Exxonmobil Hdpe 4536pa

ExxonMobil HDPE 4536PA

    • Product Name: ExxonMobil HDPE 4536PA
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    VTB
    Specifications
    HS Code 601960
    Density 0.953 g/cm³
    Melt Mass Flow Rate 190 C 2 16 Kg 0.35 g/10 min
    Melt Volume Flow Rate 190 C 2 16 Kg 0.37 cm³/10 min
    Tensile Strength At Yield 28 MPa
    Tensile Strength At Break 30 MPa
    Elongation At Break >600%
    Flexural Modulus 1200 MPa
    Environmental Stress Cracking Resistance >1000 h
    Vicat Softening Temperature 125 °C
    Melting Temperature 133 °C
    Brittleness Temperature < -70 °C
    Hardness Shore D 65
    Thermal Conductivity 0.40 W/m·K
    Volume Resistivity >1E16 ohm·cm
    Dielectric Constant 2.3

    As an accredited ExxonMobil HDPE 4536PA factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing ExxonMobil HDPE 4536PA is packaged in 25 kg multiwall bags, palletized for transport, with 1,000 kg bulk options.
    Container Loading (20′ FCL) Container Loading (20′ FCL): ExxonMobil HDPE 4536PA in 25 kg bags, palletized, stretch-wrapped, and secured inside a 20-foot FCL container.
    Shipping ExxonMobil HDPE 4536PA ships as non-hazardous polyethylene resin pellets in 25 kg bags, 1,000 kg octabins, or bulk trucks/railcars. Keep containers closed, dry, and away from direct sunlight, heat, and ignition sources. Follow local regulations and supplier handling instructions.
    Storage Store ExxonMobil HDPE 4536PA in a cool, dry, well-ventilated area, away from direct sunlight, heat, flames, and strong oxidizers. Keep original containers or bags sealed to prevent moisture, dust, and contamination. Use clean handling equipment and first-in, first-out stock rotation. Avoid excessive heat and prolonged outdoor exposure. Follow the Safety Data Sheet and local regulations.
    Shelf Life ExxonMobil HDPE 4536PA has no fixed shelf life; store dry, cool, away from sunlight and contaminants for long-term stability.
    Application of ExxonMobil HDPE 4536PA
    In multi-cavity beverage closure tooling with 48 to 96 cavities, ExxonMobil HDPE 4536PA is processed on hydraulic injection moulding machines equipped with 45 mm reciprocating screws at L/D 22:1. The melt temperature window is held between 200 and 220 °C, and the cooling water temperature is kept at 12 to 18 °C to stabilize cap skirt dimensions and reduce post-mould shrinkage. The grade is specified with a nominal density of 0.945 g/cm³ under ISO 1183-1 and a melt mass-flow rate of 3.6 g/10 min at 190 °C under 2.16 kg load per ISO 1133-1:2022. That balance gives sufficient flow for cap skirts with wall thicknesses of 1.0 to 1.8 mm while avoiding the high molecular weight tail that produces unfilled tamper-evident band edges or short shots in the cap top-plate junction. In 64-cavity valve-gated hot runner tools with gate diameters of 0.8 to 1.2 mm, fill pressure typically reaches 60 to 80 MPa. Hold pressure is profiled from 45 MPa for 1.5 s to 25 MPa for 4.0 s. That stepped profile controls sink formation at the top-plate intersection without extending total cycle time beyond 9 to 14 s. Screw rotation speed is maintained at 80 to 120 rpm with back pressure of 4 to 7 MPa to disperse slip and antiblock masterbatches without pushing the melt temperature above the degradation threshold. Erucamide slip additive is blended at 600 to 1,000 ppm, and synthetic silica antiblock is added at 300 to 600 ppm. Both additives are pre-dispersed in a PE carrier masterbatch rather than added as neat powders to avoid screw slippage and local concentration gradients.Compliance for beverage closures is governed by FDA 21 CFR 177.1520, Regulation (EU) No 10/2011, and GB 4806.7-2016. Overall migration testing under EN 1186-1:2002 must not exceed 10 mg/dm² for aqueous, acidic, and alcoholic food simulants where applicable. The grade does not contain bisphenol A, phthalate plasticizers, or heavy-metal-based pigments. Closure performance is evaluated using ASTM D3198 for application and removal torque, ASTM D1693 condition B for environmental stress crack resistance, and ASTM D638-14 for tensile yield strength and elongation at break. Environmental stress crack resistance in aqueous citric acid and sodium benzoate solutions is critical because cap-to-neck interference generates constant hoop stress. Typical F50 values for this class of medium-flow HDPE exceed 100 h under ASTM D1693 condition B. Published data for this specific configuration is limited to supplier technical bulletins, so production qualification should include a 42-day closure-on-bottle ageing trial at 40 °C in still and carbonated water to detect stress cracking before shipment. Process limitations include a narrow melt temperature corridor. Below 195 °C, hot runner pressure drop increases and gate freeze-off occurs earlier. Above 230 °C, local molecular scission generates gel particles and increases the risk of odour-generating degradation species. Regrind from sprues and out-of-spec closures can be re-incorporated at 15 to 20 wt% without measurable loss of environmental stress crack resistance when the flake is dried at 80 °C for 2 h and blended gravimetrically. Above 25 wt% regrind, batch-to-batch variation in release torque and tamper-evident band rupture force becomes statistically significant. Mould maintenance on closure gates is required every 250,000 cycles because polyolefin volatiles and additive residue accumulate at the hot runner tip and cause asymmetric filling.
    Application sectorRegulatory or test requirementStandard / clauseCritical condition or limit
    Beverage closuresUS food contactFDA 21 CFR 177.1520Olefin polymer provisions; no BPA
    Beverage closuresEU food contactRegulation (EU) No 10/2011Overall migration ≤ 10 mg/dm²
    Beverage closuresTorque retentionASTM D3198Release torque determined by closure configuration and liner system
    Collapsible cratesAccelerated weatheringISO 4892-2 cycle AHALS at 0.10–0.15 wt% active content
    Collapsible cratesLow-temperature impactISO 6603-2Failure energy evaluated at -20 °C
    HousewaresEU food contactRegulation (EU) No 10/2011Overall migration ≤ 10 mg/dm²
    Industrial pailsUN dangerous goods packagingUN Model Regulations Chapter 6.1Drop testing at -18 °C; packing group dependent
    ToysMigration of elementsEN 71-3:2019+A1:2021Nineteen-element limits in mg/kg

