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Bayport Polymers (Baystar) HDPE 535

    • Product Name: Bayport Polymers (Baystar) HDPE 535
    • 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 674933
    Density 0.953 g/cm³
    Melt Index 0.35 g/10 min (190°C/2.16 kg)
    Tensile Strength At Yield 26 MPa
    Tensile Strength At Break 30 MPa
    Elongation At Break >600%
    Flexural Modulus 1200 MPa
    Environmental Stress Crack Resistance >1000 h
    Vicat Softening Temperature 127°C
    Brittleness Temperature < -70°C
    Hardness Shore D 65
    Thermal Expansion Coefficient 1.2E-4 cm/cm/°C
    Melting Point 130°C

    As an accredited Bayport Polymers (Baystar) HDPE 535 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Bayport Polymers (Baystar) HDPE 535 is packaged in 25 kg polyethylene bags, 55 bags per pallet (1,375 kg), and bulk.
    Container Loading (20′ FCL) Bayport Polymers (Baystar) HDPE 535 loaded into a 20-foot FCL container, palletized in bags, kept dry, and secured for ocean transport.
    Shipping Bayport Polymers (Baystar) HDPE 535 is a non-hazardous high-density polyethylene resin. It ships as pellets in 25 kg bags, 1,000 kg bulk bags, or bulk trucks/railcars. Not regulated for DOT, IMDG, or IATA transport. Store dry, away from heat and prolonged sunlight; follow standard pellet handling.
    Storage Store Bayport Polymers (Baystar) HDPE 535 in a cool, dry, well-ventilated area, away from direct sunlight, heat, sparks, and flames. Keep original bags or containers closed, off the ground on pallets, and protected from moisture and contaminants. Avoid contact with strong oxidizing agents. Maintain good housekeeping to prevent dust accumulation. Follow the supplier’s SDS and local regulations.
    Shelf Life Shelf life is 24 months from date of manufacture when stored in unopened original packaging in a cool, dry, well-ventilated area.
    Application of Bayport Polymers (Baystar) HDPE 535

    Bayport Polymers (Baystar) HDPE 535 is supplied as an injection-molding high-density polyethylene with a nominal melt flow rate of 5.3 g/10 min at 190°C/2.16 kg (ISO 1133-1:2022) and a nominal density of 0.953 g/cm³ (ISO 1183-1:2019). The following scenarios are restricted to downstream processing routes where this melt-flow and density envelope is industrially applied: open-head containers, closures, thin-wall food packaging, logistics crates, ESD-protective material handling, and injection-welded automotive fluid reservoirs. Additive loadings in each section are expressed relative to total melt feed; the exact grade-specific certificate of analysis remains the controlling document for lot-to-lot variation. Statements concerning processing windows are drawn from production-scale machine behaviour and should be validated on the target tool and clamp configuration before commercial release.

    UN 1H2 Pails and Open-Head Industrial Containers

    Injection molding of open-head pails from HDPE 535 involves a coupling between sidewall draw direction and base thickness; the process is normally configured on a reciprocating-screw injection molding machine with clamp force from 600 t to 1000 t for 20 L containers, using a barrier screw with L/D ratio 20:1 to 24:1 and a four-to-six-drop valve-gated hot runner. Melt temperature is held between 200°C and 235°C, while the mold temperature is controlled at 15°C to 35°C to avoid persistent sink marks at the gate pad without producing excessive notch sensitivity in the bottom radius. When virgin fluff or pellet feed is processed, no predrying is required at relative humidity below 60%; if regrind has been exposed to humid storage or RH exceeds 60%, a predrying step at 80°C for 2 h is applied to prevent splay and gate blush. The formulation is run as 100 wt% HDPE 535 in natural or pigmented form, with colour masterbatch not exceeding 4 wt% because higher mineral-loaded colour concentrates reduce impact capacity at the handle boss. For solvent-transfer pails, antistatic concentrate is added at 1.5 wt% to 3.0 wt%; where outdoor stacking is specified, UV stabiliser masterbatch loading is set between 0.3 wt% and 0.8 wt%. Compliance documentation for industrial and food-tolerant pails references ASTM D4976 for the polyethylene material designation, ASTM D256 for notched Izod evaluation, ASTM D1693 Condition B for environmental stress-cracking resistance, FDA 21 CFR 177.1520 when the finished pail is intended for direct food contact, and UN 1H2 where the open-head plastic container is certified for dangerous-goods transport. Terminal part types are 20 L open-head pails, 5 gal buckets, and industrial containers fitted with metal or plastic carrying handles.

