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Iran Petrochemical HDPE I3

    • Product Name: Iran Petrochemical HDPE I3
    • 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 123787
    Volume Resistivity Ohm Cm 1E16
    Coefficient Linear Thermal Expansion Per C 1.2E-4
    Mold Shrinkage Percent 1.5-3.0
    Crystallinity Percent 70-80

    As an accredited Iran Petrochemical HDPE I3 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Iran Petrochemical HDPE I3 is typically packed in 25 kg PP woven bags, 40 bags per 1,000 kg pallet.
    Container Loading (20′ FCL) Container Loading (20′ FCL): Iran Petrochemical HDPE I3 in 25kg bags, palletized or loose, approx. 20–25MT, securely stowed for export.
    Shipping Iran Petrochemical HDPE I3 is a non-hazardous solid high-density polyethylene resin, shipped in 25 kg PP bags, palletized and shrink-wrapped. It is typically transported in 20-foot FCL containers by sea. Keep dry, cool, and away from direct sunlight and contamination. No special hazardous cargo handling required.
    Storage Store Iran Petrochemical HDPE I3 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and strong oxidizers. Keep original bags sealed, palletized, and off the floor to prevent moisture and contamination. Avoid excessive stacking to prevent deformation. Maintain good housekeeping; no smoking. Use first-in, first-out stock rotation and keep containers labeled. Do not store near food or drinking water.
    Shelf Life Iran Petrochemical HDPE I3 shelf life typically about 24 months if kept cool, dry, sealed, and away from direct sunlight.
    Application of Iran Petrochemical HDPE I3

    In high-cavitation closure moulds with 48 to 96 cavities, Iran Petrochemical HDPE I3 is injected through hot-runner valve gates at melt temperatures of 210–230 °C measured at the nozzle. The melt mass-flow rate of 8.0–10.0 g/10 min under 190 °C/2.16 kg load according to ISO 1133-1:2022 permits thin-walled tamper-evident band formation without excessive cavity pressure. The supplier-specified density of 0.952–0.956 g/cm³ under ISO 1183-1:2019 keeps closure shells below 3.8 g in a dimensionally stable window. Hydraulic injection pressure is limited to 70–110 MPa, while cavity pressure transducers maintain 30–45 MPa at the gate. Valve gate tip diameters of 0.6–1.2 mm per cavity reduce gate vestige height. Mould coolant enters at 8–15 °C to accelerate cap skirt solidification. Cycle time on a 160–350 t hydraulic injection moulding machine runs 4.8–7.5 s for closure shells of 2.5–3.8 g. Shrinkage along flow is 1.5–2.2% and cross-flow shrinkage is 1.8–2.5%, measured on ISO 294-4 plaques. Erucamide slip is compounded at 500–1200 ppm to bring cap removal torque into the packaging line acceptance band. The antioxidant system is retained at 800–1500 ppm from the supplier package to avoid oxidative yellowing. Food-contact compliance relies on FDA 21 CFR 177.1520(c) 3.2a and Regulation (EU) No 10/2011, with overall migration below 10 mg/dm². Gate vestige above 0.25 mm or closure skirt warpage above 0.4 mm produces capping-line vision rejects and tamper-band interference. The principal process conflict is that increasing melt temperature above 240 °C can improve fill but creates organoleptic failure in mineral water closures. I3 therefore sits below that ceiling for high-cavitation beverage work.

    What Limits Continuous Stacking Load in 25 L Industrial Pail Handles Made from I3?

    A 25 L pail handle moulded from I3 carries a bail-lift load in continuous stacking and drop testing. The handle section is typically 3.0–4.5 mm thick, with either a moulded-in pin post or a separate metal bail inserted on the assembly line. Melt temperature is held at 220–250 °C at the nozzle to fill the handle boss and pail rim in a single-cavity or two-cavity tool. Hydraulic injection pressure reaches 80–120 MPa, and hold pressure is maintained at 50–70 MPa for 10–15 s. The gate is a hot tip with 1.2–2.0 mm diameter placed opposite the handle attachment to reduce weld-line exposure at the bail-load point. Mould coolant is set at 8–15 °C because thick walls above 4.0 mm delay solidification and increase cycle time. Back pressure is held at 0.8–1.2 MPa to maintain melt homogeneity during screw recovery. Regrind from clean post-industrial scrap may be added up to 20 wt% only when the pail is non-hazardous. For UN 1H2 solid-dangerous-goods pails, the regrind ratio and source must be part of the original type approval and cannot be changed without retesting. Drop testing under UN 6.1.5.3 and stacking-load testing at 23 °C are performed on finished pails. I3 is suitable for 5–25 L open-top pails for water-based detergents, adhesives, paint, and bulk food ingredients with a liner. The limitation appears when the handle is moulded with insufficient packing: a sink mark at the boss root deeper than 0.15 mm reduces load-bearing area. Tool venting at the handle tip must be kept open. Blocked vents create short shots that fail bail-lift testing. Published data for I3-specific stack-load retention after long-term warehouse storage is limited; load tests should be validated on the actual pail geometry.