    What Constrains Low-Temperature Impact in Collapsible Crate Hinge Zones?

    Collapsible logistics crates and folding pallet boxes moulded from 4536PA require a combination of hinge flexural fatigue resistance and drop impact survival at sub-zero temperatures. The grade’s density of 0.945 g/cm³ and flexural modulus near 1,100 MPa under ISO 178 provide sidewall rigidity, while elongation at break above 600% under ISO 527-2 permits hinged sections to be flexed for more than 10,000 cycles when the hinge thickness is held between 0.8 and 1.2 mm and the hinge radius is at least 0.4 mm. In production-scale tools with 4 to 8 cavities and hot tip or edge gating, melt temperatures of 210 to 230 °C and mould temperatures of 20 to 28 °C are used to increase crystallinity in the hinge area without producing warpage in the adjacent sidewall. Injection pressure commonly reaches 70 to 90 MPa, with hold pressure of 45 to 55 MPa for 5 to 8 s to pack bosses and snap-fit feet. Screw back pressure of 5 to 8 MPa disperses carbon black masterbatch at 2 wt% and HALS/UV stabilizer masterbatch at 1.5 to 3.0 wt% with a PE carrier. The active HALS content should remain at 0.10 to 0.15 wt% for outdoor weathering under ISO 4892-2 cycle A. Carbon black particle size and dispersion affect notched impact performance, so incoming masterbatch quality control must include a filter pressure test at 240 °C and a film quality rating under DIN 53774.Low-temperature impact is the primary failure mode. Dart impact or drop weight tests on crate panels at -20 °C are conducted according to ISO 6603-2. Failure energy for medium-flow HDPE of this density class typically falls between 40 and 60 J when wall thickness is 2.5 to 3.5 mm. Hinge stress whitening after repeated folding correlates with excessive orientation at the hinge surface from high injection speed. Reducing injection speed from 100 to 70 mm/s and increasing mould temperature to 28 °C reduces whitening but increases cooling time by 2 to 3 s. Crates intended for food logistics must comply with Regulation (EC) No 2023/2006 on good manufacturing practice for food contact materials. For non-food logistics, compliance with the Packaging and Packaging Waste Directive 94/62/EC and REACH Annex XVII restrictions is required. The grade does not contain UV-absorber stabilizers at levels that create migration risk. A processing boundary is the increased clamp force demand from thick hinge bosses, which can exceed the rated clamp force of smaller machines if cavity count is not reduced accordingly.

