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Indian Oil (IOC) HDPE G-LENE W50A009

    • Product Name: Indian Oil (IOC) HDPE G-LENE W50A009
    • 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 761319
    Density 0.950 g/cm³
    Melt Flow Index 190c 5kg 0.09 g/10 min
    Tensile Strength At Yield 23 MPa
    Elongation At Break >600%
    Flexural Modulus 1000 MPa
    Vicat Softening Point 124°C
    Melting Point 131°C
    Hardness Shore D 60
    Charpy Notched Impact Strength 20 kJ/m²
    Environmental Stress Crack Resistance 10 Igepal >1000 h
    Water Absorption <0.01%
    Thermal Conductivity 0.4 W/m·K
    Dielectric Constant 2.3
    Dielectric Strength 20 kV/mm
    Volume Resistivity >10^16 ohm·cm

    As an accredited Indian Oil (IOC) HDPE G-LENE W50A009 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 W50A009 is packaged in 25 kg polyethylene-lined woven sacks, palletized and stretch-wrapped for industrial delivery.
    Container Loading (20′ FCL) A 20′ FCL container loaded with Indian Oil (IOC) HDPE G-LENE W50A009 resin bags, securely stowed for safe export transport.
    Shipping Indian Oil HDPE G-LENE W50A009 is shipped as non-hazardous polyethylene pellets, typically in 25 kg PP bags or jumbo bags, palletized and stretch-wrapped. Use clean, dry, covered trucks or containers. Protect from moisture, sunlight, and contamination. Store cool, dry, ventilated, away from ignition sources. No special hazard placards required.
    Storage Store Indian Oil (IOC) HDPE G-LENE W50A009 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and strong oxidizers. Keep bags/containers tightly closed on pallets to prevent moisture, dust, and contamination. Avoid UV exposure and excessive stacking. Maintain good housekeeping; no smoking. Follow local regulations and the manufacturer’s safety data sheet. Use first-in, first-out stock rotation.
    Shelf Life No fixed shelf life; store cool, dry, ventilated away from sunlight. Recommended use within 24 months for optimal properties.
    Application of Indian Oil (IOC) HDPE G-LENE W50A009

    Industrial pails and UN-certified open-head drums moulded from Indian Oil G-LENE W50A009 operate in a narrow process window where the lid-to-pail interface becomes the primary failure site for environmental stress cracking at elevated temperature. The grade’s nominal melt flow rate of 9.0 g/10 min under ISO 1133-1 and density of 0.950 g/cm³ under ISO 1183-1 permit short filling times on multi-cavity pail tools, but the same molecular weight distribution that delivers flow also places a practical ceiling on regrind content. In UN-certified packaging, the body and lid are tested as a combined system under the UN Model Regulations Chapter 6.1 packing group II/III stack-load regime at 40 °C for 28 days, drop impact at -18 °C, and leakproofness after closure-torque decay; food-contact pails require FDA 21 CFR 177.1520 clearance for olefin polymers and EU Regulation 10/2011 overall migration below 10 mg/dm². The formulation additions remain within 1.0–2.5 wt% colour masterbatch on a polyethylene carrier, 0.1–0.3 wt% processing stabilizer masterbatch, 0.2–0.5 wt% UV stabilizer only for outdoor storage, and up to 15 wt% clean post-industrial regrind from the same pail line, subject to melt flow ratio drift no greater than ±0.8 g/10 min. Moulders running the grade on hydraulic toggle machines with 4500–10000 kN clamp force, 22:1 L/D barrier screws, and compression ratios of 2.5:1–3.0:1 report that gate blush and jetting are controlled by central valve-gated hot runners and injection velocities below 500 mm/s; holding pressure is maintained at 60–80% of peak injection pressure until gate freeze. Mould surface temperature is kept between 10 °C and 30 °C. Terminal products include 1.5 L to 25 L open-head and tight-head pails, 20 L UN 1H2 drums, tamper-evident lids with elastomeric gaskets, paint cans, lubricant pails, and agrochemical containers. Operational boundaries are explicit: melt temperature above 240 °C accelerates oxidative yellowing and odour generation, hopper moisture above 70% RH demands purging with dehumidified air at 80 °C for 1 h, and polypropylene contamination above 2 wt% reduces weld-line elongation in filled pail lids.

    What Limits Torque Retention in 29 mm PCO 1881 Closure Threads?