    Because cap and closure tools operate with multi-cavity hot runners and very short shot recovery windows, the melt-flow envelope of HDPE 535 at 5.3 g/10 min reduces injection pressure drop across 48-cavity to 96-cavity closure tooling relative to lower-melt-index HDPE grades; the density of 0.953 g/cm³ nevertheless imposes a narrow cushion and shot-size stability window, and short-shot defects appear when the screw cushion drops below 2–3 mm on high-clamp, thin-wall closure lines. The production route is injection molding on a reciprocating screw with L/D ratio 22:1 to 25:1, barrel melt temperatures from 210°C to 240°C, mold temperatures between 12°C and 30°C, and final hold pressures of 35–60 MPa; valve-gated or tunnel-gated cold runner systems are both used, with ejection of the undercut tamper-evident band requiring the stripper plate stroke to match the snap-ring extension specified by the cap design. In formulation, HDPE 535 is run at 97 wt% to 99.5 wt% of the melt feed, with colour or white masterbatch at 0.5 wt% to 2.0 wt%, erucamide slip concentrate at 0.1 wt% to 0.3 wt% when low removal torque is required, and silicone-based release concentrate at 0.2 wt% to 0.5 wt% for food-contact caps. All food-contact additives must be listed in FDA 21 CFR 177.1520 and Regulation (EU) No 10/2011; closures used for household chemical packages are additionally assessed against ISO 8317:2015 child-resistant test procedures. Terminal products are tamper-evident beverage cap shells, hinge caps for household chemicals, and snap-on overpacks for dairy or sauce containers.

    What Constrains Thin-Wall Freezer Tub Demolding After Fast Injection?

    High-speed thin-wall injection molding of freezer tubs from HDPE 535 is governed by the crystallisation temperature of the resin and the tool’s ejection timing. When wall sections below 0.8 mm are filled, injection speeds of 300–500 mm/s are used, with mold temperatures controlled at 10–20°C to force a quick crystalline skin and reduce cycle time; the risk is that excessively high cooling rates produce post-molding shrinkage anisotropy that distorts the tub lip and compromises lid fit. Processors therefore run a two-stage hold profile after the initial fill: a short high-pressure hold of 60–80 MPa for 0.2–0.5 s, followed by a low-pressure hold of 20–30 MPa until gate seal. The formulation is 95 wt% to 98 wt% HDPE 535, with white TiO₂ masterbatch at 2 wt% to 4 wt%, a nucleating agent masterbatch at 0.1 wt% to 0.3 wt% to raise crystallisation onset, and a processing aid/aluminium release package at 0.2 wt% to 0.5 wt%; slip/antiblock levels are kept low because excess surface migration defects on the sealing flange reduce lid engagement. Compliance is controlled by FDA 21 CFR 177.1520 and Regulation (EU) No 10/2011; specific migration evaluation of the additive package should be performed under the test conditions of EN 1186-1 and the analytical methods in EN 13130-1 where fatty-food simulants are selected. Terminal parts are 150 mL to 1 L dairy spread tubs, sauce pots, and freezer storage containers with snap lids.

    Where dairy case crates and returnable logistics totes are subjected to cold-chain condensation and repeated pallet stacking, the notch sensitivity of HDPE 535 under dynamic loading conditions is determined less by melt index than by wall-thickness distribution and gate freeze-off in the base grid. The process uses a reciprocating screw with L/D ratio 20:1 to 24:1, melt temperatures of 210–235°C, and mold temperatures of 10–25°C; the tool is configured with multiple direct edge gates or valve gates to fill deep rib intersections before freeze-off, and the injection machine clamp force for a full-size dairy crate typically falls between 1000 t and 1600 t. Shot weight is controlled because the base grid remains the highest warpage region; a minimum packing time of 8–12 s is common on solid crates to allow gate area crystallisation before ejection. The formulation uses 70 wt% to 80 wt% virgin HDPE 535 with 20 wt% to 30 wt% clean post-industrial regrind, provided the regrind fraction is tested for melt flow drift after 5 extrusion/injection cycles; carbon black masterbatch is added at 2 wt% to 4 wt% for outdoor stacking and UV creep resistance. Antioxidant and process stabiliser masterbatches are kept at 0.15 wt% to 0.35 wt%. Compliance for returnable logistic crates is specified by the distribution performance requirements of ASTM D4169, while material designation is recorded under ISO 11469:2016; food-contact dairy use requires the same FDA 21 CFR 177.1520 and EU 10/2011 documentation. Terminal product types are returnable dairy crates, bakery tray stacks, and collapsible logistics totes.

