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LyondellBasell HDPE RLLP621

    • Product Name: LyondellBasell HDPE RLLP621
    • 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 143087
    Density 0.958 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 0.35 g/10 min
    Tensile Strength At Yield 29 MPa
    Tensile Elongation At Break >600%
    Flexural Modulus 1300 MPa
    Charpy Notched Impact Strength 23 C 20 kJ/m²
    Charpy Notched Impact Strength 30 C 8 kJ/m²
    Environmental Stress Cracking Resistance F50 10 Igepal >1000 h
    Vicat Softening Temperature 128°C
    Brittleness Temperature -70°C
    Hardness Shore D 65
    Thermal Conductivity 0.38 W/m·K
    Coefficient Of Linear Thermal Expansion 1.5E-4 1/°C
    Specific Heat 1.9 kJ/kg·K
    Water Absorption 0.01%
    Dielectric Constant 2.3
    Dielectric Strength 20 kV/mm
    Volume Resistivity 1E15 ohm·cm
    Ul94 Flammability Rating HB
    Oxygen Index 17%
    Carbon Black Content 2.0%

    As an accredited LyondellBasell HDPE RLLP621 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing LyondellBasell HDPE RLLP621 is supplied in 25 kg polyethylene bags, typically 40 bags per pallet (1,000 kg total).
    Container Loading (20′ FCL) 20′ FCL loading: LyondellBasell HDPE RLLP621 in 25 kg bags, palletized, shrink-wrapped, securely stowed, optimizing container payload for safe transport.
    Shipping LyondellBasell HDPE RLLP621 is a non-hazardous high-density polyethylene resin. It is not regulated for transport by DOT, IMDG, IATA, or ADR; no UN number, hazard class, or packing group applies. Ship in closed bags or octabins, keep dry, and avoid heat, ignition sources, and dust generation. Transport as general cargo.
    Storage Store LyondellBasell HDPE RLLP621 indoors in a cool, dry, well-ventilated area, away from direct sunlight, heat, and ignition sources. Keep original containers or bags closed to prevent moisture, dust, and contamination. Elevate pallets off floors, rotate stock, and protect from physical damage. Avoid contact with strong oxidizers. Follow the supplier’s SDS and local regulations for safe handling and storage.
    Shelf Life Typically 24 months when stored unopened in original packaging, dry, at moderate temperatures, away from direct sunlight and ignition sources.
    Application of LyondellBasell HDPE RLLP621

    For twist-off HDPE closures, LyondellBasell HDPE RLLP621 is processed on high-cavitation injection moulding lines where hot-runner balance and gate freeze-off control the dimensional consistency of the sealing bead. Melt temperature is held between 190 °C and 230 °C; mould temperature is set between 8 °C and 25 °C. Injection speed is adjusted to 80–120 mm/s at the screw tip, with holding pressure between 400 bar and 700 bar and back pressure between 50 bar and 100 bar. A reciprocating screw with an L/D ratio of 20:1 and a compression ratio of 2.5:1 is standard on 32-cavity and 48-cavity closure tools. Mould shrinkage falls between 1.4% and 2.2% in the flow direction and 1.2% to 1.8% transverse, measured after 48 h at 23 °C and 50% relative humidity. The closure compound typically contains 1.5–3.0 wt% colour masterbatch, 0.05–0.15 wt% hindered phenolic antioxidant, and 0.03–0.08 wt% slip/antiblock additive. Regrind at 30 wt% is common in non-food closures; food-contact closures require clean scrap and migration testing. Compliance for beverage closures uses FDA 21 CFR 177.1520(c) 2.1 or 2.2 depending density, EU 10/2011 overall migration below 10 mg/dm², and CONEG heavy metals below 100 ppm. ESCR screening per ASTM D1693-15 Condition B should be run on each regrind lot. Finished parts include still water closures, aseptic beverage caps, and pharmaceutical child-resistant caps. Process bottlenecks on high-cavitation tools include gate blush at the annular gate and dimensional drift after hot-runner nozzle tip wear. The grade is not recommended for carbonated soft drink closure shells unless oxygen permeation and top-load retention are separately validated.

    What Limits Thin-Wall Food Packaging Cycle Time with HDPE RLLP621?

    In thin-wall food packaging, the practical cycle time is limited by cooling and ejection rather than melt plasticising. The melt temperature is set at 190–220 °C and the mould at 8–30 °C. Wall sections of 0.45–1.20 mm are filled in 0.3–0.6 s using accumulator-assisted injection. Demoulding is initiated when the part surface temperature falls below 70 °C. A nucleating agent at 0.05–0.2 wt% is added to increase crystallisation temperature and reduce post-mould warpage. Colour masterbatch is used at 1–3 wt%; regrind is limited to 20–50 wt% depending on food-contact status and the presence of in-line metal detection. The supplier datasheet should be consulted for the exact ISO 1133-1:2022 melt flow rate, because high-speed filling requires the MFR value in the upper half of the specified range. Pre-drying is not normally required; if granulate is stored below dew point or exposed to relative humidity above 60%, surface moisture may create silver streaks. Finished parts include dairy cups, tamper-evident lids, and single-use fruit containers.

