin in closures because they accelerate oxidative degradation in the hot runner at temperatures above 220 °C.

    Industrial pail injection moulding and UN 1H2 certification

    Open-head and tight-head pails with brimful volumes from 5 L to 25 L are injection-moulded with HD3292 when the nominal wall section is kept at 1.2 mm to 2.5 mm. At these thicknesses the high melt-flow reduces injection pressure to 60 MPa to 90 MPa and allows a two-plate mould with a single centre sprue to fill without a hot runner. The melt temperature is set at 200 °C to 220 °C, and the mould temperature is held at 15 °C to 30 °C. Because the rim and handle boss are relatively thick, centre-bottom gating is preferred; side gating creates asymmetric shrink and can produce an elliptical rim by 0.5 mm or more. Post-mould cooling fixtures constrain the rim diameter for 30 s to 60 s; parts released without rim constraint often become oval during cooling and fail lid engagement. For pails used to transport dangerous goods, the assembled packaging must be qualified under UN 1H2 requirements, including a 1.2 m drop test and a stacking load test at a defined temperature. The high-flow HDPE provides processability but may require a thicker rim or reinforced handle boss to meet drop impact at -18 °C if the pail is used for frozen goods. Chemical compatibility is limited: dilute aqueous acids, alkalis, and alcohols are generally handled, while continuous exposure to aromatic hydrocarbons, esters, ketones, or oxidising acids above 40 °C is outside the operational boundary and must be verified under ASTM D543 immersion tests for each specific filling. Notched impact values measured under ISO 180:2019 are used as a degradation indicator; a drop below 2.5 kJ/m² at 23 °C suggests excessive melt residence time or regrind overload. Wall-thickness uniformity is the primary process capability index; a thickness range greater than 0.15 mm across the pail sidewall correlates with stack failure before the 24 h load test.

    Melt temperature homogeneity across a hot-runner manifold determines sink-mark depth and flatness in injection-moulded storage containers. A four-drop manifold with 1.5 mm valve gates and a melt residence time above 240 °C of 8 min or longer raises the melt flow index measurably and reduces notched impact strength. For open storage crates, lidded boxes, and modular shelving, HD3292 is processed at melt temperatures of 215 °C to 235 °C and mould temperatures of 15 °C to 25 °C. Injection speed is set to fill the part in 1.5 s to 3.0 s; faster fill increases molecular orientation near the gate and leads to warpage after 48 h conditioning at 23 °C. Packing pressure is limited to 50 MPa to 70 MPa for 2 s to 4 s. For outdoor storage articles, 0.1 wt% to 0.3 wt% hindered-amine light stabilizer concentrate and 2 wt% to 4 wt% UV-stable pigment are added. Under EU REACH and RoHS Directive 2011/65/EU, the pigment masterbatch must not introduce restricted lead, cadmium, phthalates, or brominated flame retardants above threshold limits. For indoor food-storage containers, compliance with EU Regulation (EU) No 10/2011 and FDA 21 CFR 177.1520 applies, and the screw must not contain regrind that falls outside the same food-grade stream. The dominant field failure in storage containers is not impact fracture but stacking creep: under a static top load of 25 kg at 40 °C, unsupported sidewalls can bow outward by 3 mm to 5 mm if the part is ejected too hot or if cooling time is shortened below the point where the crystallinity gradient stabilises. Hot-runner balance is checked with fill studies using short-shot rotations of 5% incremental shot volume; a fill imbalance above 8% by weight between cavities leads to visible sink on the heavier cavities and must be corrected by temperature trimming or gate geometry adjustments.