    Moulding Housewares and Small Appliance Components with Balanced Shrinkage

    Housewares such as storage bins, waste containers, and vacuum cleaner canisters are moulded with wall thicknesses from 1.5 to 3.0 mm, where the flow path length rarely exceeds 200 mm. In these tools, 4536PA is processed at melt temperature 195 to 215 °C with mould temperature 18 to 30 °C. The grade’s mould shrinkage under ISO 294-4 is typically recorded in the range of 1.5 to 2.2% in the flow direction and 1.8 to 2.5% transverse, so gate placement must be arranged to avoid differential shrinkage at the base corners of rectangular bins. Warpage is controlled by maintaining uniform wall thickness and using rounded transitions with radii of at least 2 mm at rib intersections. In production, a 350-tonne injection moulding machine with a 50 mm screw and L/D 22:1 is typically used. The plasticating capacity is sufficient to process 12 to 18 kg/h without excessive residence time. Masterbatch dosage for household articles is typically 2 wt% with an LDPE carrier. Polyolefin pigments such as phthalocyanine blue and carbon black are used because they do not promote oxidative degradation at normal processing temperatures.For food-contact storage containers, the base resin and masterbatch must comply with FDA 21 CFR 177.1520 para (c) 2.1 and Regulation (EU) No 10/2011. The overall migration limit of 10 mg/dm² applies to aqueous, acidic, and fatty simulants. For fatty foods, simulant D2 or 95% ethanol is used under EN 1186 methods. Small appliance housings that are not food contact fall under RoHS 2011/65/EU with maximum 0.1% lead and 0.01% cadmium in homogeneous materials, and REACH Regulation (EC) No 1907/2006 SVHC screening. Processing limitations are tied to screw residence time. At melt temperatures above 220 °C and screw speed below 60 rpm, residence times above 6 min can generate yellowing in natural grades. A purging procedure with a low-MFI LDPE at 180 °C after shutdown reduces carbonized specks in subsequent runs. The grade is not suited to ultra-thin-wall housewares with nominal wall thickness below 0.6 mm because the moderate melt mass-flow rate limits flow length at high cavity counts.For 5-L to 25-L open-head pails and tight-head containers, 4536PA is processed on machines with clamp forces from 400 to 1,000 tonnes depending on projected area. The melt temperature is increased to 210 to 230 °C to fill the thicker handle sections and sidewall ribs, while the mould temperature is held at 15 to 25 °C to minimize cycle time. Typical sidewall thickness is 2.0 to 3.0 mm, with handle boss sections up to 6 mm thick requiring extended hold pressure. Injection pressure is set at 75 to 95 MPa, and hold pressure of 50 to 60 MPa is maintained for 8 to 12 s to prevent sink marks and internal voids at the handle attachment. Screw back pressure of 3 to 5 MPa is kept lower than in closure production because the larger screw diameter and longer residence time make the melt sensitive to shear work. Carbon black masterbatch at 1.5 to 2.5 wt% with a PE carrier provides UV stabilization for outdoor storage, but the carbon black particle size and dispersion affect notched impact performance at low temperature.UN certification for dangerous goods packaging requires the pail to pass leakproofness, stack load, and drop tests under UN Model Regulations Chapter 6.1. Drop testing at -18 °C is performed from heights determined by packaging group and specific gravity. A common requirement for 1.4 relative density material is a drop height of 1.2 m for Packing Group II. The grade’s environmental stress crack resistance under ASTM D1693 condition B is critical for pails that contain surfactant solutions or agricultural adjuvants. F50 values above 200 h are expected for this product class when moulded at the specified thickness. Compatibility testing with the actual chemical formulation is mandatory because HDPE can stress crack in the presence of strong oxidizing agents, aromatic hydrocarbons, and nonylphenol ethoxylates. The open-head design must maintain a secure gasket seat. Dimensional tolerance across the pail rim is checked with a go/no-go fixture calibrated to ±0.25 mm. Recycled or regrind content is generally limited to 20 wt% for UN-rated packaging unless the plant maintains a validated closed-loop regrind stream with lot traceability to the originating food-grade or industrial-grade production. A processing limitation is the extended cooling time required at handle bosses; if demoulded too early, the bosses exhibit internal voids that reduce stack load performance.

