| HS Code | 224447 |
| Density | 0.956 g/cm³ |
| Melt Flow Rate | 0.35 g/10 min (190°C/2.16 kg) |
| Tensile Strength At Yield | 26 MPa |
| Elongation At Break | >600% |
| Flexural Modulus | 1100 MPa |
| Izod Impact Strength Notched | 20 kJ/m² |
| Vicat Softening Temperature | 125°C |
| Heat Deflection Temperature | 75°C |
| Brittleness Temperature | < -70°C |
| Hardness Shore D | 65 |
| Environmental Stress Cracking Resistance | >1000 h |
| Water Absorption | <0.01% |
| Volume Resistivity | >10^16 Ω·cm |
| Dielectric Constant | 2.3 |
| Thermal Conductivity | 0.45 W/m·K |
| Mold Shrinkage | 1.5–3.0% |
| Processing Temperature | 180–220°C |
As an accredited Iran Petrochemical HDPE EX5 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Iran Petrochemical HDPE EX5 is packaged in 25 kg polyethylene-lined woven bags, palletized, or 1,000 kg jumbo bags for shipment. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with Iran Petrochemical HDPE EX5 in 25 kg bags, palletized, stretch-wrapped, and securely braced for transport. |
| Shipping | Iran Petrochemical HDPE EX5 is typically shipped as a non-hazardous thermoplastic resin in 25 kg PP/PE bags, palletized and loaded into 20'/40' dry containers. Sea freight is standard; keep dry, avoid direct sunlight and heat. Customs documentation and import/export compliance are required, subject to applicable trade sanctions. |
| Storage | Store Iran Petrochemical HDPE EX5 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep original bags sealed, palletized, and off the floor to prevent moisture and contamination. Avoid prolonged UV exposure and temperatures above 50°C. Use first-in, first-out stock rotation. Ensure good housekeeping and avoid puncturing packaging. |
| Shelf Life | Shelf life: 24 months in unopened original packaging, stored cool, dry, well-ventilated, away from direct sunlight and heat. |
Iran Petrochemical HDPE EX5, with a nominal melt mass-flow rate of 5.0 g/10 min under ISO 1133-1:2022 and a density of 0.954 g/cm³ under ISO 1183-1:2019, is formulated at 97–99 wt% neat resin for thin-wall dairy cup and margarine tub injection moulding. The remaining fraction comprises 0.5–2.0 wt% food-contact white masterbatch and, where automated denesting demands controlled surface slip, 0.2–0.8 wt% of a food-contact slip/antiblock masterbatch. Compliance for such containers is maintained under FDA 21 CFR 177.1520(c) for olefin polymers, Regulation (EU) No 10/2011 Annex I Table 1 as amended by EU 2020/1245, and GB 4806.6-2016, with overall migration testing executed according to EN 1186 where the finished cup is not protected by a functional barrier. Production on high-speed reciprocating-screw injection moulding machines uses a three-zone screw with an L/D ratio of 20:1 to 24:1, compression ratio of 2.5:1 to 3.0:1, melt temperature 200–230 °C, mould temperature 10–20 °C, injection velocity 80–120 cm³/s, and holding pressure 400–600 bar. The gate is dimensioned at or above 0.8 mm to delay freeze-off until packing has compensated shrinkage; below 0.6 mm, premature gate freeze produces sink marks and warpage at side-wall thicknesses below 0.5 mm. Mould cooling at 8 °C or lower in humid plants creates condensation and surface splay, while cooling above 30 °C extends cycle time without proportional gloss improvement. Terminal products are 200–1000 ml dairy cups, sour cream tubs, and margarine containers with stackable rim and anti-denesting lugs.
For single-piece HDPE screw closures, the HDPE EX5 fraction is held at 98–99.5 wt% with 0.5–2.0 wt% polyolefin-based colour masterbatch; erucamide slip masterbatch is added only when the finish torque specification requires reduction, at 0.05–0.2 wt%, and must be validated for organoleptic impact under Regulation (EU) No 10/2011 Annex I Table 1. The governing standards for food-contact closures are FDA 21 CFR 177.1520(c), Regulation (EU) No 10/2011, and GB 4806.6-2016; for child-resistant closure variants, ISO 8317:2015 test fixtures apply, while torque retention is tested under ASTM D2063-12. Multi-cavity tooling with valve-gate hot runners is used on injection moulding machines with direct pressure control and screw L/D of 20:1 to 22:1, melt temperature 210–240 °C, mould temperature 10–25 °C, injection velocity 60–100 cm³/s, and holding pressure 500–650 bar. Gate diameter below 0.7 mm accelerates gate freeze before full packing of the bridge thread, generating ovality and high torque variation; gate diameter above 1.2 mm slows cycle and leaves visible vestige that can violate consumer cap appearance limits. Valve gate wear in high-cavitation tools is monitored after 100,000 cycles by measuring gate vestige height and injection pressure slope; an increase in required peak pressure above 10% of baseline indicates pin seat galling from pigment abrasion. Terminal products are tamper-evident and non-tamper-evident screw caps for non-carbonated water, dairy, condiments, and personal-care bottles in diameters between 24 mm and 48 mm; carbonated beverage closure service is excluded unless specific ESCR testing under ASTM D1693-15 condition A and a barrier liner specification are met.
