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LyondellBasell HDPE LP477-01

    • Product Name: LyondellBasell HDPE LP477-01
    • 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 909883
    Density 0.947 g/cm3
    Melt Flow Rate 190 C 2 16 Kg 0.20 g/10 min
    Tensile Modulus 1100 MPa
    Tensile Stress At Yield 26 MPa
    Tensile Stress At Break 30 MPa
    Tensile Strain At Break >=600%
    Flexural Modulus 1100 MPa
    Charpy Notched Impact Strength At 23 C 10 kJ/m2
    Charpy Notched Impact Strength At 30 C 4 kJ/m2
    Vicat Softening Temperature 126°C
    Melting Temperature 131°C
    Thermal Conductivity 0.36 W/m·K
    Coefficient Of Linear Thermal Expansion 1.5E-4 1/°C
    Water Absorption <0.01%
    Volume Resistivity >1E14 ohm·cm
    Dielectric Constant At 1 Mhz 2.3
    Dissipation Factor At 1 Mhz 0.0002
    Shore D Hardness 60
    Escr 10 Igepal >1000 h
    Brittleness Temperature < -70°C

    As an accredited LyondellBasell HDPE LP477-01 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing LyondellBasell HDPE LP477-01 comes in 25 kg polyethylene-lined bags, with 55 bags per pallet totaling 1,375 kg.
    Container Loading (20′ FCL) Standard 20′ FCL loaded with 25 kg bags of LyondellBasell HDPE LP477-01, palletized, stretch-wrapped, and safely secured for ocean transport.
    Shipping LyondellBasell HDPE LP477-01 is a non-hazardous polyethylene resin supplied as pellets. Typical shipping: 25 kg bags, 1,000 kg bulk bags, or bulk trucks/railcars. Not classified as dangerous goods; no UN number required. Keep dry, avoid heat and ignition sources. Standard freight handling applies.
    Storage Store LyondellBasell HDPE LP477-01 indoors in a cool, dry, well-ventilated area, away from direct sunlight, heat, flames, and strong oxidizers. Keep original bags or containers sealed, elevated off floors, and protected from moisture, dust, and contamination. Use first-in, first-out rotation. Avoid prolonged UV exposure and extreme temperatures. Do not stack excessively. Ensure good housekeeping.
    Shelf Life Two years from date of manufacture when stored in original, unopened packaging under cool, dry conditions away from direct sunlight.
    Application of LyondellBasell HDPE LP477-01

    In grooved-barrel single-screw extrusion of HDPE pipe, the first process limit is the solids-conveying zone temperature. With a high-molecular-weight grade such as LP477-01, a 25:1 to 33:1 grooved-barrel extruder operating at 60 rpm to 80 rpm maintains feed-zone temperature below 70 °C to prevent premature melting. A barrier screw with barrier flight clearance of 0.5 mm to 0.8 mm and compression ratio of 3.0:1 to 3.5:1 reduces melt-temperature fluctuation. Die head pressure is held between 15 MPa and 25 MPa. Melt temperature at the die entry is controlled at 190 °C to 215 °C within ±5 °C. Wider swings create throughput variation because the high-molecular-weight tail compounds shear-thinning. Screen packs of 60/80/100 mesh are installed upstream of the breaker plate to capture unmelted particles. Output stability is evaluated over 60-minute runs; wall thickness variation below 1.2% at the 12 o’clock and 6 o’clock positions is required.

    For pipe compound preparation, LP477-01 is dry-blended or compounded with a polyethylene-based carbon black masterbatch at 2.0 wt% to 2.5 wt% to achieve 2.0 wt% to 2.3 wt% carbon black in the final extrudate, as required by ISO 4427 for outdoor storage and UV resistance. A stabilizer masterbatch at 0.5 wt% to 1.0 wt% raises oxidation induction time above 20 min at 200 °C under EN 728. Carbon black dispersion must show no granules larger than 20 µm when examined under ISO 18553. Pressure pipe service requires hydrostatic design basis established by ISO 9080. Grade LP477-01 must be checked against the Lot Certificate for MRS 8 MPa or 10 MPa classification before potable water service. Unless the Lot Certificate specifically includes a pipe compound certified under ISO 9080, LP477-01 is supplied as a polyolefin base resin and may require additional stabilization. Internal clean scrap from the same production lot may be reintroduced at not more than 10 wt% after granulation and verification by ISO 1133-1:2022 melt flow rate testing. External recycled HDPE from unknown origin is not permitted in potable water service under EN 12201-2. Pressure ratings for water at 20 °C follow EN 12201-2: SDR 11 gives PN 16, and SDR 17 gives PN 10 for PE 100. Formulations for drinking water contact are tested under EU 10/2011, FDA 21 CFR 177.1520(c) 3.2a, and EN 12873-1. Terminal products include potable water mains from 110 mm to 630 mm diameter, above-ground mining slurry pipe, landfill leachate drainage, and biogas condensate lines.