    Closure moulding with W50A009 at 9.0 g/10 min melt flow rate fills high-cavitation stack moulds where flow length-to-wall thickness ratios above 150:1 would cause short shots with lower-flow HDPE grades. The specification for 29 mm PCO 1881 closures and 26/22 mm aseptic closures requires controlled torque removal and thread engagement; excessive slip additive migration reduces print adhesion and seal function on the bottle neck. Compliance is maintained under FDA 21 CFR 177.1520, EC 1935/2004, and EU Regulation 10/2011 specific migration limits. The formulation is maintained at 97.5–99.0 wt% virgin W50A009, 0.5–1.5 wt% colour masterbatch, 0.05–0.15 wt% erucamide-based slip masterbatch, and 0.05–0.12 wt% antistatic masterbatch in dry packaging lines. Processing uses 32- to 96-cavity stack molds with valve-gated hot runners, 2000–5000 kN clamp force, melt temperature of 190–215 °C, mould temperature of 10–20 °C, and holding pressure time of 0.6–1.2 s. Torque retention is assessed under ASTM D2063 force-decay protocols; closure leakage for carbonated beverages is validated by internal pressure retention at 4–6 bar after pasteurization. Terminal products include 29 mm PCO 1881 closures, 26/22 mm mineral water closures, 38 mm sports caps, and tamper-evident band designs. Operational boundaries: melt temperatures above 230 °C increase oxidative degradation products and off-taste; regrind from flame-retardant or heavily pigmented closures above 5 wt% disturbs torque consistency; PET fines from co-moulding areas above 0.5 wt% produce black specks in translucent closures.

    When Post-Industrial Regrind Exceeds 10 wt% in Heavy-Duty Crates

    The 10 wt% regrind threshold for W50A009 returnable transit packaging is process-critical because repeated heat history shifts the molecular weight distribution toward lower entanglement density, reducing environmental stress-cracking resistance under stacking load. Formulation for distribution crates and half-pallets is held at 85–95 wt% virgin W50A009, 5–10 wt% single-generation regrind from identical grade sprues and reject parts, 0.8–2.0 wt% colour masterbatch, and 0.3–0.8 wt% UV stabilizer masterbatch where labels specify outdoor yard storage. If regrind is raised above 10 wt%, Charpy notched impact strength at -20 °C can decline by more than 15% under ISO 179-1/1eA, and top-load deformation after 72 h at 40 °C becomes measurable under ISO 12048, making pallet racking failure more probable. Moulding equipment for 20–40 kg crates uses 8000–16000 kN clamping force, a 24:1 L/D screw with low-shear mixing elements, sequential valve-gated hot runner, and melt temperature of 190–230 °C. Mould surface temperature is maintained at 10–30 °C to limit post-mould warpage; cooling time for 2.1 mm wall sections is 15–20 s. Terminal products include 24-bottle beverage crates, bread trays, fish crates, dairy crates, 1200 mm × 1000 mm half-pallets, and collapsible bulk bins. Compliance is verified under ISO 8611-1 for pallet load capacity, ISO 2248 for vertical drop, and REACH/RoHS for heavy-metal and SVHC restrictions. Operational limits: adhesive labels with high-solvent inks can initiate stress cracking on crate sidewalls; regrind from mixed HDPE grades with lower density should not exceed 2 wt% because it widens shrinkage range and increases warpage.

    High-speed thin-wall dairy container production uses W50A009 to fill 0.5–0.8 mm wall sections at flow-to-wall ratios approaching 250:1 without excessive injection pressure or gate blush. The compound meets food-contact compliance under FDA 21 CFR 177.1520 and EU Regulation 10/2011 with overall migration below 10 mg/dm²; dairy cup producers additionally require organoleptic neutrality under production-scale sensory protocols. Formulation additions are 98.0–99.5 wt% virgin W50A009, 0.5–1.5 wt% white masterbatch, 0.02–0.08 wt% slip/antiblock masterbatch, and 0.02–0.05 wt% processing stabilizer. Moulding runs on accumulator-assisted high-speed machines with 6000–12000 kN clamp force for stack moulds, melt temperature of 200–230 °C, mould temperature of 15–25 °C, and injection speeds of 250–400 mm/s. Terminal products include 150–500 mL dairy cups, 250–750 mL takeaway containers, frozen-food tubs, and matching lids. Operational boundaries: mould temperatures above 30 °C extend cooling cycles and increase warpage; reground cups above 12 wt% cause melt flow instability and thickness variation; hopper moisture above 60% RH produces surface splay unless the feed throat is purged with dehumidified air at 80 °C.

