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Reliance Industries HDPE HD5301AA

    • Product Name: Reliance Industries HDPE HD5301AA
    • 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 225590
    Polymer Type High Density Polyethylene
    Density 0.954 g/cm³
    Melt Flow Index 0.35 g/10 min at 190°C/2.16 kg
    Tensile Strength At Yield 26 MPa
    Elongation At Break 800 %
    Flexural Modulus 1200 MPa
    Vicat Softening Temperature 124 °C
    Melting Temperature 131 °C
    Environmental Stress Crack Resistance >1000 h
    Shore D Hardness 65
    Water Absorption <0.01 %
    Dielectric Constant 2.3
    Volume Resistivity >1e16 ohm·cm
    Thermal Conductivity 0.45 W/m·K

    As an accredited Reliance Industries HDPE HD5301AA factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Reliance Industries HDPE HD5301AA is typically supplied in 25 kg polyethylene bags, palletized, stretch-wrapped, and labeled for industrial transport.
    Container Loading (20′ FCL) 20′ FCL container loaded with Reliance Industries HDPE HD5301AA in 25kg bags, palletized, shrink-wrapped, securely braced for safe ocean shipment.
    Shipping Reliance Industries HDPE HD5301AA is shipped as non-hazardous polyethylene pellets, not regulated for transport. Standard packaging includes 25 kg PP woven bags, palletized and stretch-wrapped, or bulk bags/containers. Transport in clean, dry vehicles and store cool, dry, ventilated, away from direct sunlight, heat, and moisture. Handle with standard industrial precautions.
    Storage Store Reliance Industries HDPE HD5301AA in a cool, dry, well-ventilated area, away from direct sunlight, heat, flames, and oxidizing agents. Keep original packaging closed to prevent moisture, dust, and contamination. Avoid prolonged UV exposure and extreme temperatures. Stack pallets securely and avoid damaging bags. Observe good housekeeping and follow the safety data sheet and local regulations.
    Shelf Life Reliance HDPE HD5301AA typically has a 24-month shelf life if stored cool, dry, away from direct sunlight in original packaging.
    Application of Reliance Industries HDPE HD5301AA

    Blown film conversion of HD5301AA on a 90 mm single-screw extruder with L/D 30:1 barrier screw and 250 mm spiral mandrel die is normally run at 80–120 kg/h, 195–210 °C melt temperature, and 3.0–3.5:1 blow-up ratio. Frost line height is held at 500–700 mm. Under these conditions 12–20 μm film retains a balance between machine-direction tear resistance and transverse-direction tensile strength. The formulation for retail carrier bag film does not exceed 5 wt% C6-LLDPE because at 5 wt% laboratory evaluation according to ASTM D882-18 shows transverse-direction tensile strength of 28–32 MPa, while dart impact according to ASTM D1709-16a Method A shifts from 90–120 g for neat HD5301AA to 130–170 g for the blend. Tear resistance is assessed according to ASTM D1922-15; the machine-direction/transverse-direction tear ratio remains above 1.8:1 when frost line height is below 700 mm. Production-scale failure modes include bubble oscillation and melt fracture at die shear rates above 450 s⁻¹, observed as rough inner bubble surface and gauge bands. If melt temperature falls below 190 °C, die pressure increases by 12–18 % and film width variability exceeds ±3 mm; if melt temperature exceeds 220 °C, oxidation generates gel particles detectable as optical defects under ASTM D1003-13 haze testing. For food-contact carrier bags, the grade must be certified under FDA 21 CFR 177.1520(c) subsection 3.1a and Regulation (EU) No 10/2011 with overall migration below 10 mg/dm².

    What Limits High-Stalk Bubble Stability During Draw-Down?

    High-stalk film lines processing HD5301AA operate within a narrower envelope than low-stalk lines because the high melt viscosity of the 0.30–0.50 g/10 min melt index band produces elevated extensional stress in the stalk. On a 120 mm extruder with a 400 mm die, die gap 1.2–1.6 mm, and blow-up ratio 4.0–5.0:1, the bubble is suspended 800–1,100 mm above the die before frost line. Melt temperature is restricted to 200–215 °C; operation below 200 °C raises die pressure to 320–360 bar and initiates sharkskin melt fracture, while operation above 215 °C thins the stalk and produces breathing marks. Cooling air velocity at the stabiliser is set at 6–10 m/s. The process yields tubular film for heavy shopping bags and industrial liners in the 20–30 μm thickness range. Under these conditions, tensile properties measured according to ISO 527-3:2018 are typically 45–55 MPa in machine direction and 30–38 MPa in transverse direction. Dart drop measured according to ASTM D1709-16a Method B for 25 μm film stays in the 180–240 g range. A practical limitation is batch-to-batch melt index variation of ±0.05 g/10 min; this variation shifts die pressure by 10–14 % and changes frost line height by 80–120 mm at constant output. The table below records the comparative envelopes used on production-scale low-stalk and high-stalk lines.