    Windshield Washer Reservoir Weld Line Integrity at -30 °C

    Windshield washer reservoirs moulded from I3 are filled in tools with wall sections of 2.0–3.0 mm, usually in P20 or 7075 aluminium mould bases. Melt temperature is raised to 230–250 °C at the nozzle to force weld lines at the pump boss and level-sensor boss to knit above the brittle-ductile transition. Mould temperature is held at 25–40 °C with pressurised water or cartridge heaters to slow weld-line skin formation. Hydraulic injection pressure is 90–130 MPa; hold pressure is 50–60 MPa for 15–25 s. A sub-gate or tunnel gate of 1.0–1.5 mm diameter is positioned away from the instrument bosses to reduce gate scar at the sealing face. Weld-line Charpy impact is assessed according to ISO 179-1/1eA at -30 °C, and the part is conditioned in washer fluid under ISO 175 before long-term under-bonnet approval. Carbon black masterbatch at 2.0–2.5 wt% is used for black parts. External mould release is not applied because pump grommet adhesion and sensor clip retention demand a clean surface. Screw boss torque is held below 2.5 N·m on M5 inserts to avoid radial cracking. The process boundary is severe: mould temperatures below 20 °C produce visible knit-line stress whitening at the sensor boss, while melt temperatures above 250 °C shorten polymer residence-time stability. I3 is appropriate when the application is validated down to -30 °C. For cold-climate programmes requiring -40 °C impact retention, a higher molecular weight HDPE or impact-modified PP should be screened.

    Representative injection moulding parameters for Iran Petrochemical HDPE I3 across selected downstream conversion units
    ParameterBeverage closure shells25 L industrial pailsWasher reservoirsFrozen food trays
    Melt temperature at nozzle210–230 °C220–250 °C230–250 °C200–220 °C
    Mould coolant inlet8–15 °C8–15 °C25–40 °C8–12 °C
    Hydraulic injection pressure70–110 MPa80–120 MPa90–130 MPa90–120 MPa
    Hold pressure30–45 MPa50–70 MPa50–60 MPa35–50 MPa
    Back pressure0.6–0.8 MPa0.8–1.2 MPa0.7–1.0 MPa0.5–0.7 MPa
    Cooling time3–5 s12–18 s15–25 s2.5–4.0 s
    Gate typeValve gate 0.6–1.2 mmHot tip 1.2–2.0 mmSub-gate/tunnel gate 1.0–1.5 mmHot-runner edge gate 0.8–1.0 mm
    Nominal wall section0.8–1.2 mm2.5–4.0 mm2.0–3.0 mm0.8–1.5 mm

    For thin-wall frozen food tray tools with 8 to 16 cavities, I3 is injected at melt temperatures of 200–220 °C. The mould coolant is maintained at 8–12 °C to shorten cycle time and reduce post-ejection distortion. Wall thickness ranges from 0.8–1.5 mm, which requires fast filling through hot-runner edge gates of 0.8–1.0 mm diameter. Filling time is controlled at 0.4–0.7 s, with hold pressure set to 35–50 MPa and cooling time at 2.5–4.0 s. Clamp force per cavity is 35–50 kN, depending on projected area and melt pressure. The grade does not require routine drying. When cold-stored resin enters a humid plant and hopper residence exceeds 8 h at relative humidity above 70%, pre-drying at 80 °C for 2 h prevents surface splay. Food-contact compliance under FDA 21 CFR 177.1520(c) and Regulation (EU) No 10/2011 requires that only authorised slip and antioxidant packages are used. Post-consumer recyclate is not accepted in this application unless a functional barrier is demonstrated or regulatory authorisation is obtained. Sink marks around the rim occur when holding pressure falls below 35 MPa or when the gate freezes before part packing completes. Differential shrinkage after ejection is controlled by coolant temperature uniformity of ±1 °C across the tool face. Finished articles are frozen food trays and dairy tubs with stackable rims.