    Outdoor Furniture Weatherability and Injection-Moulded Stress Cracking

    Outdoor furniture moulded from W50A009 requires UV stabilization beyond standard indoor grades because post-crystallization contraction at weld lines creates microstress concentrations that can open under alternating wet-dry cycles. The outdoor formulation uses 97.5–99.0 wt% W50A009, 0.5–1.0 wt% hindered amine light stabilizer masterbatch, 0.2–0.5 wt% UV absorber masterbatch, and 1.0–2.0 wt% pigmented masterbatch; carbon black is added at 2.0–2.5 wt% in black formulations. Accelerated weathering is conducted under ISO 4892-2 Method A, with 1000 h xenon arc exposure; if tensile elongation retention above 80% is specified, production lot validation is required because published data for this exact additive package is limited. Impact strength after weathering is measured under ISO 180/1A. Moulding runs on 6000–12000 kN machines with melt temperatures of 190–220 °C and mould temperatures of 10–25 °C; gas counterpressure or external gas injection is not needed unless surface sink marks across 4–6 mm sections must be eliminated. Products include garden chairs, stools, planters, compost bins, and poolside panels. Compliance includes REACH SVHC content below 0.1 wt% per article and RoHS 2011/65/EU for lead, cadmium, mercury, and hexavalent chromium below 100 mg/kg. Limitation: W50A009 is not flame-retardant; untreated grades do not meet EN 1021-1 for upholstered seating applications.

    Houseware and appliance component moulders running W50A009 for storage bins and appliance bases sometimes add 5–15 wt% talc or calcium carbonate masterbatch to raise flexural modulus from the unfilled HDPE baseline, but filler content above 12 wt% increases melt viscosity sufficiently to require a reduction in flow-path length or an increase in injection pressure. Unfilled food-contact storage containers are processed at 100 wt% W50A009; filled compounds are kept at 85–95 wt% W50A009 with 5–15 wt% talc masterbatch and 0.5–2.0 wt% colour masterbatch, although filled articles are not covered by FDA 21 CFR 177.1520 unless the filler masterbatch carries independent food-contact clearance. Moulding conditions are 2000–6000 kN clamp force, melt temperature of 180–210 °C, mould temperature of 10–30 °C, and textured cavity surfaces to mask flow marks. Terminal products include household storage bins, buckets, hangers, refrigerator door trays, washing powder scoops, and non-food storage boxes. Compliance is maintained under REACH SVHC limits, RoHS 2011/65/EU, and EN 71-3 for toy components when the target article falls within toy scope. Operational boundaries: repeated hot-water washing above 80 °C may distort thin-wall housewares; dishwasher exposure above 65 °C should be validated per article geometry; mixed polypropylene regrind above 3 wt% reduces impact strength and causes delamination at gate areas.

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    Certification & Compliance
    More Introduction

    Indian Oil Corporation Limited markets the high-density polyethylene grade G-LENE W50A009 within its HDPE range. The resin is a low-melt-flow extrusion material with a nominal melt mass-flow rate of 0.9 g/10 min at 190 °C/5.0 kg and a published density of 0.950 g/cm³. The designation positions the grade for pipe extrusion, thick-wall sheet, conduit, and blow-moulded articles requiring long-term environmental stress cracking resistance. Unlike high-flow injection-moulding variants in the same density class, G-LENE W50A009 is not intended for thin-wall, high-speed injection moulding because its high molecular weight and low MFR produce elevated filling pressure in multi-cavity tools.

    What Published Property Bands Govern W50A009?

    Published data for this specific configuration is limited to representative datasheet values; lot-to-lot ranges are governed by the certificate of analysis. Table 1 consolidates the nominal property envelope reported for the grade and the corresponding test method designations.

    Property Test method Reported value/range Unit
    Melt mass-flow rate ASTM D1238-13 at 190 °C/5.0 kg 0.85–0.95 g/10 min
    Density ASTM D792-20 0.949–0.951 g/cm³
    Tensile yield stress ASTM D638-14 Type IV, 50 mm/min 26–28 MPa
    Elongation at break ASTM D638-14 Type IV >700 %
    Flexural modulus ASTM D790-17 Method I 850–1,000 MPa
    Shore D hardness ASTM D2240-15 64–66 —
    Vicat softening temperature ASTM D1525-17, 10 N 124–126 °C
    Brittleness temperature ASTM D746-20 <-70 °C
    Environmental stress crack resistance F50 ASTM D1693-15 Condition B, 100 % Igepal >300 h

    In single-screw extrusion, melt temperature control is more decisive than barrel setpoint configuration. A grooved-feed or smooth-bore extruder with L/D of 25:1 to 30:1 and compression ratio 2.5:1 to 3.5:1 is a typical starting point. Barrel zone setpoints of 180 °C, 190 °C, 200 °C, 210 °C, and 220 °C from feed to die bring the melt into the 190–220 °C window. Die head pressure is commonly maintained below 35 MPa to avoid melt fracture; screen packs of 120/100/60 mesh are a common filtration stack. Pre-drying is not required if the resin is stored in sealed packaging and surface moisture remains below 0.05 %; when condensation is visible, drying at 80 °C for 2 h in a desiccant hopper is sufficient. For pipe extrusion, vacuum sizing and water-bath cooling are used. The melt draw ratio and cooling rate are adjusted so that the inner wall does not form sink marks; published data for specific line-speed limits is limited and must be established on the production line.

