| 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 | 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 sector | Regulatory or test requirement | Standard / clause | Critical condition or limit |
|---|---|---|---|
| Beverage closures | US food contact | FDA 21 CFR 177.1520 | Olefin polymer provisions; no BPA |
| Beverage closures | EU food contact | Regulation (EU) No 10/2011 | Overall migration ≤ 10 mg/dm² |
| Beverage closures | Torque retention | ASTM D3198 | Release torque determined by closure configuration and liner system |
| Collapsible crates | Accelerated weathering | ISO 4892-2 cycle A | HALS at 0.10–0.15 wt% active content |
| Collapsible crates | Low-temperature impact | ISO 6603-2 | Failure energy evaluated at -20 °C |
| Housewares | EU food contact | Regulation (EU) No 10/2011 | Overall migration ≤ 10 mg/dm² |
| Industrial pails | UN dangerous goods packaging | UN Model Regulations Chapter 6.1 | Drop testing at -18 °C; packing group dependent |
| Toys | Migration of elements | EN 71-3:2019+A1:2021 | Nineteen-element limits in mg/kg |
Competitive ExxonMobil HDPE 4536PA prices that fit your budget—flexible terms and customized quotes for every order.
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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.
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.
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.
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.
| Property | Test method | Published typical value | Unit |
|---|---|---|---|
| Melt flow rate (190 °C, 2.16 kg) | ASTM D1238-20 / ISO 1133-1:2022 | 0.36 | g/10 min |
| Density | ASTM D1505 / ISO 1183-1:2019 | 0.945 | g/cm³ |
| Tensile yield strength | ASTM D638-14 Type IV / ISO 527-2:2012 | 25 | MPa |
| Flexural modulus | ASTM D790-17 / ISO 178:2019 | 1,000 | MPa |
| Environmental stress-cracking resistance, 100% Igepal, Condition B | ASTM D1693-15 | >600 | h |
| Vicat softening temperature, A/50 | ASTM D1525-17e1 / ISO 306:2022 | 124 | °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.
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.