    When ESD-Safe Tote Inserts Require Controlled Surface Resistivity

    Electrostatic-dissipative component trays molded from HDPE 535 require surface resistivity values that remain stable after repeated detergent washing cycles, which limits the conductive additive composition and its deagglomeration inside the reciprocating screw. These trays are produced by injection molding with a compression ratio of 2.5:1 to 3.0:1 and a melt temperature window of 210–240°C; the tool is designed with generous edge radii and single-drop cold sprues to avoid dead spots where conductive carbon black can build up and then release as high-resistivity patches. The loading range for a proprietary carbon black masterbatch is 4 wt% to 8 wt%, and the exact value is selected to achieve surface resistivity between 10³ Ω/sq and 10⁶ Ω/sq under 12% RH test conditions, not merely at ambient 50% RH. Higher loadings above 8 wt% degrade tensile yield and create hot spots in the check ring; published data for this specific grade at loadings above 10 wt% is limited. Compliance is anchored to ANSI/ESD S20.20-2021 and IEC 61340-5-1:2016, with surface measurements performed according to IEC 61340-2-3. Terminal products are antistatic to static-dissipative trays, tote inserts, and PCB handling cassettes used in electronics assembly cells.

    Application scenarioStandard or regulationTest method designationControlled parameter
    Open-head pailsASTM D1693Condition B, 50°CESCR F50
    Caps and closuresISO 8317:2015Child-resistant package testOpening and closing torque cycles
    Thin-wall freezer tubsEU 10/2011EN 1186-1Overall migration in fatty-food simulant
    ESD traysANSI/ESD S20.20-2021IEC 61340-2-3Surface resistivity

    Automotive washer fluid reservoir molding places a specific demand on the weld line strength of HDPE 535 after two injection-molded shell halves are joined by hot plate or vibration welding. The shells are injection molded on clamp force 800–1200 t, with melt temperature 215–240°C, mold temperature 15–30°C; the outer shell wall is nominal 2.0–2.5 mm, and the injection pressure is set to meet a fill time below 2 s to avoid premature freeze at the weld flange. The formulation is 96 wt% to 98 wt% HDPE 535, with carbon black masterbatch at 2 wt%, antioxidant masterbatch at 0.2 wt% to 0.4 wt%, and no slip additive on the weld surface; if slip additive exceeds 0.1 wt%, weld line strength after vibration welding can fall below the burst-pressure criterion used by the Tier 1 supplier. Compliance documentation for material marking follows ISO 11469:2016; welded shell assemblies are evaluated for weld-line tensile integrity according to ISO 527-1:2019 and for cold impact resistance according to ISO 6603-1 at -30°C. Terminal products are automotive washer reservoirs and injection-welded fluid storage vessels for underhood installation.

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    Certification & Compliance
    More Introduction

    Bayport Polymers (Baystar) HDPE 535 is a high-molecular-weight high-density polyethylene copolymer supplied for extrusion blow molding of rigid intermediate-to-large containers. The grade is produced at the Bayport, Texas polyethylene complex and is specified around a high-load melt index rather than a conventional 2.16 kg melt index. That distinction is process-relevant: the resin is too viscous for reliable control at low load, and its melt strength is the controlling variable in accumulator-head parison stability. End-use areas include containers up to 60 L for agricultural chemicals, industrial solvents, aqueous concentrates, automotive fluids, water storage, and fuel tanks where environmental stress-cracking resistance and top-load rigidity are required.

    Typical published nominal values for HDPE 535 are summarized below. These values are not statistically guaranteed specification limits; the certificate of analysis for each lot should be obtained before setting release criteria. Density tolerance bands in commercial high-density polyethylene are commonly ±0.002 g/cm³, and high-load melt index may vary by ±0.5 g/10 min across production lots.