    When I3 Is Moulded into Agrochemical Overcaps with Child-Resistant Torque Requirements

    When agrochemical overcap threads are specified with ISO 8317 child-resistant torque, the I3 part must pass sequential opening torque, closing torque, and environmental stress crack exposure. The overcap wall thickness is 1.2–2.5 mm and the thread form is a continuous or interrupted buttress thread. Melt temperature is set at 215–235 °C at the nozzle. Mould temperature is 12–18 °C to maintain thread roundness after ejection. Injection pressure is 80–110 MPa and hold pressure is 40–55 MPa. The acid scavenger, typically calcium stearate, is limited to 500–1000 ppm to avoid excessive die build-up. Antioxidant from the supplier package remains at 800–1500 ppm. Colour masterbatch is added at 1.5–4.0 wt% for code-specific cap colours. Slip additives are generally not added when child-resistant torque retention is critical because they can reduce removal torque below the minimum after 24 h. The finished overcaps include 28 mm, 38 mm, and 53 mm sizes for detergent and agrochemical bottles. Continuous contact with aromatic solvents or strong oxidisers at temperatures above 50 °C is outside the recommended service envelope for I3 because environmental stress cracking can develop at the thread root. Published data for I3 ESCR in specific agrochemical formulations is limited; closure compatibility must be tested on the specific bottle neck and induction seal.

    Slot Flash in Nursery Pot Tools Is Governed by Clamp Force per Cavity

    Nursery pot tools running I3 at cycle times of 20–35 s demand controlled clamp force per cavity to control drainage slot flash. Stack moulds or multi-cavity tools are used with four to twelve cavities depending on pot diameter. Melt temperature is held at 210–230 °C and mould temperature at 15–20 °C. Wall thickness ranges from 1.5–3.0 mm for pots from 0.5 L to 5 L. Hold pressure is 35–45 MPa and hydraulic injection pressure is 70–100 MPa. Carbon black at 2.0–2.5 wt% is the lowest-cost ultraviolet stabiliser for black pots. For white pots, titanium dioxide is used at 1.5–3.0 wt%. A hindered amine light stabiliser may be added at 0.15–0.50 wt% where the pot must maintain impact after 1000 h of xenon-arc exposure under ISO 4892-2. Published data for I3 at these exact stabiliser loadings in nursery pot grades is limited; field validation against a reference compound is required. Flash thickness above 0.10 mm on drainage slots interferes with denesting and is a primary mould-shift indicator. The operational limitation is outdoor service life: without adequate carbon black or UV stabiliser, the polymer loses surface gloss and tensile impact at different rates depending on solar exposure. No single laboratory weathering cycle substitutes for multi-year field data. Finished articles are nursery pots, propagation trays, and landscape containers.

    Compliance matrix for I3 downstream segments
    SegmentRegulatory basisTest or acceptance criterion
    Beverage closure shellsFDA 21 CFR 177.1520(c) 3.2a, Regulation (EU) No 10/2011Overall migration <10 mg/dm²; organoleptic panel
    25 L industrial pailsUN 1H2, UN 6.1.5.3Drop test at 23 °C; stacking load on finished pail
    Washer reservoirsISO 179-1/1eA, ISO 175Charpy impact at -30 °C; fluid immersion compatibility
    Frozen food traysFDA 21 CFR 177.1520(c), Regulation (EU) No 10/2011Overall migration <10 mg/dm²; authorised additives only
    Agrochemical overcapsISO 8317, UN 6.1.4Child-resistant torque sequence; closure-bottle seal test
    Nursery potsREACH, ISO 4892-2Restricted heavy metals; 1000 h xenon arc weathering reference
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    Certification & Compliance
    More Introduction

    Iran Petrochemical HDPE I3 is an injection-moulding high-density polyethylene grade identified by the supplier suffix I3. Commercial certificates of analysis for the grade routinely list a melt mass-flow rate of 8.0 g/10 min at 190 °C under 2.16 kg load according to ISO 1133-1, and a solid density of 0.960 g/cm³ according to ISO 1183-1. The combination places the material in the high-fluidity high-density polyethylene class for short-cycle injection moulding. The grade is used in rigid articles in which thin-wall filling, fast release and dimensional repeatability outweigh environmental stress crack resistance and low-temperature impact: stackable crates, pails, household containers, overcaps, paint buckets and industrial packaging components. The comparatively high melt fluidity reduces injection pressure relative to lower-MFR high-density polyethylene, permits lower barrel temperature settings, and allows demoulding at relatively high part temperatures without excessive mould sticking. The resin is not a film grade, not a blow-moulding grade, and not a pressure pipe grade; the selection logic for I3 therefore follows the injection-moulding process window and stiffness-driven end-use requirements.