In open-head injection-moulded pails, the formulation is 94–97 wt% HDPE EX5, 2–3 wt% carbon black or inorganic pigment masterbatch, and 0.5–1.5 wt% UV stabilizer/antioxidant masterbatch; where static dissipation is required for flammable liquid packaging, an antistatic additive masterbatch is introduced at 0.5–2.0 wt%, but this addition reduces surface gloss and may require a separate UN compatibility test. The pails are type-tested as dangerous goods packagings under UN Recommendations on the Transport of Dangerous Goods Chapter 6.1, ADR/RID 2025, and 49 CFR 178.500 in the United States, with leak-proof, drop, and stacking tests performed on filled packages after soaking in the intended liquid at 23 °C and 40 °C for durations specified by the test authorities. Processing uses low-shear reciprocating screws with L/D 22:1 to 24:1, melt temperature 190–220 °C, mould temperature 15–30 °C, injection velocity 40–80 cm³/s, and holding pressure 350–500 bar; clamp force for a single-cavity 20 L pail mould typically exceeds 6000 kN, while multi-cavity 5 L tools may require more than 12,000 kN. Flashing at the lid seat below 0.02 mm is controlled by tool flatness and clamp pressure balance; flash above 0.05 mm leads to UN leak-proof test failure. Published plant data for HDPE EX5 specifically in UN pail qualification is limited, so independent testing agency verification of the finished pail remains mandatory. Terminal products are 5–25 L open-head pails for paints, lubricants, printing inks, detergents, and solvent-based construction chemicals.
| Process parameter | Thin-wall dairy cups | Multi-cavity screw closures | Open-head pails |
|---|---|---|---|
| Melt temperature | 200–230 °C | 210–240 °C | 190–220 °C |
| Mould temperature | 10–20 °C | 10–25 °C | 15–30 °C |
| Injection velocity | 80–120 cm³/s | 60–100 cm³/s | 40–80 cm³/s |
| Holding pressure | 400–600 bar | 500–650 bar | 350–500 bar |
| Gate thickness | 0.8–1.2 mm | 0.7–1.2 mm | 1.5–2.5 mm |
Regrind-rich beverage crate and bakery tray formulations use HDPE EX5 at 70–80 wt% virgin resin and 20–30 wt% clean in-house regrind, with 1–3 wt% colour masterbatch to mask grey shift and maintain batch-to-batch appearance. For trays in direct contact with unpackaged fruit, compliance with FDA 21 CFR 177.1520(c) and Regulation (EU) No 10/2011 is required; non-food logistics items are placed on the EU market under REACH and Directive 94/62/EC on packaging and packaging waste. Processing uses thick-walled injection moulds with melt temperature 200–230 °C, mould temperature 10–30 °C, injection velocity 35–60 cm³/s, holding pressure 300–450 bar, and cooling time 25–45 s for wall thickness 3.5–5.0 mm. Cross-contamination with polypropylene above 2 wt% must be avoided because it creates visible weld-line delamination and reduces ESCR; plants running both polymers on shared conveying lines use sequential purge cycles of 15–20 min and separate regrind bins. Regrind is dried to residual moisture below 0.05 wt% before blending to prevent surface splay and internal voiding. When measured under ISO 179-1:2010, notched Charpy impact declines in plant trials as regrind exceeds 30 wt%; for freezer applications, regrind is therefore capped at 20 wt%. Terminal products are bottle crates, bakery trays, fruit crates, and industrial logistics containers with load-bearing rib patterns and drainage apertures.
For child-resistant closures in pharmaceutical and household chemical packaging, HDPE EX5 is used at 98–99.5 wt% with 0.5–2.0 wt% high-purity masterbatch; external lubricants are restricted to 0.1 wt% maximum because higher levels migrate to the sealing surface and can alter cap-to-bottle bridge integrity. Compliance is established under ISO 8317:2015 for child-resistant packaging, USP <661.1> for plastic pharmaceutical packaging, Ph. Eur. 3.1.3, and FDA 21 CFR 177.1520(c) for olefin polymers in drug and food contact. Production uses closed-loop high-precision injection moulding machines with screw L/D 20:1 to 22:1, melt temperature 215–235 °C, mould temperature 15–25 °C, injection velocity 50–90 cm³/s, and holding pressure 500–650 bar. The hinge section is held to a thickness tolerance of ±0.05 mm; thinner sections commonly exhibit brittle failure during repeated opening under the ISO 8317:2015 protocol, while thicker sections increase push-down-and-turn forces beyond the senior-friendly limit. Tool steel wear in the hinge shut-off is measured after 50,000 cycles via flash thickness; flash above 0.03 mm indicates insert refurbishment is required. Terminal products include child-resistant caps for over-the-counter analgesics, vitamins, nutraceuticals, and household chemical bottles.