    PropertyTest MethodNominal Value
    DensityASTM D1505 / ISO 1183-10.954 g/cm³
    High-load melt index at 190 °C, 21.6 kgASTM D1238 / ISO 1133-15.5 g/10 min
    Melt flow rate at 190 °C, 2.16 kgASTM D1238Not a control value; typically below 0.1 g/10 min
    Tensile yield stressASTM D638-14 / ISO 527-228 MPa
    Tensile elongation at breakASTM D638-14>600 %
    Flexural modulusASTM D790-17 / ISO 1781,380 MPa
    Environmental stress-cracking resistance, 100% Igepal CO-630, F50ASTM D1693>600 h
    Brittleness temperatureASTM D746<-75 °C
    Vicat softening temperatureASTM D1525 / ISO 306 A50127 °C
    HardnessASTM D2240 / ISO 86865 D

    Mechanical test specimens are normally compression moulded and conditioned at 23 °C and 50 % relative humidity according to ASTM D618. Tensile properties are generated at 50 mm/min. The density of 0.954 g/cm³ places the grade in the rigid blow molding range; it is higher than typical medium-density polyethylene and allows a reduction in wall section at equivalent top-load performance. That density increase nevertheless reduces ultimate strain and low-temperature ductility when compared with lower-density MDPE. The trade-off is managed through comonomer placement, which maintains environmental stress-cracking resistance above 600 h in the standard ASTM D1693 100% Igepal F50 test.

    What Distinguishes a Dual-Loop Slurry HMW-HDPE from Conventional Unimodal Blow Molding Grades?

    At equal density, Baystar HDPE 535 differs from a conventional unimodal HDPE by a combination of molecular weight distribution, short-chain branch placement, and the resulting melt rheology. In a dual-loop slurry polymerization arrangement, ethylene-hexene copolymerization can be controlled to place comonomer preferentially on the higher-molecular-weight chains. This molecular architecture increases the population of load-bearing tie molecules between lamellae without lowering density below the required stiffness envelope. A chromium-catalyzed blow molding grade at identical density and high-load melt index may exhibit a broader molecular weight distribution and a different tie-molecule distribution, which can produce lower ESCR at equivalent flexural modulus. Therefore substitution by another HDPE on the basis of density and HLMI alone is technically insufficient.

    The practical consequence for processing is that HDPE 535 retains a longer parison hang time and a higher melt strength at low shear than general-purpose blow molding HDPE, while still flowing through the die at moderate head pressures. At shear rates below 0.1 s⁻¹, the molecular relaxation time is substantially longer than that of a fractional-melt HDPE used for small bottle blow molding. At die shear rates above 100 s⁻¹, shear thinning reduces apparent viscosity and prevents excessive head pressure. The grade-specific zero-shear viscosity is not routinely published on the technical data sheet and should be requested from the producer when a rheology simulation is planned.

    Processing or performance factorBaystar HDPE 535General-purpose blow moulding HDPEHigh-flow injection moulding HDPE
    Flow-control value5.5 g/10 min at 21.6 kg, ASTM D12380.30 g/10 min at 2.16 kg20 g/10 min at 2.16 kg
    Parison hang timeHigh; suitable for accumulator heads and large shot volumesModerate; suitable for continuous extrusion of small containersLow; unsuitable for large parison extrusion
    Typical ESCR in ASTM D1693, 100% Igepal F50>600 h30–150 h<30 h
    Typical flexural modulus1,380 MPa1,100–1,350 MPa1,000–1,200 MPa
    Primary process windowExtrusion blow moulding at 190–210 °C melt temperatureExtrusion blow moulding at 180–200 °CInjection moulding at 200–240 °C
    Critical limitationAvoid melt temperature above 230 °C; not intended for thin-wall injection mouldingLower ESCR; aggressive hydrocarbon containers may require a barrier linerPoor melt strength; not intended for large blow moulded parts

    The comparison values for the two generic HDPE classes are representative of commodity resin families rather than supplier-specific products. They are included to illustrate the differentiation mechanism, not as a substitute for a current competitor technical data sheet.

    On production accumulator-head lines, the substitution of HDPE 535 for a general-purpose blow moulding HDPE is usually driven by a field failure in environmental stress cracking rather than by a tensile data sheet difference. The pinch-off weld at the container bottom is a stress concentration where moulded-in strain remains high. In that zone, a low-ESCR blow moulding grade can crack after contact with alkyl aryl phosphates, surfactants, or hydrocarbon-based agricultural formulations. The high-molecular-weight tail in HDPE 535 increases the number of load-bearing tie molecules, which delays crack propagation in the ASTM D1693 test beyond 600 h. The benefit is material-specific and cannot be achieved by density control alone; high-density grades with the same 0.954 g/cm³ density may fail before 100 h if the comonomer distribution is unfavourable.