    What Property Set Distinguishes Iran Petrochemical HDPE I3 in the Injection-Moulding Range?

    Representative datasheet values for HDPE I3 are summarised below. These are commercial lot averages rather than guaranteed specification limits; converters should verify the producer’s current product specification and certificate of analysis before cutting injection tools or locking process windows.

    ParameterTest methodRepresentative value
    DensityISO 1183-10.960 g/cm³
    Melt mass-flow rate, 190 °C/2.16 kgISO 1133-18.0 g/10 min
    Tensile stress at yieldISO 527-2, 50 mm/min26 MPa
    Tensile strain at breakISO 527-2>200%
    Flexural modulusISO 1781100 MPa
    Notched Izod impact, 23 °CISO 180/A3.0 kJ/m²
    Vicat softening point, A50ISO 306127 °C
    Heat deflection temperature, 0.455 MPaISO 75-2/B75 °C
    Shore D hardnessISO 86863
    Mould shrinkage, 2 mm plaqueISO 294-41.8–2.2%
    Water absorption, 24 hISO 62<0.01%
    Melting peak, DSCISO 11357-3130–135 °C
    Environmental stress crack resistance, F50ASTM D1693, Condition B<5 h

    The density of 0.960 g/cm³ corresponds to a crystalline weight fraction near 70–75% when calculated from DSC melting enthalpy using 293 J/g as the reference for fully crystalline polyethylene under ISO 11357-3. The melting peak typically lies between 130 °C and 135 °C, and the glass transition is near −120 °C; the polymer therefore retains segmental mobility well below freezing even though branch-induced crystallinity is high. The 8.0 g/10 min melt mass-flow rate reflects a relatively low average molecular weight and a narrow-to-moderate molecular weight distribution compared with film and blow-moulding grades. This structural combination lowers melt elasticity and die swell, reduces frozen-in orientation, and shortens molecular relaxation time. The same structural features lower environmental stress crack resistance and notched impact at low temperature, which places the grade outside stressed detergent-bottle or frozen-temperature impact applications unless part geometry and service loads are specifically validated.

    Before injection moulding, HDPE I3 does not normally require desiccant drying because the pellet is non-hygroscopic; 24-hour water absorption is reported below 0.01% by ISO 62. If bags are stored in unheated high-relative-humidity warehouses and condensate forms on pellet surfaces, a hopper dryer set to 70 °C for 2 h removes surface moisture and prevents splay. On a general-purpose reciprocating-screw machine with a screw L/D ratio from 20:1 to 24:1, barrel zones are typically profiled 180–220 °C from feed throat to nozzle, with air-shot melt temperature kept below 230 °C to suppress thermo-oxidative yellowing and odour. Holding pressure is set from 60 MPa to 90 MPa depending on flow length, and back pressure is maintained below 1.0 MPa to limit screw-recovery heating. Mould temperatures of 10–40 °C are used for surface reproduction and cooling-time control. The linear polyethylene melt exhibits moderate shear-thinning; apparent viscosity at 190 °C and 100 s⁻¹ typically falls in the range 200–400 Pa·s, while at 1000 s⁻¹ it decreases to 60–150 Pa·s in capillary rheometry on general-purpose high-density polyethylene of this density class. The power-law exponent over the shear-rate range 10²–10³ s⁻¹ is near 0.4–0.5, so pressure drop is less shear-sensitive than in highly branched low-density polyethylene. Gate diameter below 0.8 mm under fast injection can produce jetting, splay or surface flow marks. Mould shrinkage measured on 2 mm plaques according to ISO 294-4 is typically 1.8–2.2%; ribs and bosses that create wall-thickness ratios greater than 1.5:1 generate differential cooling, sink marks and cycle-time extension. Core deflection becomes measurable when unsupported core length exceeds 2.5 times core diameter. Weld lines produced by multi-gate tooling can retain only 40–60% of the parent impact strength in HDPE; gate positions should be moved away from load-bearing ribs and drop-impact corners. In-plant regrind at 20 wt% is used on some lines, but higher regrind levels may increase melt-flow variability, black-speck frequency and notched impact loss.

