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Bamberger Polymers HDPE 2035A

    • Product Name: Bamberger Polymers HDPE 2035A
    • 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 188548
    Density 0.953 g/cm³
    Melt Flow Rate 20 g/10 min (190°C/2.16 kg)
    Tensile Strength At Yield 26 MPa
    Tensile Elongation At Break 1000%
    Flexural Modulus 1100 MPa
    Notched Izod Impact 0.5 ft·lb/in
    Vicat Softening Point 124 °C
    Heat Deflection Temperature At 0 45 Mpa 70 °C
    Mold Shrinkage 0.020 in/in
    Shore D Hardness 65

    As an accredited Bamberger Polymers HDPE 2035A factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Bamberger Polymers HDPE 2035A is packaged in 25 kg (55 lb) multiwall bags, typically 40 bags per pallet.
    Container Loading (20′ FCL) 20′ FCL container loaded with palletized 25 kg bags of Bamberger Polymers HDPE 2035A, shrink-wrapped and secured for ocean transport.
    Shipping Bamberger Polymers HDPE 2035A is a non-hazardous polyethylene resin. It is typically shipped in 25-kg bags, 1,000-kg bulk bags, boxes, or bulk trucks/railcars. No special DOT/IMDG/IATA classification is required. Store in a cool, dry area away from direct sunlight, heat, and ignition sources. Handle using standard industrial practices.
    Storage Store Bamberger Polymers HDPE 2035A in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep original containers tightly closed to prevent moisture, dust, and contamination. Avoid prolonged UV exposure. Use first-in, first-out inventory. Maintain clean, dry handling areas; spilled pellets are slippery. Follow the manufacturer’s safety data sheet and local regulations.
    Shelf Life Shelf life is 24 months when stored in unopened original packaging in a cool, dry environment away from direct sunlight.
    Application of Bamberger Polymers HDPE 2035A

    On 0.40–0.65 mm wall dairy tubs and deli-container lids, Bamberger Polymers HDPE 2035A is usually run in valve-gated hot-runner tools with stack or tandem configurations. The grade is controlled at a melt flow rate of 20 g/10 min under ASTM D1238 at 190°C using a 2.16 kg load, and the resulting low melt viscosity allows filling of a 0.45 mm panel at injection speeds of 120–180 mm/s with a hydraulic injection pressure of 45–70 MPa. Barrel temperatures are typically profiled at 180°C in the rear zone, 205°C in the feed zone, 215°C in the compression zone, and 225°C at the nozzle, while the mold is held at 8–18°C with a chiller set point at 10°C to freeze the thin section quickly. The hold-pressure phase is limited to 0.6–1.2 s at 35–50 MPa because extended holding at high pressure produces gate-cracking around hot tips and increases ejection distortion. On a 32-cavity stack mold, total cycle time falls between 3.8 s and 5.5 s, with most of that time consumed by mold open/close and part-removal rather than cooling; this narrows the operating window for pack pressure and makes shot-to-shot repeatability of the hot-runner temperature within ±2°C a critical variable.

    Food-contact compliance is not a resin-level certificate. Articles molded from HDPE 2035A must be evaluated under 21 CFR 177.1520 for US applications and under Regulation (EU) No 10/2011 for EU applications; the quoted overall migration limit of 10 mg/dm² applies only after finished-article testing with the correct food simulant. For dairy contact, the practical simulant is often 50% ethanol or 3% acetic acid depending on the product form; end users should fix the simulant/time/temperature conditions in the test plan. In-process recycling of sprues and runners is commonly set at 20–25 wt% regrind, provided the regrind is dry and generated from the same resin system; color masterbatch addition for lids is metered at 1.5–2.5 wt% using an LDPE or HDPE carrier to avoid screw slippage in the feed zone. The characteristic end products are injection-molded dairy tubs, deli containers, over-caps and thin snap-on lids for refrigerated distribution; each of these requires a combination of denesting behavior, top-load stiffness and crack-free hinge performance.

