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Indian Oil (IOC) HDPE G-LENE 158A180

    • Product Name: Indian Oil (IOC) HDPE G-LENE 158A180
    • 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 572017
    Polymer Type High Density Polyethylene (HDPE)
    Density 0.958 g/cm3
    Melt Flow Index 190 C 2 16 Kg 18 g/10 min
    Tensile Strength At Yield 30 MPa
    Elongation At Break >1000%
    Flexural Modulus 1300 MPa
    Izod Impact Strength Notched 23 C 40 J/m
    Vicat Softening Point 127°C
    Heat Deflection Temperature 0 45 Mpa 80°C
    Shore D Hardness 66
    Melting Point 135°C
    Water Absorption <0.01%
    Bulk Density 0.58 g/cm3
    Crystallinity 70-80%
    Thermal Expansion Coefficient 1.2 x 10^-4 /°C

    As an accredited Indian Oil (IOC) HDPE G-LENE 158A180 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Indian Oil (IOC) HDPE G-LENE 158A180 is supplied in 25 kg moisture-resistant woven polypropylene bags, palletized for industrial handling.
    Container Loading (20′ FCL) 20′ FCL container loading for Indian Oil (IOC) HDPE G-LENE 158A180: 25 kg bags, palletized, shrink-wrapped, and secured for export.
    Shipping Typically non-hazardous HDPE pellets (Indian Oil G-LENE 158A180), shipped in 25 kg PP bags, palletized and stretch-wrapped. Transport in clean, dry, covered trucks or containers, away from moisture, heat, sunlight, and contamination. Not regulated as dangerous goods; standard shipping documentation applies.
    Storage Store Indian Oil (IOC) HDPE G-LENE 158A180 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, sparks, and flames. Keep bags/containers closed, palletized off the floor, and protected from moisture, dust, oils, and other contaminants. Avoid prolonged UV exposure. Maintain good ventilation and normal ambient temperatures; stack safely to prevent bag rupture. Use first-in, first-out stock rotation. Follow manufacturer SDS and local regulations.
    Shelf Life Recommended shelf life is 12 months when stored in original sealed packaging, in a cool, dry, ventilated area away from direct sunlight.
    Application of Indian Oil (IOC) HDPE G-LENE 158A180

    Indian Oil (IOC) HDPE G-LENE 158A180 is an injection-moulding grade with a nominal melt flow rate of 18 g/10 min at 190 °C under 2.16 kg load when measured to ASTM D1238, and a nominal density of 0.958 g/cm³ when tested to ASTM D792. For thin-wall dairy spread tubs with wall sections between 0.45 mm and 0.75 mm, the primary process conflict is balancing the high melt velocity needed for filling against differential shrinkage that drives ovality in stackable lids. The filling stage runs at melt temperatures between 215 °C and 230 °C, with a mould temperature of 10 °C to 18 °C. Injection velocities are set between 120 mm/s and 180 mm/s, yielding fill times of 0.25 s to 0.45 s for part weights from 8 g to 18 g. A hot-runner system with 4 to 8 valve-gated drops is used; gate drop diameters are held between 0.8 mm and 1.2 mm to limit gate shear heating. Holding pressure is applied from 30 MPa to 50 MPa for 1 s to 2 s, and the melt cushion is maintained at 2 mm to 4 mm. If ambient relative humidity is above 60% during warehouse storage, surface moisture should be removed by drying at 70 °C for 2 h; otherwise, splay may appear as striations on the sealing ledge. Wall-thickness transitions are limited to 25% of nominal wall, and rib roots are designed at 0.5 to 0.6 of the nominal wall to prevent sink marks on the sealing surface. A general-purpose polyolefin screw with a compression ratio of 1.8:1 to 2.2:1 and an L/D ratio of 20:1 to 25:1 is preferred. The grade is suitable for cold-fill and ambient food packaging but not for hot-fill above 90 °C continuous service because distortion risk increases above the heat deflection region. Compliance is assessed under FDA 21 CFR 177.1520(c) 3.1a and 3.2a for food-contact olefin polymers, and under EU 10/2011 the applicable overall migration limit is 10 mg/dm². Terminal parts include margarine tubs, frozen dessert cups, portion containers, and stackable overcap lids.