    When Toy and Sporting Component Acceptance Depends on Fracture Limits and Migration Testing

    Toy storage bins, ride-on toy wheels, and gymnasium accessories moulded from 4536PA are evaluated against EN 71-1:2014+A1:2018 mechanical and physical properties and ASTM F963-23. The process window is shifted toward lower melt temperatures of 190 to 210 °C to reduce odour and volatile organic emissions from the melt, although mould temperatures are kept at 20 to 30 °C to maintain surface gloss and reduce sink marks in thick toy wheels. Wall thicknesses range from 2.0 to 4.0 mm, and the flow length generally remains below 150 mm. Fill speed is reduced to 50 to 80 mm/s to prevent jetting and gate blush in large flat surfaces. Hold pressure of 35 to 45 MPa for 6 to 10 s packs the thick sections without introducing excessive stress at the gate. Colour masterbatch is dosed at 2 to 3 wt% with an LDPE carrier. Heavy-metal-free pigments are required, and the masterbatch must be screened under EN 71-3:2019+A1:2021 for migration of nineteen elements. For child-care articles, phthalate content is restricted under REACH Annex XVII entries 51 and 52, with limits below 0.1% for each restricted phthalate.The fracture behaviour of toy components is assessed by drop testing from 1.0 to 1.5 m onto a steel plate. The HDPE part must not produce small parts or sharp edges. Notched Izod impact under ISO 180/A is used for incoming quality control, with typical values for this grade class from 4 to 6 kJ/m² at 23 °C. At low temperatures, impact strength declines, so outdoor toys intended for use below -10 °C require a specific conditioning test at -20 °C for 24 h before drop testing. A limitation is the grade’s relatively low melt flow compared with high-flow HDPE used for thin-walled toy components. When wall thickness is below 1.0 mm, insufficient flow length and high injection pressure may cause short shots and increased gate stress. For sporting goods such as storage boxes and target frames, falling-weight impact is evaluated under ISO 6272-1. Stress whitening after impact is visually inspected under standardized lighting conditions to establish acceptable quality limits. The grade should not be combined with amine-based flame retardant systems because such additives can react with the carbonyl species formed at high processing temperatures and produce discolouration or reduced thermal stability.
    Free Quote

    Competitive ExxonMobil HDPE 4536PA prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8618005193850 or mail to sales8@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8618005193850

    Email: sales8@ascent-chem.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    When downstream converters evaluate high-density polyethylene for rigid packaging and industrial containers, ExxonMobil HDPE 4536PA is generally positioned as a blow-moulding resin with a nominal density of 0.945 g/cm³ under ASTM D1505 and ISO 1183-1:2019, and a melt flow rate of 0.36 g/10 min at 190 °C and 2.16 kg as specified in ASTM D1238-20 and ISO 1133-1:2022. The combination of low melt flow rate and mid-range density indicates a material of higher average molecular weight than typical thin-wall injection-moulding HDPE. Published data for this specific configuration in secondary literature is limited; current lot-specific certificates of analysis should therefore be used before tooling is cut or clamp-force limits are established.