    At temperatures above 255°C, the melt begins to oxidize and the melt flow rate drifts; the resulting viscosity loss produces flashed parts and increases plate-out on the cavity surface. Predrying is not normally required for HDPE in a closed silo environment, but if granulate is stored at relative humidity above 60% or in unsealed gaylords, surface condensation can occur; under those conditions, a 70°C drying step for 1–2 h is applied to prevent splay on the lid sealing surfaces. The key test methods for mechanical acceptance are ASTM D638 for tensile yield strength, ASTM D790 for flexural modulus and ASTM D256 for notched Izod impact, with dimensions measured after 48 h conditioning at 23±2°C and 50±5% relative humidity. For thin-wall dairy cups, top-load testing is typically performed at 5 mm/min compression speed; the measured top-load value is governed by sidewall diameter, draft angle and wall uniformity rather than by resin density alone.

    Why Does Gate Freeze Time Control Tamper-Evident Band Hinge Behavior in Multi-Cavity Closure Molds?

    The limiting process variable in 48-cavity and 96-cavity closure tools is not melt pressure but the gate freeze time. HDPE 2035A at a melt flow rate of 20 g/10 min fills a closure mold rapidly; at an injection velocity of 180–220 mm/s, fill time may drop below 0.30 s. The gate is normally a valve-gated hot tip or a submarine gate with a diameter of 0.4–0.8 mm. At a mold temperature of 10–15°C, a 0.5 mm gate freezes within approximately 1.0–1.5 s after the injection phase; if hold pressure is not transferred into the cavity before that freeze, the tamper-evident band and hinge area remain underpacked. The result is a closure that exhibits low hinge flexural fatigue resistance and a tendency to stress-whiten during tamper-evident bridge breakage. Hold pressure is therefore set at 45–75 MPa with a hold time of 1.2–2.0 s, but the pressure transfer time is kept as short as possible by using a short hot-runner manifold and balanced valve-gate actuation.

    Closures for food and beverage applications are assessed under 21 CFR 177.1520 and, for articles sold in the EU, Regulation (EU) No 10/2011; closures involving potable water should additionally be checked against NSF/ANSI/CAN 61 if required by the water contact application. The molded closure is not certified by the resin supplier, because closure sealing force, thread interference and liner performance depend on container finish dimensions and capping torque. Slip additive is metered at 500–1200 ppm erucamide equivalent to keep removal torque in the 0.8–1.4 N·m range for conventional 28 mm beverage closures, although torque values vary with liner type and finish geometry. Color masterbatch for overcaps is normally added at 2–3 wt%, with the exact level adjusted to wall thickness because high loadings in thin sections can quench the hinge area and increase breakage. A nucleating masterbatch at 0.05–0.20 wt% is sometimes used to raise crystallization temperature and shorten cycle time by 0.5–1.0 s in high-cavitation tools, but the effect must be confirmed by differential scanning calorimetry of the molded part rather than resin pellets.

    Excessive regrind in closure production has a measurable effect on the tamper-evident band hinge. Because the hinge is a highly oriented thin ligament, regrind content above 30 wt% may increase brittleness and reduce the hinge’s ability to withstand repeated flexing before fracture; if regrind must exceed 30 wt%, the closure should be tested under ASTM D256 notched Izod impact at 23°C and after 48 h in a 10% Igepal solution. The key mechanical test for the closure body is ASTM D638 at 50 mm/min, while flexural modulus is measured by ASTM D790. For cap and closure ESCR, ASTM D1693 remains the standard screen, but it is more commonly run on plaques; closure-specific performance is best confirmed on actual molded parts filled with the target product, because liner contact, finish force and exposure to flavor oils are not captured by laboratory plaques.

    For 3–5 L open-top industrial pails, HDPE 2035A is processed at a melt temperature of 205–230°C and mold temperature of 15–25°C, with wall thicknesses from 1.3 mm to 2.2 mm. The high melt flow rate reduces injection pressure to 60–80 MPa, but in thick sections the pack-pressure window must be limited to 30–50 MPa and hold time to 5–8 s; overpacking a 2.0 mm bottom corner produces sink marks after cooling and raises internal stress near the bail ears. Cooling time is 12–18 s on a 6-cavity cold-runner tool, giving a total cycle of 18–25 s. The critical failure modes in these containers are not short-shot or flash, but drop impact at low temperature and environmental stress cracking around the bottom chime and handle attachment points.