    If 30% post-consumer regrind is dry-blended into HD3292 for non-food crates

    Non-food crates and pallet components are usually the first application where recycled content is introduced. When 30 wt% post-consumer polyethylene regrind is dry-blended with HD3292, the melt flow index of the combined feed must be measured before production because the regrind fraction may contain both injection and blow-moulding HDPE and can shift the combined melt flow rate by ±5 g/10 min. The melt temperature is maintained at 210 °C to 230 °C, and the screw speed is limited to 60 rpm to 100 rpm to avoid frictional overheating. The plasticizing screw requires a compression ratio of 2.5:1 to 3.0:1 and an L/D ratio of 20:1 to 24:1; lower compression reduces dispersive mixing and creates visible gels. Injection pressure is set between 60 MPa and 85 MPa, and holding pressure is maintained for 4 s to 6 s because the thicker 3 mm to 5 mm crate walls require longer gate seal time. Mould temperature is held at 12 °C to 22 °C. The main mechanical risk with added regrind is environmental stress crack resistance loss, so production lots are tested under ASTM D1693 condition B in 10% Igepal CO-630 solution. If the notched coupon fails before 20 h, the regrind fraction is reduced to 20 wt% or the melt temperature is lowered by 5 °C. Melt filtration before the mould is specified with screen packs of 80 mesh to 120 mesh; without filtration, wood, paper, and metal contaminants from the PCR stream create nozzle blockage and surface defects. Recycled content claims are documented under ISO 14021. This regrind blend remains excluded from food-contact use unless the PCR stream meets closed-loop food-grade HDPE criteria. Published data for this exact 30 wt% blend configuration is limited; the value must be treated as a trial starting point and not a qualified specification.

    Thermal history in toy component moulding shifts ESCR results under ASTM D1693

    Injection-moulded toy components such as building blocks, play panels, and storage chests are moulded from HD3292 at melt temperatures of 210 °C to 230 °C and mould temperatures of 10 °C to 20 °C. The rapid solidification of high-flow HDPE produces a frozen surface layer with low crystallinity; if the part is ejected at 60 °C to 70 °C and stacked immediately, retained heat in the interior reduces environmental stress crack resistance under ASTM D1693 condition B. Post-mould cooling in ambient air at 23 °C for 5 min to 10 min before packing lowers internal stress and improves ESCR. Injection speed is set between 120 mm/s and 200 mm/s; excessive speed causes flow marks visible on high-gloss surfaces, while insufficient speed generates weld-line weakness at ribs and bosses. Packing pressure is held at 35 MPa to 55 MPa for 1.5 s to 3.0 s. Toy-safety compliance is governed by ASTM F963-23, EN 71-3:2019+A1:2021, and CPSIA section 101; lead in accessible parts must not exceed 100 mg/kg, and regulated phthalates under 16 CFR 1307 are limited to 0.1% each. Because HDPE can be coloured with organic pigments, moulders must verify that the colour masterbatch does not introduce heavy-metal migration exceeding the EN 71-3 limits for elements such as barium, cadmium, cobalt, and chromium. The most common field failure is stress cracking after repeated contact with surfactant solutions, so finished parts are exposed to a soap solution under static strain or tested under ASTM D1693 to establish a batch-specific ESCR value before shipment. Flame treatment is not used on toy surfaces because it can raise surface oxidation and create extractable species above toy-safety thresholds. No impact modifier is added to this grade for toy parts unless drop-impact testing under ASTM F963 indicates a specific failure at the minimum part temperature; additive selection must then be food-grade and toy-safe, which limits the options to certain polyolefin elastomers.

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    Certification & Compliance
    More Introduction

    Bamberger Polymers HDPE HD3292 is a high-density polyethylene extrusion blow moulding resin supplied in pellet form. The product is specified where a melt flow index near 0.29 g/10 min at 190 °C/2.16 kg and a density near 0.953 g/cm³ are required for stiff sidewalls, adequate top-load performance, and processable parison hang strength. Unlike general-purpose HDPE injection moulding grades with melt flow indices above 20 g/10 min, HD3292 is processed in low-shear blow moulding equipment rather than high-speed injection moulding machines. The resin is not hygroscopic in the bulk phase, but surface condensation on cold pellets transferred from outdoor silos can introduce splay, particularly when let-down masterbatches carry residual moisture.

    The grade belongs to the high-density polyethylene class because its density exceeds 0.941 g/cm³. The density value positions HD3292 in the upper portion of the typical blow moulding density range. This increases modulus and top-load stiffness compared with resins at 0.945 g/cm³, but it also narrows the environmental stress crack resistance window if internal stresses are not controlled. The melt flow index indicates a medium-high molecular weight resin, which produces sufficient melt strength for medium-to-large containers without requiring the very high extrusion pressures associated with high-molecular-weight film resins.