Household storage boxes and injection-moulded toy components are produced from 100 wt% virgin HDPE EX5 or from 75–90 wt% virgin resin with 10–25 wt% controlled internal regrind, with 1–4 wt% colour masterbatch selected for heavy-metal migration limits under toy safety law. For toys, compliance with EN 71-3:2019+A1:2021 migration of certain elements and REACH Annex XVII restrictions is mandatory; food-storage boxes are evaluated under FDA 21 CFR 177.1520(c) and Regulation (EU) No 10/2011 when direct food contact is claimed. Processing on low- to medium-pressure injection moulding machines uses melt temperature 190–220 °C, mould temperature 10–20 °C, injection velocity 30–60 cm³/s, and holding pressure 300–450 bar; multi-cavity cold-runner tools are fitted with sprue break or valve gates to reduce gate vestige on visible surfaces. Shrinkage compensation follows ISO 294-4:2018 and is typically between 0.8% and 2.0% for wall thicknesses 1.5–3.0 mm, requiring tool makers to adjust rib and boss dimensions before pilot tooling. Pellets stored outdoors or in elevated humidity should be conveyed through a hopper dryer at 70 °C for 2 h if surface moisture is visible; no prolonged desiccant drying is required for sealed, undamaged loads. Terminal products are stackable storage boxes, drawer organizers, toy construction blocks, and general household injection-moulded components.
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In the extrusion-grade high-density polyethylene portfolio of Iran Petrochemical, the grade designated HDPE EX5 is specified for medium-output rigid packaging, industrial profiles, drainage pipe, and selected pressure pipe applications in which melt strength, resistance to environmental stress cracking, and dimensional stability under load are controlled simultaneously. The resin is characterized by a broad molecular weight distribution and a moderate-high weight-average molecular weight, which produce shear-thinning behavior that is practical for reducing extruder torque while retaining enough melt elasticity to support pipe and profile dimensions before calibration. Commercial technical literature typically benchmarks this grade against ISO 1133-1:2022 for melt mass-flow rate and ISO 1183-1:2019 for density. The product is differentiated from high-flow injection grades and narrow-molecular-weight film grades by the balancing of extensional viscosity and flow-channel pressure drop, not by a single property value.
Commercial resin data sheets for Iran Petrochemical HDPE EX5 commonly list a base resin density of 0.947–0.951 g/cm³ after conditioning at 23 °C ± 2 °C under ISO 1183-1:2019. Melt mass-flow rate measured at 190 °C with a 2.16 kg dead weight in accordance with ISO 1133-1:2022, Method A, is typically controlled in the range 0.4–0.6 g/10 min. The 0.5 g/10 min class places the grade between blow moulding resins near 0.9 g/10 min and high-molecular-weight film resins below 0.1 g/10 min. This intermediate flow position affects screw fill, screw torque, die pressure, and shear heating. Because melt density and flow-rate ratio are sensitive to polymerization lot and pelletizing history, processors should verify the incoming certificate against the actual silo batch rather than reference nominal values only. Published data for this specific configuration is limited where the supplier certificate does not include the full extrusion curve; in such cases, a capillary rheometry sweep at 190 °C, 210 °C, and 230 °C is required before modifying tooling or screw design.
Single-screw extrusion of Iran Petrochemical HDPE EX5 is typically carried out on extruders with an L/D ratio of 30:1 or 33:1 and a barrier screw or Maddock mixing section. Barrel-zone set points are commonly profiled from 170 °C in the feed throat to 200 °C in the metering zone, while the adaptor and die are held at 190 °C–210 °C. At screw speeds above 90 min−1, sharkskin or melt fracture can appear when the die land length is short relative to the relaxation time of the melt. Production records from pipe lines using 75 mm single-screw extruders show that throughput reductions of 8–12% during switchover from lower-viscosity film resin eliminate surface scoring caused by unmelts. Screen packs combining 20/40/60 mesh layers are used to disperse micro-gels; extruder head pressure commonly rises by 0.5–1.5 MPa as screens load during a run. Screen change intervals should be based on that pressure rise rather than on fixed time. Melt temperature measured by an immersion probe should remain below 220 °C to limit antioxidant consumption and chain scission.