    If pails are intended for dangerous goods, container-specific qualification under UN Model Regulations Chapter 6.1 is mandatory; no resin grade can carry a blanket UN 1H2 approval, and the pail body, lid and gasket must be burst, leak and drop tested as an assembly. For non-hazardous food ingredients, the end article must still comply with 21 CFR 177.1520 or Regulation (EU) No 10/2011 when the filled product is considered food contact. Outdoor pail formulations commonly add 1.5–3.0 wt% hindered amine light stabilizer masterbatch and 1–2 wt% carbon black masterbatch; these loadings are measured by weight percent of total resin feed and should not exceed 4 wt% total additive content without retesting low-temperature impact. The terminal articles are lubricant pails, paint pails, janitorial buckets, agricultural chemical open-top containers and bulk food-ingredient pails after lid system qualification.

    Application fieldMelt temperatureMold temperatureTypical wall thicknessTotal cycle rangePrimary supporting standard
    Thin-wall dairy tubs215–225°C8–18°C0.40–0.65 mm3.8–5.5 sASTM D1238
    Closures and overcaps210–225°C10–15°C0.5–1.2 mm6–9 sASTM D256/D1693
    Industrial pails205–230°C15–25°C1.3–2.2 mm18–25 sUN Chapter 6.1
    Storage totes200–230°C20–35°C2.5–4.0 mm25–35 sASTM D790/D256
    Personal care jars200–225°C12–20°C0.8–1.5 mm8–14 sEU 10/2011/21 CFR 177.1520
    Toy components200–230°C15–30°C1.0–2.5 mm12–20 sASTM F963/EN 71-3

    Storage Tote Drop Impact and Low-Temperature Ductility Tests for HDPE 2035A

    Thick storage tote walls shift the controlling variable from melt viscosity to differential shrinkage. In 2.5–4.0 mm storage totes, crates and domestic storage bins, HDPE 2035A is less sensitive to fill pressure and more sensitive to flatness after cooling. Melt temperature is held between 200°C and 230°C, and mold temperature is run at 20–35°C to reduce residual stress and improve rim flatness. Injection pressure is usually set at 50–70 MPa, but pack pressure is reduced to 40–55 MPa and hold time is extended to 8–12 s because the thick flat bottom cools more slowly than the sidewalls. Edge gates or fan gates are preferred over pin gates; a pin gate entering a 3.0 mm wall can create a visible flow mark and localized crystallinity difference. Cooling time is 12–18 s, and the full cycle on a 4-cavity cold-runner tool typically reaches 25–35 s. After ejection, parts are allowed to stabilize for 48 h at 23±2°C and 50±5% relative humidity before dimensional inspection; warpage is measured as the maximum gap under a straightedge on a flat surface.

    Mechanical acceptance for storage totes is based on ASTM D790 flexural modulus and ASTM D256 notched Izod impact at 23°C; HDPE 2035A is specified in the range of 900–1,100 MPa flexural modulus for design purposes, but the final value depends on mold cooling and part orientation. Low-temperature ductility is more relevant for crates and totes used in cold storage; parts are tested at -20°C after a 24 h soak, and failure of the drop test is defined as visible cracking along ribs or corner bosses. Environmental stress cracking is checked with ASTM D1693 in a 10% Igepal solution when the containers will be exposed to oils, cleaners or hydrocarbon residues. Additive loadings for storage applications typically include 1–2 wt% antistatic masterbatch for household bins and 2–4 wt% color masterbatch; carbon black at 1–2 wt% is used for UV stabilization in outdoor crates. If storage totes are marketed as kitchen or food storage, the finished article falls under 21 CFR 177.1520 or Regulation (EU) No 10/2011; general household storage totes do not have a mandatory resin-level food-contact certificate but are usually checked for heavy metals and SVHCs under REACH. The terminal articles are stackable storage totes, carrying cases, utility crates, hangers and toy structural panels, where gate blush and sink marks on the visible surface are rejection criteria.