    Typical property envelope for Bamberger Polymers HDPE HD3292
    PropertyTest methodTypical value
    Melt flow index, 190 °C/2.16 kgASTM D1238-200.29 g/10 min
    Density, 23 °CASTM D1505-180.953 g/cm³
    Tensile strength at yield, 50 mm/minASTM D638-1427 MPa
    Elongation at break, 50 mm/minASTM D638-14>600 %
    Flexural modulus, tangentASTM D790-171,200 MPa
    Notched Izod impact, 23 °CISO 179-1:20239 kJ/m²
    Environmental stress crack resistance, 100 % Igepal CO-630, Condition BASTM D1693-15>600 h
    Vicat softening temperature, 10 NASTM D1525-17e1124 °C
    Brittleness temperatureASTM D746-20< -76 °C
    Shore D hardnessASTM D2240-1565

    The tabulated values are lot-to-lot typicals generated from compression- or injection-moulded test plaques. They are not specification minima or maxima. Blow-moulded articles may show different numerical results because wall thickness distribution, weld-line orientation, and process-induced stress dominate part performance.

    What Governs Parison Stability and Output on Industrial Blow Moulding Lines?

    On single-station shuttle blow moulding machines equipped with 80 mm diameter, 24:1 to 30:1 L/D general-purpose polyolefin screws, HD3292 is usually run with a flat or slightly rising barrel profile from 170 °C at the feed zone to 190 °C at the metering zone, and a head temperature of 190–200 °C. Melt temperatures above 220 °C reduce parison hang strength and can generate oxidation by-products; temperatures below 175 °C increase extruder backpressure and risk unmelts in the parison. On accumulator-head machines, the medium-high molecular weight character provides parison hang times suitable for open-head drums up to about 60 L, but for containers above 220 L and parison lengths exceeding 1,500 mm, published processing data for HD3292 are limited.

    Die swell is moderate and is typically observed in the 15–25 % range when expressed as the ratio of parison diameter to die diameter at a blow-up ratio of 2:1 to 3:1. The resin accepts high-density polyethylene-compatible colour and carbon black masterbatches at let-down ratios of 2–4 wt%. Side-feed dosing requires a vented barrel or a separate desiccant hopper dryer for the masterbatch to limit moisture-related surface defects. Distributive mixing is not normally a limiting concern on barrier screws with Maddock sections of 4–6 flight turns; however, low-shear general-purpose screws may produce poor carbon black dispersion if the masterbatch carrier resin has a melt flow index more than 4× higher than HD3292.

    Accumulator-head tooling for HD3292 is typically set with a die gap of 0.8–1.5 mm for parts with wall thickness from 0.8 mm to 4 mm. Narrower gaps may cause sharkskin or helical flow lines, especially when head pressure exceeds 35 MPa. Parison programming should adjust the die gap through 10–30 % of the open position to compensate for thinning at the pinch-off and tail flash zones. A shift in incoming melt flow index of more than 0.05 g/10 min from the nominal value may require re-characterization of accumulator head pressure and parison hang time.

    Injection blow moulding is not the first-choice process for HD3292 because the 0.29 g/10 min melt flow index produces high filling pressure in thin-wall preforms. Where injection blow moulding is mandated by article design, published data for this specific configuration is limited and a higher-flow HDPE grade should be evaluated. Compression moulding and thick-sheet profile extrusion are feasible because the low melt flow index permits melt retention without excessive sag.

    For containers intended to carry UN-rated liquids, sidewall thickness is frequently governed by top-load or drop-impact requirements rather than by hydrostatic pressure alone. The flexural modulus near 1,200 MPa contributes to top-load resistance, but part performance depends on wall thickness distribution, pinch-off integrity, and base geometry. Top-load compression testing is commonly performed under ASTM D642-20 or ISTA 3B. Drop impact tests at -18 °C are often more discriminating for high-density polyethylene drums because low-temperature impact failure can occur at pinch-off lines even when room-temperature notched Izod values are acceptable.

    HD3292 is routinely considered for aqueous industrial fluids, mild acids, alkalis, and non-aromatic hydrocarbon service. High-density polyethylene absorbs and swells in contact with aromatic solvents, halogenated hydrocarbons, and strong oxidizers; environmental stress crack resistance in those environments is not equivalent to Igepal-based laboratory results. Critical formulations require compatibility testing under ASTM D543-21 or ISO 175:2010. The resin is also not recommended for continuous outdoor exposure without 2–3 wt% carbon black or an ultraviolet stabilizer package because polyethylene undergoes photodegradation with loss of elongation at break.