    Processing variableLow-stalk carrier filmHigh-stalk film
    Melt temperature195–210 °C200–215 °C
    Die gap1.8–2.0 mm1.2–1.6 mm
    Blow-up ratio3.0–3.5:14.0–5.0:1
    Frost line height500–700 mm800–1,100 mm
    Cooling air velocity4–6 m/s6–10 m/s

    Large-Part Extrusion Blow Moulding Pressure Drop and Flash Control

    Accumulator-head extrusion blow moulding of HD5301AA for 10–30 L industrial containers and jerry cans requires a melt temperature of 180–200 °C, blow pressure 0.6–0.8 MPa, and mould temperature 15–30 °C. The formulation is neat HD5301AA with 1.0–1.5 wt% carbon black masterbatch containing 40 wt% carbon black in an LLDPE carrier; the carbon black content in the finished wall is therefore 0.4–0.6 wt%. Screw speed on a 100 mm extruder with L/D 24:1 and grooved feed section is limited to 30–50 rpm. Parison sag becomes significant above 205 °C when shot mass exceeds 2.5 kg, producing wall-thickness variation above ±12 % and top-load failure in the shoulder region. Finished containers are tested according to ASTM D2463-15 for drop impact at -20 °C and according to ASTM D1693-15 Condition B for environmental stress crack resistance; F50 values above 500 h are accepted for moderate-risk liquids. Stack load testing is performed according to ISO 2234:2015 at 40 °C for 24 h, with creep deformation below 3 mm. Flash control at the parting line requires mould clamping force of 60–120 t for a 15 L jerry can. Regrind addition above 20 wt% reduces ESCR F50 from above 500 h to below 300 h and increases surface roughness at the pinch-off weld.

    In heavy-duty industrial liner conversion, plant regrind is introduced at 15–25 wt% into virgin HD5301AA only after regrind from edge trim and rejected film has been densified and screened to remove particles larger than 1.5 mm. Extrusion on a 120 mm single-screw line with L/D 30:1, 400 mm annular die, 2.0 mm die gap, and 3.0:1 blow-up ratio produces 75–150 μm film at 180–210 °C melt temperature. The formulation adds 0.5–1.0 wt% hindered phenolic antioxidant masterbatch and 0.3–0.5 wt% slip/antiblock masterbatch based on erucamide and synthetic silica; the silica loading in the finished film remains below 1,500 ppm to preserve Elmendorf tear resistance. Tensile properties are checked according to ISO 527-3:2018, puncture resistance according to ASTM D5748-19, and slow crack growth resistance according to ISO 16770:2004 at 50 °C. On production lines, regrind addition above 25 wt% lowers ESCR F50 from above 500 h to below 200 h and increases gel count by 30–50 % under ASTM D1003-13 haze evaluation. The finished article is used as construction debris sacks, agricultural silage covers, and temporary containment liners; when intended for chemical contact, the liner is not used for hydrocarbons because swelling exceeds 3 % mass gain after 72 h immersion in toluene at 23 °C according to ISO 175:2010. Pre-drying is not normally required, but after storage at relative humidity above 60 %, surface moisture is removed at 70–80 °C for 2–4 h in a desiccant dryer with dew point -30 °C.