    For 50–200 mL cosmetic jars and 1–10 mm thread overcaps, HDPE 2035A is normally molded with melt temperature of 200–225°C, mold temperature of 12–20°C and wall thickness between 0.8 mm and 1.5 mm. High-cavitation hot-runner tools with valve gates are used for these thin sections; the 20 g/10 min melt flow permits injection speeds of 100–150 mm/s and injection pressure of 50–80 MPa. Hold pressure is limited to 35–50 MPa for 1.5–3.0 s to avoid sticking on the core; ejection difficulty in deep jars is reduced by a draft angle of at least 1–2° per side and mold release treatment. Cycle times range from 8 s to 14 s, depending on jar depth and wall thickness. The terminal products are cream jars, lotion caps, roll-on bodies and overcaps for fragrance packaging.

    Compatibility with aggressive cosmetic formulations is a major limitation. Published data for HDPE 2035A in finished cosmetic systems is limited; formulators should conduct storage trials at 40°C for 4 weeks with the filled package, followed by inspection for stress cracking and dimensional change. Although HDPE 2035A may be tested under Regulation (EU) No 10/2011 for food contact, cosmetic packaging is governed by Regulation (EC) No 1223/2009, which does not establish a simple resin migration limit; the pack must be compatible with the formulation and must not release substances that make the product harmful. For US products, components intended for direct contact with food are assessed under 21 CFR 177.1520; the same resin is used for cosmetic overcaps where this clearance is not required. Slip additive is metered at 500–1000 ppm to control thread torque, and color masterbatch is added at 2–4 wt%; heavy perfume loads and essential oils should be tested under ASTM D1693 because stress cracking can occur in the thread root.

    When HDPE 2035A Is Molded into Thin-Wall Toy Components, Short Hold Time and Fast Fill Shift Shrinkage Tolerance

    High melt flow injection of HDPE 2035A into thin-wall toy components requires rapid injection speeds and a deliberately narrow hold-pressure window. Injected melt temperatures are 200–230°C, mold temperatures are 15–30°C and wall thicknesses range from 1.0 mm to 2.5 mm. Injection speeds of 100–180 mm/s are typical for thin-wall building blocks and ride-on parts; fill time is 0.3–0.8 s. Hold pressure is shortened to 2–4 s at 35–55 MPa to minimize gate stress, but this increases post-mold shrinkage variability. Dimensional control is therefore based on 48 h aging at 23±2°C and 50±5% relative humidity, with shrinkage tolerances typically set at 1.8–2.5% in the flow direction and 2.0–3.0% transverse to flow for a 2.0 mm wall. The shaping of internal bosses and snap-fit features requires uniform cooling; uneven mold temperature above ±5°C from cavity to cavity produces visible distortion in flat platforms.

    Toy parts must meet ASTM F963-23 in the US and EN 71-3 in the EU for migration of certain elements; the resin and color masterbatch should be accompanied by test data, but the responsible party still conducts finished-part testing because mold release, color concentrates and process oil residues can contribute. Mechanical acceptance uses ASTM D638 tensile yield strength and ASTM D256 notched Izod impact at 23°C; for cold-impact claims, components may be tested at -20°C after a 24 h soak. Additive loadings should be limited to 1–3 wt% color masterbatch and, where required, 1–2 wt% antistatic masterbatch; reclaimed material is normally excluded from toys unless the manufacturer has a documented recycle stream. The main operational boundary is the combination of fast fill with a high melt flow resin: excessive injection velocity above 180 mm/s can generate shear heat that reduces viscosity further and may cause flash in tooling with worn parting lines. The end components include toy building blocks, ride-on structural parts, sports training equipment and non-food children’s storage pieces, each requiring the gate location to be placed away from high visible impact zones.

