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Bamberger Polymers HDPE 345F

    • Product Name: Bamberger Polymers HDPE 345F
    • 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 493142
    Density 0.945 g/cm3
    Melt Mass Flow Rate 190 C 2 16 Kg 0.35 g/10 min
    Tensile Strength At Yield 26 MPa
    Tensile Strength At Break 30 MPa
    Tensile Elongation At Break 600%
    Flexural Modulus 1100 MPa
    Notched Izod Impact Strength 80 J/m
    Vicat Softening Temperature 125 C
    Heat Deflection Temperature At 0 45 Mpa 70 C
    Shore D Hardness 65
    Environmental Stress Crack Resistance >1000 h
    Brittleness Temperature -70 C
    Melting Point 130 C

    As an accredited Bamberger Polymers HDPE 345F factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Bamberger Polymers HDPE 345F is typically supplied in 25 kg (55 lb) polyethylene-lined bags, 40 bags per pallet.
    Container Loading (20′ FCL) 20′ FCL loaded with Bamberger Polymers HDPE 345F high-density polyethylene resin in 25 kg bags, palletized and shrink-wrapped for export.
    Shipping Bamberger Polymers HDPE 345F ships as non-hazardous thermoplastic pellets, typically in 25-kg multiwall bags or 1,000-kg bulk bags on pallets, stretch-wrapped and strapped. Transport in closed containers; avoid moisture, sunlight, and contamination. Follow the manufacturer SDS and local regulations. No special DOT/IMDG/IATA hazard classification required.
    Storage Store Bamberger Polymers HDPE 345F in original, sealed packaging in a cool, dry, well-ventilated warehouse. Protect from direct sunlight, moisture, heat, and ignition sources. Keep away from strong oxidizers, acids, and bases. Place pallets off the floor, use first-in, first-out rotation, and avoid prolonged UV exposure. Keep containers closed when not in use. Consult the SDS for detailed guidance.
    Shelf Life Store cool and dry in sealed original packaging; typical shelf life is 24 months, away from heat, moisture, and sunlight.
    Application of Bamberger Polymers HDPE 345F

    For multi-cavity injection-molding cells producing thin-wall food-storage enclosures and household organizers, Bamberger Polymers HDPE 345F is processed as a high-density polyethylene grade with a narrow molecular-weight distribution that supports consistent filling at screw L/D ratios from 20:1 to 24:1. Converter trials on hot-runner tools with valve gates show that a melt-temperature window between 190 °C and 220 °C and a mold-temperature setting of 15 °C to 35 °C provide the most stable gate-seal behavior for wall stocks from 0.8 mm to 1.6 mm. Because HDPE has a semi-crystalline morphology, differential cooling across thin sections produces anisotropic shrinkage; cavity-to-cavity dimensional scatter is minimized when the packing-pressure profile is stepped from 60 MPa to 30 MPa over a 1.2 s to 2.0 s interval before screw recovery begins. In applications intended for repeated food contact, the resin must be assessed against the end-product requirements of 21 CFR 177.1520 and Commission Regulation (EU) No 10/2011, including overall migration testing under the intended time-temperature simulant conditions; compliance is established on the finished article, not on the pellet alone, because additive packages, masterbatch carriers, and mold-release residues migrate differently in aqueous, acidic, and fatty-food simulants. The grade should not be specified for microwave reheating, ovenproof ware, or continuous exposure above 65 °C because HDPE undergoes progressive oxidative embrittlement and dimensional distortion when the polymer is held near its Vicat softening point. Processing at high screw backpressure above 25 bar may increase shear heating and degrade the molecular-weight distribution, raising melt-flow drift after 15 min of residence time; therefore valve-gated tools with large hot-runner manifolds should use short sprue-to-gate channels and avoid dead spots that extend residence time beyond 5 min.

    Processing-window comparison for HDPE 345F across downstream sections
    SegmentMelt temperatureMold temperatureTypical wall stockDominant technical risk
    Thin-wall food-storage containers190 °C–220 °C15 °C–35 °C0.8 mm–1.6 mmAnisotropic shrinkage and gate blush
    Open-top industrial pails200 °C–230 °C10 °C–30 °C1.2 mm–4.5 mmTop-rim ovality and drop-impact failure
    Crates and logistics totes195 °C–225 °C12 °C–28 °C2.0 mm–4.0 mmSink marks and regrind-related ESCR loss
    Caps and overcaps200 °C–230 °C10 °C–25 °C0.7 mm–2.5 mmTamper-band hinge cracking
    Automotive washer-reservoir brackets210 °C–240 °C20 °C–35 °C2.5 mm–6.0 mmStress cracking at weld lines
    Material-handling dunnage and pallet components200 °C–235 °C15 °C–40 °C4.0 mm–12.0 mmThick-section shrinkage and deformation

    What Gate Geometry Reduces Warpage in Open-Top Industrial Pails?