    What Limits Gate Vestige Height in HDPE Closure Moulding?

    The sealing plane in tamper-evident HDPE closures is the functional datum, not the top of the shell. For a 28 mm two-piece closure moulded in a 48-cavity tool, a sub-gate diameter between 0.6 mm and 0.9 mm is used, but the resulting gate vestige must be kept below 0.25 mm above the sealing plane to prevent the gasket liner from bridging the gate scar. Total indicated runout across the sealing plane is specified at 0.15 mm maximum, because a larger deviation reduces the effective torque window on a PET PCO 1881 finish. The melt temperature is maintained between 210 °C and 225 °C, and the mould is run at 8 °C to 15 °C to solidify the gate rapidly. Fill time for a 2.5 g to 5 g closure is controlled between 0.15 s and 0.30 s. Application torque is set at 1.8 N·m to 2.2 N·m; removal torque after 24 h is expected between 0.8 N·m and 1.6 N·m on cold-filled still water bottles. The grade should not be specified for retort or pasteurisation above 60 °C under closure load, because torque retention drops when the closure is reheated in the packed condition. Environmental stress-cracking resistance is assessed to ASTM D1693 under condition B; published data for this specific closure configuration is limited, so incoming quality control should verify F50 on moulded plaques against an agreed internal control. Compliance follows FDA 21 CFR 177.1520 for food-contact closures and EU 10/2011 for specific migration testing in the final pack. Terminal products include still water closures, edible oil closures, personal care flip-top caps, and detergent measuring closures.

    Crate Rib Geometry and Post-Mould Shrinkage Compensation

    Mono-material HDPE crates produced from G-LENE 158A180 are typically specified for a five-high stack at 40 °C with individual crate loads from 250 kg to 350 kg. The functional risk is not total collapse but sidewall bowing at the third-high position because moulded-in orientation causes anisotropic post-mould shrinkage. Along-flow shrinkage ranges from 1.6% to 2.4%, while transverse shrinkage ranges from 1.8% to 2.6%; this differential must be compensated in the tool split by a short-side-long-side scale correction. Sidewall ribs are dimensioned with a rib root thickness of 0.55 to 0.65 times the nominal wall, and rib height is limited to 2.5 times the wall to avoid sink streaks on the logo panel. Draft angle is at least 0.5° per side on all vertical faces. The moulding window uses a melt temperature of 220 °C to 245 °C, a mould temperature of 15 °C to 25 °C, and injection pressure from 80 MPa to 120 MPa. For a crate weighing 800 g to 1.8 kg with a wall thickness of 2.5 mm to 4.0 mm, fill time is 1 s to 3 s, and cooling time is 20 s to 35 s. Stacking lugs are cored from the rear to prevent wall-thickness concentrations above 50% of adjacent wall. If the crate is intended for outdoor agricultural use, 2% carbon black masterbatch or an equivalent UV stabilizer package is required; the neat resin does not provide long-term UV resistance. Packaging compliance is evaluated under EU 94/62/EC and the destination market packaging regulation. Terminal products include dairy crates, bread trays, fish crates, and ventilated produce totes.

    Regulatory checkpoint matrix for G-LENE 158A180 downstream applications
    ApplicationRegulationClause or test methodControl limit
    Food-contact containers and closuresFDA 21 CFR 177.1520(c)3.1a / 3.2aOlefin polymer identity
    Food-contact migrationEU 10/2011Overall migration≤10 mg/dm²
    Toy accessible substrateUS CPSIALead content≤90 ppm
    Toy heavy-metal migrationEN 71-319 elementsSpecific migration limits
    Household storage chemical restrictionsREACH Annex XVIIRestricted substancesCadmium, lead, phthalates