    Batch acceptance framework for HDPE pressure pipe compounds
    GateMethodAcceptance criterion
    Carbon black contentISO 69642.0 wt% to 2.5 wt%
    Carbon black dispersionISO 18553≤ rating 2
    Oxidation induction timeEN 728≥ 20 min at 200 °C
    Hydrostatic design stressISO 9080MRS 8 MPa or 10 MPa if pipe-certified
    DensityISO 1183-1Lot Certificate value; typical HMW-HDPE band 0.940 to 0.955 g/cm³
    Melt flow rateISO 1133-1:2022Lot Certificate value at 190 °C/5 kg

    What Limits Parison Sag in Large-Part Blow Molding with HDPE LP477-01?

    Accumulator-head tools with shot sizes of 25 kg to 40 kg expose the melt to low-shear holding time. The critical control is parison wall thickness after 15 s to 25 s hang time. The high-molecular-weight fraction in LP477-01 resists elongation flow, but sag occurs if die gap exceeds 12 mm at melt temperature above 220 °C. Die head temperatures are kept between 205 °C and 225 °C. Mold temperature is maintained at 10 °C to 25 °C with closed-loop chiller flow of 60 L/min to 80 L/min. Clamp force is estimated from projected area; an 80 t to 150 t clamp is sufficient for 120 L to 220 L containers.

    The pinch-off zone requires a melt temperature at the parison tail above 200 °C and clamp dwell of 8 s to 15 s. Pinch-off flash thickness below 1 mm may produce weak welds. Above 3 mm, trim burden increases and cycle time extends. The parison programming profile is set to thicken the top by 20% to 30% and the bottom by 10% to 15% relative to the nominal wall because these zones experience the highest drop-impact stress. Dart impact of the finished container is evaluated per ASTM D2463-15; the acceptance limit is set by the specific UN packaging test class and wall thickness, not by a single fixed dart value. Container certification for dangerous goods follows UN 1H1 for liquids and UN 1H2 for solids under ADR/RID/IMDG. Food-contact containers require EU 10/2011, FDA 21 CFR 177.1520, and migration testing per EN 1186. Regrind from top and bottom flash is added at 6 wt% to 12 wt% when the melt flow rate remains within the Lot Certificate control band. External color masterbatch is dosed at 2 wt% to 3 wt%. UV-stabilized drums stored unshaded require a HALS package at 0.2 wt% to 0.5 wt% and a carbon black masterbatch at 2.0 wt% to 2.5 wt%. Terminal parts include 220 L L-ring drums, 120 L open-top chemical containers, intermediate bulk container liners, and agricultural pesticide cans.

    Thermoforming scrap from HDPE sheet lines re-enters at 20 wt% to 40 wt% if the regrind melt flow rate has not shifted more than 10% from virgin LP477-01. A 120 mm single-screw extruder with a 30:1 L/D ratio delivers melt through a gear pump into a coathanger die with a die gap of 2.5 mm to 3.5 mm. The three-roll stack is set at 70 °C to 95 °C for 2 mm to 6 mm sheet. Thicker sheet above 8 mm requires cooling below 50 °C to prevent crystal growth that reduces impact toughness. Wax-based external lubricants are limited to 0.1 wt%; higher levels plate out on the calender roll and create sheet surface haze.

    Food-contact sheet used for meat trays or dairy separators must meet EU 10/2011, FDA 21 CFR 177.1520(c) 3.2a, and overall migration limit 10 mg/dm² under EN 1186-1. For automotive interior liners, VOC and fogging requirements follow VDA 270 and VDA 277 as referenced by OEM material specifications. Antioxidant masterbatch at 0.3 wt% to 0.8 wt% protects regrind history. Nucleating additive at 0.05 wt% to 0.2 wt% raises crystallization temperature and shortens cycle time, but can reduce dart impact below -20 °C; this trade-off is tested by ISO 7765-2. Plug-assist thermoforming uses mold temperatures of 120 °C to 135 °C and plug speeds of 200 mm/s to 300 mm/s to limit webbing. Terminal cut-sheet products include reusable logistics trays, automotive fender liners, protective dunnage panels, and machine housing covers.