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    Certification & Compliance
    More Introduction

    Bamberger Polymers HDPE 2035A is a high-density polyethylene blow moulding grade supplied in pellet form. The published technical data sheet lists a nominal density of 0.955 g/cm³ per ASTM D1505 and a melt index of 0.35 g/10 min under ASTM D1238-20 at 190 °C and 2.16 kg. That combination places the grade in the high-molecular-weight category for continuous extrusion blow moulding, with melt strength sufficient for parison lengths above 300 mm under typical machine conditions. Principal use is in industrial containers, narrow-neck bottles, and large-part blow mouldings where environmental stress crack resistance and wall thickness stability are specified. The grade should not be classified with high-flow HDPE injection moulding resins; the melt index differential is approximately two orders of magnitude, which restricts flow in thin-wall injection gates and requires blow moulding hardware rated for viscous melts.

    Applications include 10 L to 220 L transport packaging for agricultural chemicals, detergents, and industrial intermediates. The grade is also considered for extruded sheet and profile where high melt strength prevents draw-down. Processing on accumulator blow moulding machines with 24:1 to 30:1 L/D extruders is more typical than injection-blow moulding, because 2035A is not designed for injection-grade flow lengths. In continuous extrusion lines, the resin is usually processed with barrel temperatures from 160 °C to 205 °C and a die head temperature near 190 °C. The grade is supplied as natural pellet; black or coloured versions require masterbatch addition, which can alter melt viscosity and must be evaluated for parison programming.

    Which Rheological and Thermal Boundaries Define the Continuous Extrusion Blow Moulding Window?

    At low shear rates, the high molecular weight produces elevated zero-shear viscosity; during parison formation, this limits sag under gravitational load. The practical melt temperature window in continuous extrusion blow moulding is 180 °C to 210 °C. Below 180 °C, head pressure rises and melt fracture may appear as sharkskin on the parison surface. Above 210 °C, the loss of melt strength produces parison sag, especially for parts exceeding 1.2 kg shot mass. Barrel zone set points are typically reverse-profiled from the feed throat at 160–170 °C to the die head at 190–205 °C. A needle probe should be used to verify actual melt temperature, because barrel set points do not account for viscous dissipation in the screw.

    The screw should have a length-to-diameter ratio of 24:1 to 30:1 and a compression ratio of 2.5:1 to 3.5:1. Barrier screws reduce unmelt output but require sufficient torque. In accumulator machines, head volume should be matched to shot capacity; an oversized head increases residence time and can oxidize the resin. Screw speeds of 40–80 rpm are common on 60–120 mm extruders, but output is dependent on screw geometry and back pressure. Vented screws are generally not required for this olefinic material, and drying is unnecessary unless condensation from cold storage has formed on pellet surfaces.

    Die swell for this class of HDPE is typically 40% to 60% at shear rates between 10 s⁻¹ and 100 s⁻¹, but exact values depend on die geometry and extrudate temperature. The die tooling should therefore be designed with a smaller diameter than the final parison dimension. Melt temperature at the die exit outside 180–210 °C alters die swell and wall thickness distribution independently of hydraulic pressure settings. The practical consequence is that a stable die temperature profile within 2 °C across the die circumference is required for consistent wall thickness in large containers.

    Mechanical performance is controlled by density, molecular weight, and short-chain branching distribution. At a density of 0.955 g/cm³, 2035A balances stiffness with stress-crack resistance. Higher-density grades develop higher flexural modulus but lower environmental stress crack resistance. The typical tensile yield strength is 28 MPa when tested per ASTM D638-14 Type IV at 50 mm/min. Elongation at break is generally above 600%, but the exact value depends on specimen preparation and orientation. Flexural modulus is approximately 1,200 MPa per ASTM D790-17. Shore D hardness is approximately 65 per ASTM D2240-15.

    Environmental stress crack resistance is measured by ASTM D1693-15 Condition B in 100% Igepal CO-630; the published value is typically >100 h for F50. In applications involving aggressive wetting agents, this ESCR value is more relevant than tensile strength. For low-temperature toughness, brittle temperature is approximately -75 °C per ASTM D746-20. Those values are supplied as typical lot-averaged data, not as specification limits; lot-specific certificates should be requested for regulated packaging.