    When Flat-Die Geomembrane Sheet Approaches 2.5 wt% Carbon Black

    Flat-die extrusion of HD5301AA for geomembrane sheet is carried out on a 150 mm single-screw extruder with L/D 30:1, a 2,000 mm coat-hanger die, and a three-roll polishing stack set at 50–70 °C. Melt temperature is controlled at 200–215 °C; sheet thickness ranges from 1.0 mm to 2.5 mm. Carbon black masterbatch with 50 wt% carbon black in HDPE carrier is added at 2.0–2.5 wt% to achieve finished carbon black content of 1.0–1.25 wt%. Above 2.5 wt% masterbatch, dispersion quality measured according to ISO 18553:2002 degrades: fused agglomerates larger than 60 μm appear, and dart puncture resistance according to ASTM D4833-07 declines by 15–25 % relative to 2.0 wt% loading. The stabiliser package consists of 0.2–0.5 wt% HALS masterbatch and 0.1–0.3 wt% hindered phenolic/phosphite antioxidant masterbatch; oxidative induction time measured at 200 °C according to ISO 11357-6:2018 is maintained above 25 min. Weldability is evaluated by hot-wedge welding at 320–370 °C wedge temperature and 2.0–3.0 m/min weld speed; peel separation in shear mode must remain below 10 % of the welded seam area. The compliance matrix for geomembrane applications is provided below. Published data for HD5301AA at carbon black loadings above 2.5 wt% in flat-die sheet is limited; the boundary is derived from production-scale HDPE sheet lines with equivalent melt index and density.

    RequirementStandard or regulationMeasurement condition / limit
    DensityASTM D1505-180.952–0.956 g/cm³
    Melt flow rateISO 1133-1:2022190 °C / 5 kg, 0.30–0.50 g/10 min
    Environmental stress crack resistanceASTM D1693-15 Condition B10% Igepal, 50 °C, F50 > 500 h
    Oxidative induction timeISO 11357-6:2018200 °C, OIT > 25 min
    Carbon black dispersionISO 18553:2002Agglomerate size < 60 μm
    REACH SVHCRegulation (EC) No 1907/2006< 0.1 wt%
    RoHS restricted substancesDirective 2011/65/EU Annex IIPb, Hg, Cd, Cr(VI), PBB, PBDE limits

    Because low melt index raises die pressure, tape lines feeding HD5301AA are configured with a 65 mm single-screw extruder with L/D 30:1, a flat film die gap of 0.5–0.8 mm, and a water bath at 30–45 °C. The formulation uses neat HD5301AA with 2–4 wt% coloured masterbatch and 0.2–0.5 wt% polyolefin processing aid; filler or calcium carbonate is excluded because it increases draw resonance at draw ratios above 6:1. The quenched primary tape is slit and orientated at 5:1–8:1 draw ratio in a hot-air oven set at 110–130 °C, followed by annealing at 80–110 °C on heated godets. At take-off velocities below 120 m/min, final tape tensile strength according to ISO 527-2:2012 is 280–350 MPa in the orientation direction, with elongation at break 15–25 %. Above 180 m/min, tape fibrillation and edge splitting are observed when the draw ratio exceeds 8:1; this failure is measured as a reduction in tape tenacity from 4.5–5.5 cN/dtex to below 3.5 cN/dtex. The woven fabric is tested for UV resistance according to ASTM G154-16 Cycle 2 for 500 h; tensile retention must be above 70 %. Finished articles include woven sacks, flexible intermediate bulk container fabrics, and tarpaulins.

    Thermoformed Dunnage Trays from High-Density Sheet Stock

    Sheet extrusion of HD5301AA for reusable logistics trays uses a 120 mm extruder with L/D 30:1, a 1,500 mm flat die, and a three-roll stack with roll temperatures of 40–60 °C. Sheet thickness is maintained at 1.5–3.0 mm with thickness tolerance ±5 %; recycled sheet from skeletal scrap is reintroduced at 30–50 wt% without antioxidant top-up if the regrind fraction has been processed for no more than three heat histories. Thermoforming is performed on a plug-assist pressure former with sheet surface temperature 165–180 °C, mould temperature 40–60 °C, forming pressure 0.4–0.6 MPa, and cycle time 20–35 s. Wall thickness distribution is checked by ultrasonic thickness gauge; corner thinning below 40 % of nominal sheet thickness is rejected because drop impact failure occurs at -20 °C according to ISO 6603-2:2019. Flexural modulus of the formed tray is measured according to ISO 178:2019; values of 1,100–1,300 MPa are typical. The trays are used for automotive component dunnage and industrial material handling; the grade is not suitable for direct contact with oily metal parts unless a barrier liner is used because oil absorption causes surface swelling of 1.5–2.5 % after 168 h at 23 °C according to ISO 175:2010. Process failure modes on production lines include sheet sag in the preheater when surface temperature exceeds 180 °C, and corner thinning when plug speed exceeds 200 mm/s.

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