    On production-scale extrusion blow-moulding lines equipped with single-screw diameters from 50 mm to 90 mm and L/D ratios of 24:1 to 30:1, the material processes most stably at a melt temperature of 190–210 °C. Below 180 °C, melt pressure at the die head can exceed 350 bar, and sharkskin melt fracture may appear on the parison. Above 220 °C with residence times beyond 8–10 min, oxidative degradation can produce gel particles and reduce notched impact resistance when measured under ASTM D256. Hopper drying at 60–70 °C for 2 h is recommended only when the resin has been stored at relative humidity greater than 60%; otherwise, internal moisture levels below 0.01% generally do not require pre-drying. The operational failure mode most commonly observed in blow-moulding plants is parison sag variation during ambient temperature changes. Because the melt flow rate is low, a melt temperature drift of ±5 °C can alter parison length by ±8% on a 55 mm grooved-feed extruder with 24:1 L/D, leading to wall-thickness deviation in containers with nominal wall thickness below 1.2 mm. Closed-loop melt pump control and parison programmer adjustment are generally required.

    Does the Low Melt Flow Rate Restrict the Grade to Blow Moulding Only?

    In practice, the grade is not restricted to blow moulding, but the process window narrows when it is used in injection moulding or sheet extrusion. The measured melt flow rate of 0.36 g/10 min under ASTM D1238 corresponds to high melt viscosity and limits flow-length-to-wall-thickness ratios in injection moulding to approximately 150:1. Beyond that threshold, cavity pressure can exceed 1,200 bar on a 150 t injection-moulding machine, and weld-line tensile strength may fall below the value required for hydrocarbon-containing fluids when tested as Type IV specimens under ASTM D638-14. In thick-wall profiles and sheet extrusion, however, the same melt strength reduces draw-down and edge sag. The distinction from a 20 g/10 min injection-moulding grade is therefore not merely flow rate but the practical consequence that cooling time in thick sections may increase by 30–50% because of longer heat removal from the slower-flowing, higher-molecular-weight melt.

    When dry blending a color concentrate at 2–4 wt%, pellet-to-pellet viscosity mismatch can create local colour streaks if the concentrate carrier has a melt flow rate above 20 g/10 min. The recommended practice is to use a concentrate based on an HDPE carrier with a melt flow rate within 0.5–2.0 g/10 min or to pre-compound on a 40 mm twin-screw extruder with L/D 40:1 and distributive mixing elements. Colour uniformity is conventionally assessed by ASTM D2244 using a colour difference value below 1.0 ΔE*ab across the part surface. Addition of external lubricant or fluoropolymer processing aid above 2.5 wt% may reduce die-wall friction enough to delay solidification and produce a rough internal parison surface at die gaps below 1.2 mm. In high-gloss applications requiring processing aid levels above 2.0 wt%, a pre-dispersed masterbatch and head-pressure stability log are recommended before production approval.

    When Cross-Compared Against Pipe Grades and Film Resins

    At the same nominal density of 0.945 g/cm³, the product differs from a high-load melt index pipe grade in molecular architecture and in the test protocol used to measure long-term performance. Pipe grades are routinely evaluated by ISO 9080 or ASTM D2837 for long-term hydrostatic strength, whereas blow-moulding grades are more commonly qualified by environmental stress-cracking resistance under ASTM D1693 and by drop-impact resistance under ASTM D2463. The grade is also distinct from high-density film resins with melt flow rates above 1.0 g/10 min, which permit thinner gauge and higher line speeds but do not provide the same parison melt strength in large-part blow moulding. In terms of shear viscosity, class-level comparisons at 190 °C and 10 s⁻¹ place this molecular weight class in the 4,000–6,000 Pa·s range, while pipe grades of the same density may exceed 8,000 Pa·s and injection-moulding grades may fall below 800 Pa·s.

    This differentiation also affects regrind strategy. In blow-moulding operations, regrind of 4536PA can typically be added back at 20–30 wt% without eliminating the ESCR safety margin, provided the regrind is free of polypropylene contamination above 5 wt%. Polypropylene above that level forms a discrete dispersed phase that reduces stress-cracking resistance and can be detected by differential scanning calorimetry as a second melting peak between 160 °C and 165 °C under ISO 11357-3:2018. Higher regrind levels require verification of filled-container drop-impact performance and top-load resistance, not simply a melt-flow check.