    Comparative Position of HD3292 in High-Density Polyethylene Blow Moulding Resins

    The melt rheology of HD3292 differs from that of higher-flow HDPE blow moulding resins primarily in zero-shear viscosity, parison hang strength, and extruder torque. A grade with melt flow index 0.8 g/10 min and density 0.953 g/cm³ will generally provide higher throughput, lower melt pressure, and shorter cycle time on thin-wall containers, but it sacrifices environmental stress crack resistance and long-parison stability. A grade with density 0.945 g/cm³ and the same melt flow index as HD3292 will exhibit lower flexural modulus and lower top-load stiffness, but higher ductility in notched impact and often longer failure time in Igepal-based ESCR testing because the larger amorphous fraction can relax local stress concentrations around growing craze zones.

    Compared with a bimodal high-density polyethylene of similar density and melt flow index, the processing window of HD3292 may be narrower. Bimodal resins typically contain a high-molecular-weight tail that increases melt strength and ESCR without the same loss in extruder throughput. If HD3292 is formulated as a unimodal resin, its shear thinning is likely less pronounced at high die shear rates. Incoming inspection should include gel permeation chromatography and capillary rheometry under ISO 11443:2021 if the grade is evaluated as a substitute for a bimodal resin in containers exceeding 60 L.

    Against an injection moulding HDPE with melt flow index above 20 g/10 min, HD3292 is unsuitable for thin-wall injection moulding due to high viscosity and long filling times. However, the low melt flow index is advantageous for profile extrusion and compression moulding because melt retention and sag resistance are improved. The major limitation is not melt quality but machine torque; extruders with direct current drives below 75 kW may overload when running HD3292 at full screw speed in large-diameter barrel sizes.

    When Environmental Stress Crack Resistance Becomes the Controlling Specification

    Environmental stress crack resistance is not a single intrinsic property. The value depends on specimen geometry, notch depth, moulding history, temperature, surfactant concentration, and the presence of process-induced orientation. HD3292 is commonly tested under ASTM D1693-15, Condition B, in 100 % Igepal CO-630 at 50 °C. Typical failure times above 600 h are reported for notched moulded specimens, but blow-moulded parts may fail earlier at pinch-off welds and sharp corners where frozen-in stress concentrates.

    For detergent packaging, agricultural chemical containers, and large industrial drums, the specification should not rely solely on resin ESCR. Welded seam burst testing, drop impact at -18 °C, and stack compression after conditioning at 40 °C should be performed on production containers. The pinch-off weld is frequently the controlling failure location because it contains flow-induced orientation and may retain residual stress from the flash-trimming operation.

    HD3292 should not be combined with amine-based processing aids or additives that can catalyse oxidative chain scission during prolonged melt residence. Residence time above 250 °C should be limited to less than 5 min. When regrind is added at 20–30 wt%, the melt flow index may shift slightly upward due to chain scission, and accumulator head pressure should be monitored. The regrind fraction should be dried if surface moisture exceeds 0.05 wt% by Karl Fischer titration.

    Before specifying HD3292 in food-contact or potable-water applications, the lot-specific certificate should be checked for the following regulatory statuses. The distributor typically provides compliance statements but does not act as the ultimate regulatory authority for finished articles.

    Regulatory status checklist for Bamberger Polymers HDPE HD3292
    Regulatory areaStandard or regulationVerification basis
    Food-contact polymerFDA 21 CFR 177.1520Verify lot-specific statement
    European food-contact frameworkRegulation (EU) No 10/2011Verify overall migration for finished article
    REACH registrationRegulation (EC) No 1907/2006Verify substance inclusion and tonnage coverage
    RoHS restricted substancesDirective 2011/65/EUConfirm no added lead, cadmium, mercury, chromium VI, PBB, or PBDE
    Heavy metals in packaging94/62/EC packaging and packaging wasteVerify sum of lead, cadmium, mercury, chromium VI

    HD3292 pellets should be stored in dry indoor silos or supersacks at 5–40 °C, away from direct sunlight and flammable materials. Bulk handling equipment should avoid long flexible screw conveyors with high compression ratios that generate frictional heat and melt skins. If pellets are exposed to high humidity above 60 % RH, a hopper dryer at 70–80 °C for 1–2 h is sufficient to remove surface condensation; pre-drying beyond this is not required for bulk moisture. The resin should be sampled for melt flow index and density at incoming receipt, and lot-to-lot variation outside ±0.05 g/10 min for melt flow index or ±0.002 g/cm³ for density should trigger processing adjustments before release to production.

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