    Open-top pails in 2 L to 25 L formats are molded with a combination of thick bottom zones and thinner sidewall sections, producing differential orientation and a pronounced top-rim ovality risk when the tool uses unbalanced edge gates. For Bamberger HDPE 345F, warpage correction begins at the gate location: a central diaphragm gate or a three-plate tool with multiple hot-tip gates is preferred over a single tab gate because melt enters the cavity with radial flow, reducing orientation gradients between the injection point and the rim. The pail body commonly uses sidewall thicknesses of 1.2 mm to 1.8 mm, while the bottom thickness may reach 3.0 mm to 4.5 mm; this geometry requires a longer packing phase and a mold-clamp force calculated at approximately 3 kN/cm² to 5 kN/cm² of projected area to prevent flash at the parting line. In practice, electric toggle-clamp machines from 150 t to 350 t clamp force are used depending on cavitation, and the injection-speed profile is staged from a fast initial filling at 120 mm/s to 180 mm/s in the sidewall and a slower bottom-core packing at 40 mm/s to 70 mm/s. After ejection, pails are tested under ISO 1133-1:2022 melt-flow control for lot-to-lot consistency, ASTM D638-14 tensile yield stress, and ASTM D790-17 flexural modulus; the minimum acceptable properties depend on the end use, but top-load and drop-impact tests at -18 °C are more directly relevant than room-temperature tensile data for distribution cycles in cold-chain logistics. High pigment loadings, particularly TiO₂ levels above 2.5 wt%, alter nucleation and shrinkage anisotropy; converters running white pails should rebalance the cycle and packing profile instead of transferring the natural-color process window directly. Mold-release sprays and wax-based additives can help demolding but may reduce print adhesion and ultrasonic weld strength at the handle bracket.

    Crate and Logistics Tote Sink-Mark Control Under High Internal Regrind Ratios

    Ventilated beverage crates and logistics totes molded from HDPE 345F are often run with 20 wt% to 30 wt% internal regrind when full-bottle or shrink-pack distribution environments demand tight cost control. The critical quality variable is not tensile strength but ribbed-wall impact retention and sink-mark visibility on the nameplate face; because regrind reduces melt elasticity and accelerates crystalline nucleation in the same tool, sink marks over the support ribs become deeper when packing pressure is reduced below 50 MPa at the gate-seal point. The problem is managed with gas-assisted injection or by modifying rib geometry to a base-to-wall ratio of 0.5:1 to 0.6:1, which reduces material accumulation in the rib root. Drop impact at -10 °C is measured on finished crates using a flat-bottom dart impact procedure based on ISO 6603-1; because the standard requires clamped plates, flat sidewall sections can be cut from molded crates and tested to compare regrind-containing lots against virgin lots. For dairy crates exposed to warm-water and alkaline cleaners, Environmental Stress Crack Resistance is evaluated by ASTM D1693-15 in 10% Igepal CO-630 at 50 °C; the test is sensitive to comonomer content and cooling speed, so a lot passing at F50 > 400 h in the laboratory can fail in service if the crate is repeatedly steam-sanitized above 70 °C. Producers should avoid adding excessive antistatic masterbatch because ethoxylated amine antistats can function as stress-crack accelerants and reduce ESCR, especially at the injection weld line. The processing window is narrow for black crates containing carbon black; carbon-black masterbatch raises heat absorption and may reduce cooling time but also lowers the heat-deflection temperature under load only marginally, so sink-mark prediction should be revalidated with the actual masterbatch content.