    Thermal analysis under ISO 11357-3:2018 generally indicates a peak melting temperature near 128–132 °C for HDPE in this density class. The cooling water temperature in blow-moulding moulds is typically maintained at 10–30 °C to achieve a crystallinity level that balances stiffness and impact. Higher mould temperatures may increase crystallinity and top-load strength but can extend cycle time and increase shrinkage after demoulding; lower mould temperatures can quench the surface too rapidly, producing internal voids in thick sections. The practical mould temperature should be validated with a pressure sensor or thermocouple installed in the mould cavity, not inferred from chiller setpoint alone.

    Specification Values Reported for the Grade

    The following values are compiled from class-level manufacturer literature and should be verified against the current product datasheet. They are not intended as a purchase specification.

    PropertyTest methodPublished typical valueUnit
    Melt flow rate (190 °C, 2.16 kg)ASTM D1238-20 / ISO 1133-1:20220.36g/10 min
    DensityASTM D1505 / ISO 1183-1:20190.945g/cm³
    Tensile yield strengthASTM D638-14 Type IV / ISO 527-2:201225MPa
    Flexural modulusASTM D790-17 / ISO 178:20191,000MPa
    Environmental stress-cracking resistance, 100% Igepal, Condition BASTM D1693-15>600h
    Vicat softening temperature, A/50ASTM D1525-17e1 / ISO 306:2022124°C

    The ESCR value is highly dependent on moulded-in stress, test temperature, and surfactant concentration. A value above 600 h does not guarantee resistance to all hydrocarbon or detergent environments; end-use testing under ASTM D1693 is required for each final container design.

    Resin stored at high relative humidity or exposed to outdoor conditions can pick up surface moisture. If the container is to be used in a hot-fill application above 80 °C, the grade should be dried and the final article tested for dimensional stability under ASTM D648 or a customer-specific hot-fill protocol. The product is not recommended for continuous contact with strong oxidizers, aromatic hydrocarbons, or chlorinated solvents; these agents can plasticize the amorphous phase and reduce the apparent ESCR. In such cases, a fluoropolymer-lined container or a different polymer class is usually required.

    Evaluating Food-Contact Status and Regulatory Test Boundaries

    For food-contact applications in the United States, the base HDPE polymer is generally covered by 21 CFR 177.1520, which specifies extractive limits and end-use temperature restrictions for olefin polymers. In the European Union, compliance is governed by Commission Regulation (EU) No 10/2011, including an overall migration limit of 10 mg/dm² and specific migration limits for additives and monomers. A grade-specific declaration from the manufacturer is necessary because catalyst residues, antioxidant packages, and processing aids can shift between production campaigns. The product is not recommended for continuous contact with strong oxidizers, aromatic hydrocarbons, or chlorinated solvents. Continuous-use temperature above 80 °C in contact with aggressive detergents should be validated by migration testing and environmental stress-cracking resistance testing on the finished article.

    For industrial articles sold in the European Economic Area, REACH SVHC declarations should be obtained from the resin supplier; if no SVHC is present above 0.1% w/w, the article is outside the notification duty under Article 7(2) of Regulation (EC) No 1907/2006 for that substance. The product is not within the scope of Directive 2011/65/EU (RoHS) unless the final electrotechnical article places it under the directive; the resin itself does not contain lead, cadmium, mercury, hexavalent chromium, PBB, or PBDE above the RoHS maximum concentration values.

    In multilayer coextruded containers, 4536PA is typically used as the structural high-density polyethylene layer because its density and melt strength provide stiffness and parison stability. The tie layer and barrier layer are selected separately; the HDPE layer must be tested for interlayer adhesion using ASTM F88/F88M or a peel test appropriate to the container geometry. At processing temperatures below 210 °C, interlayer adhesion is generally stable, but at temperatures above 220 °C, oxidation of the HDPE surface can reduce bond strength. In such constructions, the use of regrind containing the barrier polymer should be limited to levels that do not reduce the environmental stress-cracking resistance of the structural layer; data for the specific regrind concentration is limited and must be qualified on the production line.

    Top