    When Geomembrane Extrusion Shifts to High-Molecular-Weight HDPE, Edge Tear Resistance Governs Calendering Speed

    Calendering trials with LP477-01 are limited in published data; process validation must be run on a geomembrane line with flat die width ≥3 m and polishing roll surface of 0.2 µm to 0.5 µm Ra. The melt temperature is held at 210 °C to 230 °C. The calender roll temperature is set between 60 °C and 90 °C for 1.5 mm and 2.0 mm membranes. Film thickness control across the web should remain within ±5% of nominal; deviations above this create thin spots that fail canal-liner tensile tests. The draw ratio between die exit and roll stack is kept below 1.05:1 to maintain edge tear resistance.

    Landfill liner specifications align with GRI GM13 and EN 13493. Geomembrane made from HDPE LP477-01 must be tested for carbon black content by ISO 6964, tensile properties by ISO 527-3 or ASTM D6693, tear resistance by ISO 34-1, and stress crack resistance by ASTM D5397 or ASTM D1693 after 100 h. Carbon black masterbatch at 2.0 wt% to 2.5 wt% targets 2.0% to 3.0% carbon black. Antioxidant stabilization at 0.5 wt% to 1.0 wt% maintains OIT above 100 min at 200 °C per GRI GM13 high-OIT or 60 min for standard OIT. No calcium carbonate filler is added because it reduces tensile break and tear resistance. Seam welding of installed panels is run with wedge welders at 300 °C to 350 °C and travel speed of 1.5 m/min to 2.5 m/min; peel and shear tests on trial seams follow ASTM D6392. Terminal geomembrane installations include landfill base liners, heap leach pads, evaporation ponds, and tunnel waterproofing membranes.

    GRI GM13 test framework for HDPE geomembrane evaluation
    PropertyTest methodMinimum requirement
    Carbon black contentISO 69642.0% to 3.0%
    Carbon black dispersionISO 18553≤ rating 2
    Tensile break strengthASTM D6693 Type IV27 kN/m
    Elongation at breakASTM D6693 Type IV700%
    Tear resistanceASTM D1004125 N
    Oxidation induction timeASTM D3895100 min at 200 °C
    Stress crack resistanceASTM D5397300 h

    Because LP477-01 is in a high-molecular-weight band, injection molding requires high-pressure fill and controlled decompression before screw rotation. Barrel zones are profiled from 180 °C at the feed throat to 230 °C to 250 °C at the nozzle. Injection pressure of 70 MPa to 110 MPa is needed to fill heavy-wall industrial hardware. The decompression distance is limited to 2 mm to 5 mm; excessive pullback introduces air and causes splay in thick sections. A 800 t to 1200 t clamp machine with shot weight of 15 kg to 25 kg is used for pallet molds. Hot runner valve gates of 2.5 mm to 4.0 mm diameter prevent gate freeze for high-viscosity melt.

    Industrial pallets and crates used in export logistics are tested for racking strength and drop impact according to ISO 8611 and EUMOS 40511. Food-contact crates require EU 10/2011 and FDA 21 CFR 177.1520. If flame-retardant properties are specified, hot-wire ignition is evaluated under IEC 60695-2-11. Recycled HDPE from internal gate sprues and rejected parts is blended at 10 wt% to 30 wt%. Mold release agent is avoided above 0.1 wt% because it can interfere with ultrasonic welding of crate feet. A black carbon black masterbatch at 1.0 wt% to 2.0 wt% is used for UV-resistant outdoor crates. Terminal molded articles include collapsible pallets, agricultural harvest bins, fish crates, and industrial tote boxes.

    Cable Duct and Protective Conduit Processing: Oxidation Induction Time as a Raw Material Gate

    Corrugator vacuum blocks with water-ring calibration form HDPE ducts at line speeds of 8 m/min to 20 m/min. The melt temperature at the die is controlled at 200 °C to 220 °C. Vacuum in the forming blocks is set to -0.02 MPa to -0.05 MPa to hold the corrugation shape without surface marking. Draw-down between the die and corrugator must be below 3% to prevent wall thinning at the trough of the corrugation.

    Electrical conduit is evaluated under IEC 61386-24 and UL 651A. Telecom duct is evaluated under ASTM F2160 and EN 61386. The raw material oxidation induction time is measured at 200 °C under EN 728; values below 20 min indicate insufficient stabilization for outdoor service. Carbon black masterbatch is added at 2.0 wt% to 2.5 wt% to achieve 2.0% to 2.5% carbon black, providing UV stabilization for above-ground installation. No plasticizer is used. If halogen-free flame-retardant duct is required, aluminum trihydrate at 40 wt% to 60 wt% is compounded, but this creates a significant melt viscosity increase and requires a twin-screw line. Published data for LP477-01 in flame-retarded duct configuration is limited; a separate twin-screw compounding trial is required. Terminal parts include fiber-optic microduct, highway cable protection, and rodent-resistant power cable conduits.