    Accumulator-Head Extrusion Blow Molding Parameter Limits and Die Gap Control

    Recommended processing of HDPE 535 on accumulator-head machines uses a barrier screw with a mixing section that imposes low shear work, typically a Maddock or pineapple configuration, and a barrel length of 24:1 to 30:1 L/D. Barrel set points are distributed from 160 °C near the feed throat to 190 °C at the die adapter, with die head zones held at 190–205 °C. Melt temperature at the die exit should remain between 190 and 210 °C. When die head pressure exceeds 35 MPa because of a narrow die gap or high throughput, shear heating may add 2–5 °C to the measured melt temperature; this offset must be established on the production line rather than assumed from barrel set points. Die lands are commonly chrome-plated and configured with a land length ratio of 10:1 to 15:1. A longer land may reduce melt fracture but does not eliminate the need for parison programming. Mold temperature is maintained at 10–25 °C to shorten cycle time. Colder molds can increase residual stress at the pinch-off and reduce the finished-part ESCR margin.

    Pellet moisture is not a direct processing concern because HDPE is not hygroscopic. Surface condensation can occur when pellets are transferred from an unheated silo into a warm indoor feed hopper, particularly if warehouse relative humidity exceeds 60 %. If condensation is visible, drying at 70 °C for 2 h is sufficient. Hot-air dryers above 90 °C are not recommended because pellet agglomeration and additive loss may occur. The grade is also not intended for thin-wall injection moulding, and blending with polypropylene or incompatible barrier scrap should be avoided in blow molding because the pinch-off weld can delaminate during subsequent drop testing.

    When Part Wall Thickness Must Remain Above 1.5 mm Across a 60 L Container

    Large-part blow molding with HDPE 535 shifts the critical control variable from melt index to parison programming. At a shot volume of 60 L, a uniform die gap typically produces wall-thickness variation exceeding 20% after inflation because the container circumference changes along the vertical axis. Accumulator-head machines therefore use servo-hydraulic die gap control with 50 to 150 programming points to vary the gap during parison extrusion. The high melt strength of HDPE 535 permits a parison length above 1.0 m before sag becomes critical, but the exact sag limit depends on parison weight, die diameter, melt temperature, and ambient air movement. Published data for this specific configuration is limited; processors should establish a head-specific swell curve by extruding a free parison and measuring its diameter at intervals before setting the gap profile.

    Agricultural chemical containers represent a demanding application because the packaged fluid may itself act as a stress-cracking agent. Containers made with HDPE 535 are usually tested on laboratory plaques according to ASTM D1693, but the finished part must also pass a filled-container drop test and a stack-creep test under the relevant United Nations packaging test protocol. The resin contributes to stress-cracking resistance but does not by itself provide barrier retention of aromatics or chlorinated solvents. For those fluids, surface fluorination or a multilayer structure with polyamide or EVOH is required. The HDPE layer in a fluorinated container must be processed with the same 230 °C melt-temperature ceiling because fluorination after moulding does not reverse thermal pre-damage.

    Fuel tank applications use HDPE 535 in multilayer coextruded structures that may contain EVOH, polyamide, and adhesive tie layers. The HDPE layers are extruded at 190–210 °C, while the barrier resin may require a separate temperature profile. Interlayer adhesion is evaluated by peel testing under ASTM D1876 or by falling-dart impact on the finished tank. Since HDPE 535 contains no maleated adhesion promoter, it is not a tie-layer resin and should not be used as a direct substrate for post-moulding adhesive lamination without surface treatment.

    Regulatory status is lot-specific and must be confirmed with the producer. Typical high-density polyethylene of this class is covered by FDA 21 CFR 177.1520(c) for direct food contact when the polymer meets extraction limits and the article is used under the specified conditions. For pharmaceutical packaging, a drug master file or food-contact statement should be requested. For potable water tanks, the finished article, not the resin alone, must demonstrate compliance with NSF/ANSI 61. Industrial chemical containers made from HDPE 535 require separate packaging certification because the resin does not provide a United Nations performance rating by itself.

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