    Because consumer storage drawer frames require a parting-line flatness below 0.3 mm over a 350 mm span, the hold-pressure profile must be trimmed to the minimum required to pack the gate region without overpacking the distal ends. The grade is processed at a melt temperature of 200 °C to 220 °C and a mould temperature of 15 °C to 25 °C. For a drawer frame with a projected area of 0.12 m² to 0.18 m², clamp force is calculated at 0.45 to 0.60 tonnes/cm², and injection pressure falls between 60 MPa and 100 MPa. Holding pressure is run from 40 MPa to 60 MPa for 4 s to 8 s. Bosses are cored to reduce sink depth on the visible face, and ribs are designed at 0.5 to 0.6 of the nominal wall. Part mass ranges from 400 g to 900 g, and wall thickness ranges from 2.0 mm to 3.0 mm. The moulded drawer should be held in a cooling fixture for 10 s to 15 s after ejection if flatness is critical; free-floor cooling can increase central bow by 0.1 mm to 0.2 mm. Compliance for household storage products falls under REACH Annex XVII heavy-metal restrictions and, where food contact is intended, EU 10/2011. Terminal products include stackable storage totes, modular drawer units, under-bed boxes, and wardrobe organisers.

    When G-LENE 158A180 Replaces Medium-Flow HDPE in Pail Lid Tear Strips

    Tear-strip pail lids present a split process demand: the central panel must be rigid enough to resist doming under stack load, while the tear strip must propagate cleanly without fibre bridging. The hinge is moulded at 0.4 mm to 0.6 mm thickness, and the notch depth is set between 0.2 mm and 0.3 mm. A fan gate at the rim with a land thickness of 2.0 mm to 3.0 mm is preferred over a tunnel gate because the lower gate shear protects the hinge from molecular orientation that would cause splitting before the notch is opened. The observed tear force for a 200 mm diameter pail lid is typically 30 N to 80 N when the tear strip is pulled at 90°; however, published data for this specific grade in tear-strip geometry is limited, so incoming tool trials should verify force-loss after 24 h of crush loading. Flatness across the lid flange is held below 0.5 mm over 200 mm, and melt temperature is controlled from 210 °C to 230 °C. The processing window is tight; a melt temperature above 230 °C reduces tear-strip ductility, while a melt temperature below 210 °C can freeze the fan gate early. Mould temperature is set at 15 °C to 25 °C, with fill time from 0.8 s to 1.5 s. Holding pressure runs from 35 MPa to 50 MPa. The material alone does not provide a resilient seal; a separate EPDM or EVA gasket is required for liquid-tight pails. When the complete pail is certified for dangerous goods, the lid must be tested with the body under UN 6.1 or UN 6.5 packaging group conditions. Terminal products include lids for 5 L to 25 L paint pails, lubricant pails, and adhesive pails.

    For toy building blocks, which compliance thresholds govern the injection moulding window?

    A low-stress injection moulding window for toy building blocks is established not by tensile strength alone but by the combined constraint of migration limits and sharp-edge safety. The grade is moulded at 190 °C to 210 °C to reduce oxidative degradation, with a mould temperature of 10 °C to 20 °C. Gate vestige is kept below 0.3 mm because a taller raised gate can fail the sharp-edge check under EN 71-1. For building blocks with a wall thickness of 1.5 mm to 2.5 mm, a sub-gate or a valve gate should be positioned in a recessed area, not on the clutch face where dimensional interference controls stack retention. The material is evaluated against the heavy-metal migration thresholds of EN 71-3 for the 19 listed elements, and the US market requires lead below 90 ppm in accessible substrates under CPSIA. Residual stress is relevant because toy components may contact mineral oil, soap, or food simulants during use; excessive packing pressure increases ESCR sensitivity. Holding pressure is limited to 30 MPa to 45 MPa, and cooling time is set to 10 s to 18 s. Terminal products include building blocks, toy storage bins, play panels, and ride-on toy structural parts.