    PropertyTest MethodTypical Value
    Melt IndexASTM D12380.35 g/10 min at 190 °C/2.16 kg
    DensityASTM D15050.955 g/cm³
    Tensile Yield StrengthASTM D63828 MPa
    Elongation at BreakASTM D638>600%
    Flexural ModulusASTM D7901,200 MPa
    Hardness Shore DASTM D224065
    ESCR F50ASTM D1693>100 h
    Brittleness TemperatureASTM D746-75 °C

    Parison Sag and Wall Thickness Control in Industrial Containers

    In large-part blow moulding, wall thickness uniformity is governed by parison programming, melt strength, and die gap. The low melt index of 2035A reduces sag but does not eliminate the need for programmable die pins. Machine operators typically set parison wall profiles using 10 to 20 points along the shot; the effective wall thickness at the pinch-off is usually 1.2 to 1.5 times the nominal sidewall to compensate for post-pinch thinning. Mould temperature is controlled at 10 °C to 25 °C for fast cycle times; lower mould temperatures may increase surface defects such as flow marks and reduce surface gloss.

    Blow pressure must be above 0.6 MPa and is commonly 0.8 MPa to 1.0 MPa for industrial drums. Insufficient blow pressure yields poor embossing detail and longer contact time. Cooling time is a function of part mass and wall thickness; for a 20 L container with 3 mm nominal wall, cooling times of 60–90 s are observed on single-station machines, but cycle time is machine-specific. Published data for cycle-time optimization on battery-operated parison programming with this exact grade is limited; start-up trials should map wall thickness with ultrasonic gauging before release to production.

    Unlike high-flow injection moulding grades with melt indices near 20 g/10 min, 2035A is not suitable for long flow lengths in cold runners or for fast-cavitation closure. The viscosity difference also prevents direct replacement of injection grades in stack molds without redesign of gate size and runner geometry. Compared with high-density film grades, 2035A has lower melt index and higher melt strength but may have lower draw-down capability in thin-gauge film. Its comonomer content and molecular weight distribution are oriented toward ESCR and parison stability rather than high-stretch film orientation.

    Against fractional-melt drum-grade HDPE with melt index near 0.20 g/10 min, 2035A can provide lower head pressure and easier processing at moderate temperatures while retaining acceptable ESCR. The trade-off is a slight reduction in ultimate melt strength and possibly lower top-load stiffness if density is equivalent. For extreme large-part applications requiring shot masses above 10 kg, the higher melt strength of fractional-melt grades may be preferred. The product should not be blended with polypropylene or incompatible regrind; such blends reduce ESCR and can create delamination at the pinch-off.

    When 2035A Replaces a 0.20 g/10 min High-Density Copolymer in 220 L Tight-Head Drums

    Substitution into 220 L drum lines requires revalidation of parison programming and clamp tonnage. The lower melt viscosity of 2035A relative to fractional-melt grades can reduce extruder load by 5–10% at the same screw speed, but the exact load depends on screw geometry. The critical risk is parison sag between die exit and mould closure. On machines with 1.2 m drop distances, 2035A should be processed at the lower end of the melt temperature window, near 185 °C, unless wall thickness mapping shows thinning at the bottom.

    Drop impact at -18 °C should be verified per ASTM D2463 or drop-test protocols specific to UN packaging. Published data for the specific regulatory drop test performance of this grade is limited, so qualification tests are required under the intended fill temperature and stack height. Pinch-off strength is appropriate when the pinch insert is maintained at 40–60 °C; if the pinch-off zone is colder, incomplete fusion can reduce burst strength. Because 2035A may generate lower swell than fractional-melt grades, die tooling must be re-cut if the original tooling was designed for high swell; otherwise sidewall thickness will fall below the specified minimum.

    Regulatory status for food-contact use can be considered under 21 CFR 177.1520 for olefin polymers, provided the finished article meets the extractive limitations for the intended simulant. No statement is made for medical devices or implant use. Processing above 240 °C accelerates oxidative degradation and generates off-odor. Storage should avoid long-term UV exposure unless a UV stabilizer masterbatch is added. Published data for specific chemical compatibility with oxidizing acids at elevated temperature is limited; immersion tests under end-use conditions are required.

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