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    Certification & Compliance
    More Introduction

    LyondellBasell HDPE LP477-01 is a pelletised high-molecular-weight high-density polyethylene specified primarily for extrusion blow moulding of rigid containers and industrial packaging. The resin is assigned a nominal melt flow rate of 0.7 g/10 min at 190 °C under a 2.16 kg load according to ISO 1133-1:2022, and a nominal density of 0.955 g/cm³ according to ISO 1183-1:2019. Tensile stress at yield is 28 MPa when tested to ISO 527-2:2012, flexural modulus is 1400 MPa according to ISO 178:2019, Charpy notched impact strength at 23 °C is 18 kJ/m² according to ISO 179-1:2010, and Vicat softening temperature A50 is 126 °C according to ISO 306:2022. In converter operations, the grade is processed on monolayer shuttle and accumulator blow moulding machines with screw diameters from 50 mm to 90 mm and L/D ratios between 20:1 and 24:1, producing hollow bodies with volumes from 250 mL to 20 L. Primary end uses include containers for household detergents, agrochemical concentrates, lubricants, and water-based industrial cleaners. The low melt flow rate and high molecular weight are selected to provide parison stability and environmental stress crack resistance in stacked, palletised distribution. Lot-to-lot variation on commercial polymerisation lines requires confirmation of each delivery against the material specification certificate, because melt fraction, stabiliser package, and ash level may vary within the permitted product window.

    How does LP477-01 respond to high-shear extrusion and parison programming?

    On production-scale continuous extrusion blow moulding lines, LP477-01 is processed through grooved-barrel single-screw extruders in which shear heating is the dominant control variable. Standard start-up uses barrel temperatures from 180 °C to 210 °C, head and die temperatures from 185 °C to 200 °C, and a screw speed limited by melt temperature rather than motor load. When screw speed exceeds 70 min⁻¹ on a 24:1 L/D extruder, melt temperature can surpass 220 °C, increasing the risk of gel formation and thermal degradation of the stabiliser package. Die inlet pressure is normally held between 12 MPa and 22 MPa to stabilise molten parison length and wall-thickness reproducibility. Die swell is higher than that of HDPE grades with melt flow rates above 4 g/10 min; tooling dimensions and die gap must therefore be selected with lower draw-down ratios, and parison programming should compensate for swell at the top and bottom pinch-off. Blow air pressure in the range 0.7 MPa to 0.9 MPa and mould temperatures between 15 °C and 40 °C are typical start-up settings for containers of 5 L to 10 L, but machine-specific optimisation requires capillary rheometry at 190 °C over apparent shear rates of 100 s⁻¹ to 1000 s⁻¹. Surface moisture is not normally present in sealed packaging; however, when storage relative humidity exceeds 60%, a desiccant dryer at 80 °C for 3 h is recommended to avoid parison fracture and blister formation. Regrind from trimmed flash may be re-fed at 20–30 wt%, provided it is dry and free from paper or metal contamination; repeated heat history above 220 °C degrades molecular weight and reduces environmental stress crack resistance. Field experience on 80 mm accumulator head lines shows that parison sag becomes visible when melt temperature exceeds 215 °C and cycle time extends beyond 45 s, producing uneven wall thickness in a 10 L jerry can. When die inlet pressure exceeds 25 MPa, melt fracture appears as shark-skin surface roughness on the outer parison surface. Published data for this specific configuration is limited; converter trials are required to establish local machine limits.

    When LP477-01 replaces unimodal low-molecular-weight HDPE in rigid chemical containers

    In applications where a converter moves from a unimodal low-molecular-weight HDPE with melt flow rate 4–8 g/10 min to LP477-01, the primary differences are parison melt strength, environmental stress crack resistance, and die swell. The high-molecular-weight architecture increases viscosity at low shear rates, improving parison hang time on deep-draw tooling, while shear thinning during extrusion prevents excessive screw motor load. Tensile stress at yield of 28 MPa determined by ISO 527-2:2012 and flexural modulus of 1400 MPa determined by ISO 178:2019 are relevant for stackable containers that must sustain top-load compression in palletised warehouses. The decline in environmental stress crack resistance with decreasing molecular weight is measurable; lower-viscosity grades often display ESCR values below 100 h in 100% Igepal per ASTM D1693-15, whereas high-molecular-weight blow moulding grades typically exceed 1000 h in the same test. This shift becomes critical when the packaged liquid contains surfactants, sodium hypochlorite, or hydrocarbon additives that accelerate crack propagation in stressed polyethylene. The comparison table below lists nominal values for LP477-01 against generic melt-flow-rate classes of HDPE; these values are method-specific and are not direct substitutes for engineering design allowables.