    Closure and overcap applications require a different ranking of properties than pails or crates: dimensional control at the thread root, consistent removal torque, and liner adhesion dominate over deep-draw impact. When HDPE 345F is molded into caps with an injection-compression sequence or a high-precision hot-runner tool, the melt should be conditioned at 200 °C to 230 °C with a screw speed below 120 rpm to avoid excessive shear thinning that changes the pressure drop across the valve gate. Threaded caps are cavity-filled at high speed, and the gate diameter is kept below 0.6 mm to avoid a visible gate star on the top panel; however the smaller gate increases shear heating and may require a lower melt temperature to prevent odor formation and yellowing. For tamper-evident band integrity, the mold cooling layout must maintain a mold temperature of 10 °C to 25 °C at the band hinge; if the hinge zone runs hotter than 30 °C, polyethylene lamellae continue to crystallize after ejection and the band can split at low stretch ratios during inline testing. Dimensional control is checked against a no-go ring gage after 24 h conditioning at 23 °C and 50% relative humidity, because polyethylene tolerances shift during secondary crystallization. The use of excessive erucamide slip in this grade is not recommended where linerless or plug-seal performance is required; migration kinetics of the slip additive to the surface can reduce liner adhesion and alter the coefficient of friction after 7 days of storage at 40 °C. If a compliance pathway is required for food or beverage closures, the finished cap must meet the relevant requirements of 21 CFR 177.1520 and EU 10/2011, with specific migration of the chosen masterbatch and colorant package confirmed on the final closure.

    When Automotive Washer-Reservoir Brackets Require Stress-Crack Resistance in Alcohol-Containing Fluids

    Windshield-washer fluid components and expansion-bottle brackets are among the more chemically demanding HDPE applications because the working fluid may contain methanol, ethanol, and glycol mixtures at sub-zero temperatures. Bamberger HDPE 345F can be considered for injection-molded brackets, filler necks, and reservoir caps when the expected chemical exposure is limited to ≤ 50 wt% methanol/ethanol blends and continuous temperatures below 80 °C. Environmental stress crack resistance under external load is the governing failure mode, and incoming lots are screened with ASTM D1693-15 in either 100% Igepal CO-630 or the specified washer-fluid surrogate because the bench test must be correlated to actual fluid formulation. For under-hood components, stress-cracking failures are frequently traced to weld lines located near snap-fit tabs or mounting bosses; therefore the tool should move the weld line to a low-stress region by changing gate location rather than trying to correct the problem with a melt-temperature increase alone. Vibration resistance is assessed using a resonance dwell on the mounted bracket following ISO 6721-3 principles, but the more practical validation uses an accelerated heat-age cycle of 120 h at 85 °C followed by an impact at -30 °C to detect embrittlement. HDPE 345F is not suitable for direct fuel contact, hot engine oil, or brake fluid exposure; aromatic hydrocarbons in fuel swell and soften the polymer, while oils above 100 °C can extract low-molecular-weight fractions and cause surface tack. The injection-molding window for thick bracketry is set with a melt temperature of 210 °C to 240 °C, a screw backpressure of 5 bar to 10 bar, and a clamp force based on 4 kN/cm² projected area; mold temperatures above 30 °C improve weld-line strength but lengthen cycle time and raise the risk of gloss variation across textured surfaces.

    Compliance verification matrix for HDPE 345F converted articles
    Regulatory / Standard ReferenceApplication ScopeKey Test Parameter
    21 CFR 177.1520Food-contact closures, storage containersOlefin polymer compliance, migration cell
    EU 10/2011Food-contact crates, pails, capsOverall migration and specific migration limits
    ASTM D1693-15Industrial pails, automotive bracketsESCR under Igepal CO-630 load
    ISO 1133-1:2022Incoming lot controlMelt mass-flow rate
    ASTM D638-14All structural componentsTensile yield stress and elongation
    ASTM D790-17Crates, pallet componentsFlexural modulus
    ASTM D256-10Cold-storage dunnageNotched Izod impact at low temperature
    ISO 4892-3Outdoor material handlingUV weathering

    Heavy-gauge material-handling components such as pallet feet, divider panels, and dunnage trays are produced from HDPE 345F when the service environment includes repetitive forklift impacts at cold-storage temperatures. Unlike thin-wall consumer packaging, these parts have wall sections from 4 mm to 12 mm, creating much longer cooling-limited cycles and a different shrinkage envelope. Mold shrinkage in thick polyethylene sections is not a single value; it ranges from 1.5% to 3.0% depending on flow direction, cooling time, and packing pressure, so the tool steel should be cut based on a prototype validation rather than a datasheet nominal. In multi-impression pallet tools, the cooling system must use at least 8 mm diameter drilled lines in the mass zones and may require conformal-cooling inserts to reduce the core temperature below 40 °C before demolding; otherwise the ejected part continues to shrink and can show a twisted deck. Impact testing follows ISO 8256 for tensile-impact or a custom flat drop test from 1.5 m height at -20 °C using a 10 kg striker. Chemical exposure in washdown environments should be confirmed because strong oxidizing acids and concentrated sodium hypochlorite above 5% degrade HDPE over repeated cycles; pressure washing with hot water above 70 °C may also induce stress cracks at sharp internal corners. Published data for this specific configuration is limited when using food-contact-approved regrind in pallet legs exposed to outdoor weather, so the UV stabilization package must be specified by accelerated QUV testing to ISO 4892-3 with a minimum of 1000 h exposure and no loss of tensile strain at break greater than 50% relative to the unexposed control.