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    Certification & Compliance
    More Introduction
    Indian Oil (IOC) HDPE G-LENE 158A180 is a high-molecular-weight high-density polyethylene extrusion blow moulding grade. The grade designation places it in the G-LENE HDPE matrix: the 158 series is associated with a nominal density of 0.958 g/cm3 measured under ISO 1183-1:2019, and the A180 suffix corresponds to a melt flow index of 0.18 g/10 min determined under ISO 1133-1:2022 at 190 °C with a 2.16 kg load. The combination of low melt flow index and density above the conventional 0.950 g/cm3 HMW-HDPE range indicates high average molecular weight, elevated melt strength, controlled parison sag, and higher hoop stiffness in finished parts. The product is supplied in pellet form with a stabilizer and processing-lubricant package intended for accumulator-head and continuous extrusion blow moulding of large rigid containers, industrial drums, jerry cans, and packaging for dangerous goods.

    What distinguishes 158A180 from conventional blow moulding grades?

    The primary distinction is molecular weight and density. Conventional blow moulding HDPE grades often combine melt flow index values from 0.30 g/10 min to 0.70 g/10 min with densities near 0.945 g/cm3 to 0.952 g/cm3; those materials process at lower head pressure and exhibit shorter parison hang times, but they develop less melt strength. In contrast, 158A180 has a melt flow index of 0.18 g/10 min, which indicates a higher weight-average molecular weight and longer relaxation time. This characteristic produces higher die swell, lower sag under its own weight, and improved thickness uniformity in long parisons. Relative to injection moulding HDPE grades in the G-LENE family with melt flow index values above 8 g/10 min, 158A180 requires higher melt temperature and pressure, and its high elongational viscosity prevents adequate cavity filling in thin sections below approximately 1.5 mm. Published data for this specific configuration is limited; processors should obtain lot-specific flow curves because comonomer distribution and molecular-weight distribution can shift die swell and melt strength across production campaigns. On accumulator-head machines used for 200–220 l tight-head drums, production behaviour of HMW-HDPE grades with melt flow index around 0.18 g/10 min is controlled by parison length, die gap, and accumulator push-out speed. Melt temperature at the accumulator is commonly held between 190 °C and 220 °C, while barrel zones may run from 180 °C to 210 °C. Because 158A180 is formulated for high melt strength, the parison can be run longer without sag-induced thinning, but excessive accumulator residence time beyond 10 min can initiate shear-history-dependent viscosity loss. Extruders with 24:1 to 30:1 L/D and barrier screws provide sufficient plastication; screw compression ratios from 2.2:1 to 2.8:1 are typical for this viscosity class. Die swell values observed on continuous blow moulders for similar HMW-HDPE grades are frequently in the 30–50 % range; tooling must accommodate this swell to prevent wall-thickness control errors. Blow pressure at the blow pin is typically controlled at 0.6–0.8 MPa for large-area drums, while mould clamping pressure remains machine-specific. These ranges are indicative industrial practice, not a substitute for trial validation on the specific accumulator-head, shuttle, or wheel machine.

    Benchmark values are not specification limits

    Specification values are released by Indian Oil in lot certificates and should be used in preference to generic technical data. The following table summarises typical producer-reported values for G-LENE 158A180 from published grade documentation; each value is accompanied by the test standard used.
    PropertyTest methodTypical valueUnit
    Melt flow index at 190 °C, 2.16 kgISO 1133-1:20220.18g/10 min
    DensityISO 1183-1:20190.958g/cm3
    Tensile yield stressISO 527-2:201228MPa
    Elongation at breakISO 527-2:2012>600%
    Flexural modulusISO 178:20191000MPa
    Charpy notched impact at 23 °CISO 179-1:20105kJ/m2
    Vicat softening point A50ISO 306:2022126°C
    Shore D hardnessISO 868:200364—
    Environmental stress-crack resistance, 10% IgepalASTM D1693-15>1000h
    The values in the table are not intended as minimum or maximum specification limits. Incoming quality control should test melt flow index, density, and colour consistency on every lot, while mechanical properties such as Charpy impact and environmental stress-crack resistance are appropriate for annual type-testing or when a new silo, railcar, or packaging configuration is introduced. Lot-to-lot variation in HMW-HDPE grades is influenced by catalyst residuals, comonomer distribution, and post-reactor pellet conditioning. If the grade is stored in humid coastal warehouses at RH above 60 % or in open silos, surface condensation can cause splay in blow moulded parts. Predrying at 70–80 °C for 2–4 h is recommended only for material exposed to moisture; sealed original packaging does not normally require predrying.