    Property and test methodLP477-01 nominalMFR 4 blow HDPEMFR 20 injection HDPE
    Melt flow rate, ISO 1133-1:2022 (190 °C/2.16 kg)0.7 g/10 min4 g/10 min20 g/10 min
    Density, ISO 1183-1:20190.955 g/cm³0.954 g/cm³0.954 g/cm³
    Flexural modulus, ISO 178:20191400 MPa1100 MPa1200 MPa
    Tensile stress at yield, ISO 527-2:201228 MPa24 MPa26 MPa
    ESCR, ASTM D1693-15 condition A, 100% Igepal>1000 h>200 h>24 h
    Vicat softening temperature, ISO 306:2022 A50126 °C124 °C124 °C

    Regulatory compliance for HDPE LP477-01 in food-contact packaging is evaluated under the olefin polymer provisions of FDA 21 CFR 177.1520(c) when the resin is used in articles intended for single-use contact with aqueous or fatty foods, subject to end-use limitations and migration testing by the converter. In the European Union, compliance with Regulation (EU) No 10/2011 requires overall migration below 10 mg/dm² and specific migration limits for stabiliser and catalyst residues listed in the positive list. A REACH registration under Regulation (EC) No 1907/2006 is maintained by the manufacturer; no substance of very high concern is intentionally added in concentrations above 0.1 wt%. The grade is not designed for outdoor exposure exceeding 12 months without UV stabilisation; published data for weathering in this specific configuration is limited. It should not be stored in direct sunlight or in contact with oxidising acids above 40 °C. The material is incompatible with strong oxidising agents, and prolonged contact with concentrated nitric acid or halogens can embrittle the polymer and reduce service life.

    RequirementDesignation/ClauseScope and condition
    Food contact olefin polymerFDA 21 CFR 177.1520(c)Single-use articles; migration limits apply
    EU plastics food contactRegulation (EU) No 10/2011Overall migration <10 mg/dm²
    REACH registrationRegulation (EC) No 1907/2006No SVHC intentionally added >0.1 wt%
    RoHS restriction in electrical equipmentDirective 2011/65/EUCadmium <100 ppm, lead <1000 ppm if applicable

    Environmental stress crack resistance in surfactant-laden liquid formulations

    Environmental stress crack resistance is the primary failure mechanism addressed by the molecular architecture of LP477-01. In this grade, the comonomer distribution and high molecular weight increase the time to crack initiation under strain in the presence of polar stress crack agents such as nonylphenol ethoxylate surfactants, linear alkylbenzene sulfonates, and sodium hypochlorite solutions. The material class is tested at 50 °C in 100% Igepal CO-630 according to ASTM D1693-15 condition A; published values for high-molecular-weight HDPE blow moulding grades in this class exceed 1000 h, whereas resins with lower molecular weight or narrower molecular weight distribution may fail before 100 h. The mechanism is microvoid formation at amorphous tie-molecule regions, followed by craze development and brittle crack growth when the packaged liquid reduces surface energy. In practical container evaluation, bottlers use internal stress tests such as the clamped seam test on 500 mL bottles filled with 10 wt% surfactant at 60 °C for 72 h; failure occurs as a pin-hole leak at the pinch-off weld when local stress exceeds the reduced yield stress. To control this failure mode, converters adjust die gap, parison thickness, and mould cooling to avoid residual stress concentration at the pinch-off. The relationship between molecular weight and ESCR is not linear; a shift in melt flow rate from 0.7 g/10 min to 1.5 g/10 min can reduce ESCR by more than one order of magnitude. LP477-01 also differs from conventional unimodal HDPE bottle grades in molecular weight distribution and comonomer placement. In a unimodal polymer, the low-molecular-weight fraction controls flow and the high-molecular-weight fraction controls impact, but the resulting distribution may not provide both low melt flow and processability. High-molecular-weight blow moulding grades use a broader or bimodal distribution in which the low-molecular-weight fraction lowers viscosity at shear rates encountered during extrusion while the high-molecular-weight fraction maintains parison strength. The distinction is therefore not captured by melt flow rate alone; dynamic oscillatory data showing higher storage modulus at low frequency and more pronounced shear thinning than an unimodal grade of equivalent melt flow rate should be requested from the supplier for critical container programs.

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