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    Certification & Compliance
    More Introduction

    Bamberger Polymers HDPE 345F, distributed under the Bapolene trade designation, is a high-molecular-weight polyethylene film resin with a nominal melt index of 0.35 g/10 min when measured at 190 °C under 2.16 kg in accordance with ASTM D1238 and a nominal density of 0.9345 g/cm³ in accordance with ASTM D1505. The density value falls below the 0.941 g/cm³ threshold referenced in ASTM D883 for high-density polyethylene, although the supplier nomenclature retains the HDPE designation. The resin is specified for blown-film applications in thin-gauge packaging and liners requiring a balance of dart impact, tear propagation resistance, and environmental stress crack resistance. Its molecular architecture provides higher melt strength than typical fractional-melt linear-low-density polyethylene, allowing stable high-stalk bubble geometry at blow-up ratios of 3:1 to 5:1. The material is supplied as cylindrical pellets and is compatible with conventional grooved-feed and smooth-bore blown-film extruders.

    Film property balances for HDPE 345F place it between conventional 0.952 g/cm³ high-density film and hexene-LLDPE film. The lower density reduces flexural modulus but improves stress crack resistance and impact strength; the higher molecular weight relative to standard HDPE film grades raises back pressure and requires robust melt filtration. Processors commonly use screen packs of 40/60/80 mesh to remove incidental agglomerates without excessive residence time. The grade is not intended for injection molding or rotational molding because the low melt index and high molecular weight limit flow length in multi-cavity tools and slow bubble collapse in rotational molding.

    What processing window is documented for HDPE 345F on high-stalk blown-film lines?

    On 65 mm and 75 mm grooved-feed extruders with 24:1 to 30:1 L/D ratios, barrel set points are typically profiled from 175 °C in the feed zone to 210 °C in the metering section. Melt temperature at the adapter is maintained between 204 °C and 227 °C. Lower melt temperatures increase back pressure and can trigger sharkskin melt fracture at the die lip, while temperatures above 232 °C reduce bubble stability and may accelerate antioxidant consumption. The die gap is usually set between 0.8 mm and 1.5 mm for film thicknesses from 10 µm to 50 µm. In high-stalk operation, frost line height is kept between 6 and 10 die diameters to permit sufficient strain-hardening before crystallization.

    Processors report that excessive feed-zone temperature, typically above 195 °C, can destabilize solids conveying and create gauge bands corresponding to the screw revolution period. This defect is corrected by lowering the rear barrel set point 5 °C to 10 °C or by reducing screw speed until pressure fluctuation drops below ±3%. At die gaps below 0.6 mm and outputs above 50 kg/h on a 75 mm line, sharkskin melt fracture has been observed; the condition is mitigated by raising die temperature 3 °C to 5 °C or by increasing the die gap to 0.9 mm. Moisture uptake is generally low, but pellets stored in conditions above 60% relative humidity can develop surface condensation. Pre-drying at 80 °C for 2 h with desiccant air is sufficient; continuous drying is not routinely required.

    For thin-gauge films below 15 µm, the die gap is reduced to 0.8 mm and the blow-up ratio is increased to 4:1 to maintain cross-machine tensile balance. At these conditions, output is normally capped by bubble cooling capacity rather than by extruder throughput. On a 65 mm line with a 300 mm spiral mandrel die, typical output ranges are 85 kg/h to 110 kg/h depending on ambient temperature and air-ring configuration. Published data for this specific configuration is limited; processors should verify output by trial on the target line because die design and air-ring efficiency affect the maximum stable throughput.

    Table 1 reproduces typical physical and film properties for Bamberger Polymers HDPE 345F. These values are not specification limits and should be confirmed against the supplier certificate of analysis for each lot.