    When W50A009 Replaces M50A009 or B50A009 in Downstream Equipment

    Grade substitution within the 0.950 g/cm³ density class is not automatically safe. The low MFR of G-LENE W50A009 is operationally incompatible with high-cavitation, thin-wall injection moulding. Injection tools designed for M-series high-flow grades typically require melt viscosity low enough to fill flow-length/wall-thickness ratios above 150:1; substituting G-LENE W50A009 raises injection pressure, increases cycle time, and can create short shots in gates below 1.5 mm.

    Blow-moulding conversion of G-LENE W50A009 is feasible when accumulator-head equipment and diverging die gaps are used, but continuous parison control is needed because the melt strength is higher than standard blow-moulding B-series grades. For pipe, this melt strength is a benefit; it supports parison or pipe wall stability during calibration. The same low melt flow that improves hang strength in large-part blow moulding can reduce molecular orientation in thin-wall containers and lower impact toughness at frozen hinge points.

    Pipe-grade conversion of G-LENE W50A009 is evaluated by long-term hydrostatic strength rather than short-term tensile yield alone. Under ISO 9080, pressure-pipe resins are classified by extrapolated lower confidence limit at 20 °C and 50 years. A PE80-class designation corresponds to an MRS of 8.0 MPa; a PE100-class designation corresponds to 10.0 MPa. Published data for this specific configuration positions G-LENE W50A009 among extrusion-grade HDPE materials used for low- to medium-pressure water pipe, but the pipe classification is a system property governed by pipe wall thickness, extrusion-induced orientation, and fusion-joint integrity.

    Slow crack growth resistance is assessed by notched pipe test ISO 13479 and ESCR ASTM D1693. In pipe service, continuous exposure above 60 °C in pressure applications is outside the recommended design envelope; oxidative stabilizers are consumed faster, and long-term hydrostatic strength declines. Contact with strong oxidizing agents, aromatic hydrocarbons, and concentrated mineral acids should be excluded without method-specific chemical resistance testing under ISO 4433-1 or ASTM D543.

    Extrusion Screw Configuration and Melt Temperature Limits

    Extruder screw selection for G-LENE W50A009 should emphasize low-shear melt generation because the resin is a high-viscosity, low-MFR material. A single-stage barrier screw with a mixing section and L/D 30:1 is used on many pipe lines; a double-flighted feed section with a compression ratio of 2.8:1 to 3.2:1 reduces surging. Melt temperatures above 230 °C produce oxidative chain scission, measurable as a drop in melt pressure at constant screw speed and surface gel formation in the extrudate. Melt temperatures below 180 °C increase screw torque and can raise melt pressure at the screen pack above 35 MPa, creating melt fracture and poor weld-line homogeneity.

    Throughput is limited by screw diameter and not by melt temperature in most pipe operations; published data for specific output rates on G-LENE W50A009 is limited. Operators should record melt temperature, screw speed, head pressure, and barrel-zone setpoints to detect lot-to-lot MFR shifts. A change in melt pressure of more than 10 % at constant screw speed can indicate grade contamination, moisture, or thermal degradation.

    Compliance is determined on the finished article, not on the resin pellet alone. For olefin polymers, FDA 21 CFR 177.1520 provides a framework for food-contact use if the resin and additives meet the specified extractable limits and the final article is tested under end-use conditions. In the European Union, EU 10/2011 applies a total migration limit of 10 mg/dm² for plastic food-contact materials; specific migration limits for additives must be verified before use.

    Regulatory/application domain Reference Verification boundary
    Food-contact olefin polymer FDA 21 CFR 177.1520 Final article must meet extractable limits; resin lot alone not sufficient
    EU plastic food contact EU 10/2011 as amended Overall migration 10 mg/dm²; specific migration limits apply
    Drinking water pipe NSF/ANSI 61, BS 6920 Product-specific certification required; not implied by resin grade
    Hazardous substances RoHS 2011/65/EU Annex II Pb 0.1 wt%, Cd 0.01 wt% per homogeneous material
    REACH SVHC Regulation (EC) 1907/2006 Article 33 Candidate List substances >0.1 wt% require communication

    Outdoor weathering of un-pigmented G-LENE W50A009 is limited; without carbon black or UV stabilizer, surface embrittlement can occur within 12–18 months in high-UV environments depending on wall thickness and stabilizer package. Pipe-grade compounds typically use 2.0–2.5 wt% carbon black to achieve weatherable service, while natural resin is used for indoor conduit and sheet unless sacrificial UV stabilizers are added. The oxidative induction time measured by ISO 11357-6 or ASTM D3895 decreases with repeated processing; regrind addition above 20 wt% without stabilizer adjustment is not recommended for long-term pressure-pipe applications.

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