    When HDPE I3 Replaces Blow-Moulding HDPE or Impact Copolymer Polypropylene in Rigid Packaging

    The substitution case for HDPE I3 appears in injection-moulded caps, overcaps, crates, pails and housewares where polypropylene impact copolymers or lower-MFR HDPE grades have been used. The 8.0 g/10 min melt mass-flow rate is higher than blow-moulding HDPE grades commonly specified at 0.2–0.7 g/10 min and film-grade HDPE near 0.7–1.0 g/10 min. This high fluidity reduces injection pressure and clamp force but also lowers environmental stress crack resistance under constant strain: injection-moulding HDPE grades with a density near 0.960 g/cm³ typically show F50 ESCR values below 5 h in ASTM D1693 Condition B, whereas blow-moulding grades can exceed 100 h. HDPE I3 is therefore not selected for detergent or pressurised bottle service but is used where mould filling, cycle time and part stiffness dominate. Compared with a polypropylene impact copolymer of similar MFR, HDPE I3 has a density of 0.960 g/cm³ and a flexural modulus near 1100 MPa, yielding higher part mass for a given volume and lower upper-service temperature. Notched Izod impact at −20 °C is lower for HDPE I3 than for many impact copolymer polypropylenes; HDPE I3 should not be used in thin-wall containers subjected to frozen-temperature drop impact unless the mould design includes generous radii and controlled gates.

    ParameterHDPE I3Blow-moulding HDPE classFilm-grade HDPE classPP impact copolymer class
    Melt mass-flow rate, 190 °C/2.16 kg8.0 g/10 min0.2–0.7 g/10 min0.7–1.0 g/10 min0.5–8.0 g/10 min
    Density0.960 g/cm³0.945–0.958 g/cm³0.940–0.955 g/cm³0.900–0.910 g/cm³
    Flexural modulus1100 MPa800–1000 MPa700–900 MPa1000–1400 MPa
    ESCR, F50<5 h>100 h>50 hNot applicable
    Typical processing routeInjection mouldingExtrusion blow mouldingBlown film extrusionInjection moulding
    Representative end useCrates, pails, overcapsBottles, containersFilm, linersAutomotive, caps, closures

    Top-load or compression resistance of finished pails and crates should be measured under ASTM D642 or ISO 12048. Because HDPE I3 has a flexural modulus near 1100 MPa, it provides higher wall stiffness per unit thickness than low-density PE, but lower stiffness-to-weight than typical polypropylene grades. Practical top-load capacity depends on sidewall geometry, stacking lugs and cooling rate; the resin alone does not determine pass/fail outcome. Published data for adjacent Iran Petrochemical HDPE grade designations is limited; the comparison above is against broader HDPE and PP classes rather than a single equivalent lot.

    Regulatory Status and Thermal Processing Boundaries

    Regulatory documentation for HDPE I3 should be obtained as a batch-specific statement. Food-contact suitability must be evaluated at the finished-article level under 21 CFR 177.1520 or Commission Regulation (EU) 10/2011 using migration tests such as EN 1186 and EN 13130; base resin conformity does not automatically confer compliance because colourants and processing aids can alter migration behaviour. RoHS directive 2011/65/EU Annex II screening for lead, mercury, cadmium, hexavalent chromium, PBB and PBDE should be performed by ED-XRF or IEC 62321-5 digestion at the homogeneous-material level. REACH SVHC content below 0.1% w/w per article must be confirmed with the supplier’s safety data sheet or product statement. The grade is not UV-stabilised as supplied; outdoor service in sunlight produces surface oxidation and embrittlement, so outdoor use requires carbon black masterbatch at 2.0–2.5 wt% in the final compound at a particle size of 20–50 nm or an equivalent hindered amine stabiliser package. Continuous-use temperature under structural load is normally limited to 60–80 °C; tensile creep in polyethylene rises sharply above 80 °C. Avoid contact with strong oxidising acids, chlorinated solvents, and aromatic hydrocarbons at elevated temperatures, as covered by chemical-resistance data in ISO/TR 10358. Processing waste can be re-pelletised and blended, but degraded material raises melt-flow variability, odour and black-spec frequency; a 20 wt% regrind limit is commonly applied unless the converter validates higher addition on a specific line. Published data for this specific configuration is limited.

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