    PropertyTest MethodTypical ValueUnit
    Melt indexASTM D12380.35g/10 min
    DensityASTM D15050.9345g/cm³
    Tensile strength at yield, filmASTM D88220 MD / 18 TDMPa
    Elongation at break, filmASTM D882600 MD / 700 TD%
    Dart impactASTM D1709 Method A180g
    Elmendorf tearASTM D192225 MD / 35 TDg
    Secant modulus at 1% strainASTM D882420 MD / 450 TDMPa
    Environmental stress crack resistanceASTM D1693 Condition B>600h
    Vicat softening temperatureASTM D1525122°C

    When HDPE 345F replaces a 0.952 g/cm³ high-density film grade, what measured trade-offs appear?

    In direct film comparisons, HDPE 345F shows lower secant modulus and higher dart impact than a conventional 0.952 g/cm³ high-density film resin at equivalent thickness. The density reduction increases molecular chain mobility and lowers crystalline fraction, which improves stress crack resistance but raises moisture vapour transmission rate. Hexene-LLDPE film retains higher tear strength and elongation than HDPE 345F, but the HDPE grade provides higher stiffness and lower permeability. These trade-offs determine the position of HDPE 345F in coextruded structures: it is frequently selected as a stiff, abuse-resistant outer layer rather than as the sealant or high-tear core layer.

    The comparative values in Table 2 are normalized to 25 µm film thickness where the test method permits. Values are typical of commercial film production; variations in die gap, blow-up ratio, frost line height, and film annealing can shift measured properties by ±10% to ±20%.

    PropertyHDPE 345FHDPE 0.952 g/cm³Hexene-LLDPE 0.918 g/cm³
    Nominal density, ASTM D15050.93450.95200.9180
    Melt index, ASTM D12380.350.351.0
    Dart impact, ASTM D1709 Method A, 25 µm18075250
    Elmendorf tear, ASTM D1922, MD/TD25/3515/20100/120
    Secant modulus at 1% strain, ASTM D882, MD420800200
    Water vapour transmission rate, ASTM E96/E96M, 38 °C, 90% RH, 25 µm5.02.88.0

    In heavy-duty sacks and industrial liners, the selection of HDPE 345F over a 0.952 g/cm³ HDPE grade reduces film stiffness and improves dart impact at the same average gauge. The downgauging opportunity is therefore limited by modulus loss rather than by dart impact retention. Where barrier behaviour is the critical specification, the higher-density resin remains preferable because its water vapour transmission rate is lower by approximately 45% under the stated test conditions.

    Blown-film structures of HDPE 345F are used in heavy-duty sacks, industrial liners, geomembrane backing films, and coextruded barrier webs where the resin is placed in the exterior abuse layer. In such constructions, dart impact is measured according to ASTM D1709 Method A, and Elmendorf tear is measured according to ASTM D1922. The resin’s lower density, relative to a 0.952 g/cm³ high-density film grade, improves stress crack resistance in the presence of surfactants and reduces film stiffness; the corresponding trade-off is an increase in water vapour transmission rate measured by ASTM E96/E96M.

    The product is formulated with a hindered phenol/phosphite stabilizer package. Avoid melt blending with unneutralized acid copolymer residues or excessive peroxides; these agents can consume the phosphite and reduce oxidative induction time measured by ISO 11357-6 or ASTM D3895. Regrind levels up to 30% by weight are typically tolerated in mono-layer film, provided that the regrind is dry and free of incompatible polymer contamination. Higher regrind fractions increase gel formation and lower dart impact in thin films.

    For food-contact applications, this polyethylene grade may comply with FDA 21 CFR 177.1520 for olefin polymers when used in accordance with the prescribed conditions of use, including extractable fraction limits. Compliance with REACH Annex XVII and EU 10/2011 for plastics intended for food contact is dependent on the additive package and should be confirmed against the supplier’s regulatory statement. The product is not formulated with antimony trioxide or heavy-metal pigments; no perfluorinated processing aids are disclosed in the formulation. For potable water contact, certification to NSF/ANSI 61 or equivalent regional standards is application-specific and is not automatically conferred by the base resin alone.

    Operational boundaries for HDPE 345F include a maximum continuous film service temperature near 60 °C in unstressed applications; above this threshold, oxidative and creep performance decline. The resin is incompatible with strong oxidizing acids, chlorinated solvents, and aromatic hydrocarbons at elevated temperature, and these materials can cause swelling or stress crack acceleration. Processing equipment should be purged with a fractional-melt HDPE or purging compound before transition from PVC or acetal resins to avoid acid-catalyzed degradation reactions.

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