    When 158A180 replaces 0.950-density HMW-HDPE in industrial drum liners

    Replacement of a lower-density HMW-HDPE with 158A180 changes the property envelope rather than simply improving it. At equivalent wall thickness, density increase from 0.950 g/cm3 to 0.958 g/cm3 raises flexural modulus and top-load capacity, but it lowers conventional environmental stress-crack resistance and impact toughness. Published data for this specific configuration is limited for some surfactant-laden fill goods; therefore qualification must follow ASTM D1693-15 ESCR testing in the actual chemical medium or a validated surrogate, rather than relying only on density and melt flow index. In 210 l open-head drums for solvent-free aqueous emulsions, the higher stiffness of 158A180 can support stacking height in warm warehouses where lower-density HMW-HDPE may creep. In contrast, for aggressive detergent or ethoxylate-containing formulations, lower-density HMW-HDPE grades may provide longer service life because of higher stress-crack resistance. The selection is therefore application-dependent: 158A180 is preferable when hoop stiffness, hydrocarbon barrier, and top-load strength dominate, while lower-density HMW-HDPE is preferable when ESCR and cold-temperature impact govern. In packaging for UN-certified dangerous goods, the grade is processed into inner liners for fibreboard drums and into all-plastic jerry cans subject to hydrostatic pressure testing under the applicable transport regulations. The higher density contributes to lower permeation of hydrocarbon-based fill goods than HDPE grades of 0.945 g/cm3 density, although permeation remains finite. Stacking tests at 40 °C for 28 days are commonly used for drum qualification; density and creep modulus are relevant but not sufficient to predict UN certification. Weld-line integrity at the pinch-off and handle areas must be verified because high-molecular-weight grades can show slower interdiffusion across weld lines when processing temperatures are low. For 158A180, lower melt temperatures near 190 °C reduce parison sag but may restrict molecular diffusion at the pinch-off; processors therefore raise pinch-off zone temperature or increase pinch pressure to avoid weld-line cracking.

    Which regulatory boundaries apply to unfilled HDPE food-contact articles?

    Indian Oil supplies G-LENE 158A180 with documentation reflecting compliance for olefin polymers under FDA 21 CFR 177.1520(c) when used in food-contact articles, subject to the article’s intended temperature and food-type conditions. For the European Union, compliance is typically assessed against Regulation (EU) No 10/2011 with overall migration limits of 10 mg/dm2 for food-contact plastics; end-use testing remains the responsibility of the article manufacturer. REACH registration obligations apply to the substance in Europe, and RoHS restrictions are not generally triggered for unfilled HDPE packaging. The grade should not be combined with amine-based or peroxide-generating additives unless specifically validated, because such additions can alter thermomechanical stability and colour. Recycled content streams or post-consumer recyclate should not be blended without compatibility and sensory testing for food or high-purity chemical packaging.

    Operational window constraints in high-shear accumulation blow moulding

    The operational window is bounded by shear heating, parison sag, and weld-line strength. If melt temperature exceeds 230 °C, prolonged residence time can shift melt flow index upward and reduce melt strength; if melt temperature remains below 180 °C, plastication becomes inconsistent and die-head pressure rises beyond typical machine capability. Injection of this grade into thin-wall moulds below 1.5 mm is impractical because high viscosity and long relaxation times produce weld-line weakness and excessive clamp consumption. For continuous extrusion blow moulding of bottles below 500 ml, 158A180 is generally over-engineered; lower-viscosity blow moulding grades with melt flow index 0.50–0.70 g/10 min deliver faster cycle times. Published data for this specific configuration is limited in the public domain, so these boundaries should be confirmed with trial runs on the actual accumulator-head, shuttle, or wheel machine.
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