The selection of Iran Petrochemical HDPE EX5 over HDPE 5000S or HDPE 7000F is driven by the interaction of melt flow, density, and environmental stress-cracking resistance. HDPE 5000S is optimized for blow moulding with a melt flow rate near 0.9 g/10 min and a density near 0.954 g/cm³, giving high rigidity but reduced notched environmental stress-cracking resistance in aggressive surfactant solutions. HDPE 7000F is a film-extrusion grade with a melt flow rate near 0.04 g/10 min, providing high melt strength but requiring elevated melt temperatures that can degrade antioxidant packages and increase gel formation. EX5 occupies an intermediate viscosity window where pipe and profile dies maintain stable parison sag and drawdown without excessive head pressure. The difference is most evident in spiral mandrel dies where wall-thickness uniformity depends on controlled shear viscosity and die swell.
| Property | Test method | Iran Petrochemical HDPE EX5 | HDPE 5000S | HDPE 7000F |
|---|---|---|---|---|
| Melt flow rate at 190 °C/2.16 kg | ISO 1133-1:2022 | 0.4–0.6 g/10 min | 0.8–1.0 g/10 min | 0.03–0.05 g/10 min |
| Density at 23 °C | ISO 1183-1:2019 | 0.947–0.951 g/cm³ | 0.952–0.956 g/cm³ | 0.950–0.953 g/cm³ |
| Tensile yield stress | ISO 527-2 | 22–25 MPa | 24–28 MPa | 21–24 MPa |
| Notched ESCR, 10% Igepal CO-630 | ASTM D1693-15e1, condition B | 600–800 h | 100–300 h | 500–1,000 h |
These boundaries are representative of commercial data sheets and should not be interpreted as guaranteed lot certificates. The ESCR values are particularly sensitive to processing history, cooling rate, and specimen preparation. A direct substitution of EX5 into tooling designed for HDPE 5000S without pressure-drop verification can produce under-filled sections because the higher viscosity of EX5 shifts the operating point on the screw curve.
Mechanical property testing of extruded Iran Petrochemical HDPE EX5 is typically performed on compression-moulded plaques prepared under ISO 293:2023 or on specimens machined from extruded sheet. Tensile yield stress per ISO 527-2 is commonly reported between 22 and 25 MPa at 50 mm/min, while elongation at break frequently exceeds 600%. Flexural modulus under ISO 178:2019 is frequently in the range 900–1,100 MPa. These values are not sufficient for predicting pressure pipe performance; long-term hydrostatic strength under ISO 9080 is the governing design input for pressure service. For non-pressure drainage pipe, ring stiffness under ISO 9969 is controlled by wall thickness and pipe design rather than by resin modulus alone. Processors should not apply injection-moulded data to thick-wall pipe because cooling rates in solid-wall pipe are slower by orders of magnitude and produce through-thickness anisotropy.
Shear history in the die land and adaptor determines the surface finish and molecular orientation of Iran Petrochemical HDPE EX5. At high output, the resin exhibits sharkskin when the wall shear stress exceeds the critical threshold for melt fracture; this threshold is dependent on die geometry and melt temperature, not solely on melt flow rate. A die land length of at least 10 times the die gap is often maintained to allow stress relaxation before the free surface exits. Extrudate die swell is generally lower than that of HDPE 7000F because the lower molecular weight tail reduces elastic recovery after extensional flow. However, swell remains sufficient to require calibration sleeve entry angles below 8° to avoid scoring and drag marks. Melt orientation induced in the die can be locked in by rapid quenching; slow cooling in thick sections reduces orientation but increases residual shrinkage. Dimensional control therefore requires independent adjustment of water vacuum calibration, cooling-bath temperature, and haul-off tension.
Regulatory and compatibility constraints for Iran Petrochemical HDPE EX5 follow the standard limits for high-density polyethylene extrusion. The natural resin has low equilibrium moisture uptake, but surface condensation from outdoor storage at relative humidity above 60% can cause surface splay in the extrudate. A pre-drying step at 80 °C for 2 h is recommended when pellet surface moisture exceeds 0.05 wt% as measured by a halogen moisture balance. The resin should not be processed above 240 °C for extended residence times because oxidative chain scission accelerates and notched ESCR can decline. Copper-containing pigments and certain alkaline earth carboxylates should be avoided in high-temperature processing zones because they catalyze oxidative embrittlement. Residence time at 220 °C should be kept below 20 min. Food-contact compliance requires a converter-specific migration study under Regulation (EU) 10/2011; published data for this specific configuration is limited unless the finished article has been tested by the converter. The grade is supplied with lot-level certificates that typically include melt flow rate, density, tensile yield, and visual pellet contamination, but these certificate values do not replace process validation on the intended production line.