    Thin-Wall Food Packaging Compliance Checklist
    ApplicationRequirementStandard/TestTypical Limit
    Food contactOverall migrationEU 10/201110 mg/dm²
    Food contactResin complianceFDA 21 CFR 177.1520(c)Density-specific olefin polymer
    Heavy metalsSum of Pb, Hg, Cd, Cr VICONEG Model Toxics100 ppm
    REACH SVHCCandidate list substanceEC 1907/20060.1 wt%

    When 5 L to 25 L open-head pails are injection moulded from HDPE RLLP621, the design priority is drop-impact retention after cold conditioning. Melt temperature is maintained at 200–240 °C and mould temperature at 15–30 °C. Clamp force on production lines ranges from 5000 kN to 12000 kN for shot weights between 800 g and 2000 g. Wall thickness is held at 1.8–3.2 mm. Carbon black masterbatch at 2.5–4.0 wt% of a 40% carbon black concentrate provides UV screening; 0.1–0.3 wt% hindered amine light stabilizer is added for long-term outdoor stacking. Regrind use is limited to 20–35 wt% because higher levels reduce ESCR and cold-temperature drop impact. Drop impact is measured per ASTM D5276-19 after 24 h at -18 °C. Stacking strength is evaluated per ASTM D4577-19 under constant load at 40 °C for 14 days. For pails certified for dangerous goods, UN 1H2 qualification requires a 1.2 m drop after storage at -18 °C and a 100 kPa hydrostatic pressure test for 30 min. End products include chemical pails, lubricant pails, and food ingredient pails. Processing bottlenecks on production tools are weld-line weakness at handle bosses and inconsistent wall thickness at the top chime.

    When HDPE RLLP621 Replaces Polypropylene in Logistics Crates

    Crate and pallet tools originally balanced for polypropylene require rebalanced gating when HDPE RLLP621 is substituted because the shrinkage range differs. HDPE mould shrinkage in logistics parts is 1.2–2.0%, while PP typically shrinks 1.0–1.8% depending wall thickness. Melt temperature is set at 200–230 °C, mould temperature at 15–30 °C, and injection speed is reduced to avoid jetting in thick ribs. Back pressure of 30–60 bar and screw rotation speed of 60–100 rpm improve additive dispersion. Unfilled HDPE flexural modulus is lower than PP; the addition of 10–25 wt% talc or calcium carbonate increases the flexural modulus from the unfilled range of 900–1300 MPa to 1800–2600 MPa when tested per ASTM D790-17. A maleic anhydride-grafted polyolefin coupling agent at 1.0–2.0 wt% may be used to improve filler-matrix adhesion. Post-consumer recycled HDPE can be incorporated at 25–50 wt%, but impact strength under ASTM D256 may fall by 15–30% depending the recycled fraction. Compliance for export is maintained under RoHS 2011/65/EU and REACH SVHC thresholds. End products include beverage crates, distribution pallets, and collapsible storage boxes. Process bottlenecks include sink marks over thick bosses and warpage caused by differential shrinkage between flow and transverse directions.

    Pipe Fittings: ESCR, Water Compliance, and Hot-Runner Balancing

    HDPE RLLP621 can be injection moulded into PE100 water network fittings when the final part passes hydrostatic strength testing under ISO 4427-3:2019. Melt temperature is held between 190 °C and 220 °C; mould temperature between 15 °C and 30 °C. Hot-runner balancing is more critical in fittings than in solid-walled pipe because weld lines at the intersection of the bore and outlet can reduce burst pressure. Injection speed is reduced to 40–70 mm/s at the screw tip, and holding pressure is maintained at 500–800 bar for 8–15 s. Shrinkage ranges from 1.5% to 2.5%, requiring core-pin retraction to avoid microcracking at the sealing surface. The compound should contain 0.1–0.2 wt% thermal stabilizer and 0.05–0.15 wt% processing aid. Regrind is generally excluded from pressure-bearing fitting bodies because hydrostatic strength loss may exceed acceptable limits. Potable water contact requires NSF/ANSI 61 or AS/NZS 4020; European potable water fittings typically conform to EN 12201-3 and ISO 4427-3. End products include compression fittings, tapping tees, and valve bodies for PE100 distribution systems. ESCR testing per ASTM D1693-15 Condition C is used as a screening tool, but the controlling qualification is the 20 °C, 100 h, 12.4 MPa hoop stress requirement for PE100. Not all injection-moulding HDPE grades meet PE100 hydrostatic classification; material-specific hydrostatic testing is mandatory before this application is qualified.

    Housewares and Appliance Components—Antistatic and Colour Masterbatch Ratios

    Storage containers, buckets, and appliance housings made from HDPE RLLP621 are moulded at melt temperatures of 190–230 °C and mould temperatures of 10–30 °C. Injection pressure is set between 600 bar and 1000 bar, with clamp force from 1500 kN to 5000 kN depending projected area. Colour masterbatch is used at 1–2 wt% for opaque shades. Antistatic additives are incorporated at 0.05–0.2 wt% to reduce dust attraction; published data for specific static decay times in this precise compound is limited. Antioxidant levels of 0.05–0.15 wt% are common for long-term thermal stability during processing. Mould shrinkage is 1.4–2.2%; dimensional checks after 24 h at 23 °C and 50% relative humidity are required before release to production. This application is governed by REACH SVHC 0.1 wt% limits and RoHS 2011/65/EU for electrical and electronic appliance housings. End products include storage boxes, buckets, vacuum cleaner housings, and white appliance internal panels. Processing bottlenecks are weld lines at handle bosses and sink marks opposite ribs; these are controlled by gas counterpressure or by reducing rib thickness to 50–60% of the nominal wall. Post-mould annealing is not normally required, but parts with thick bosses may require 2–4 h at 80 °C to stabilise dimensions before assembly.

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    Certification & Compliance
    More Introduction

    LyondellBasell HDPE RLLP621 is a high-density polyethylene grade positioned for rotational moulding of large hollow components where the production process requires a powder with controlled flow, low moulding pressure, and adequate thermal-oxidative stability during long oven dwells. The grade is characterised by a nominal density of 0.953 g/cm³ determined under ASTM D1505 and a melt flow rate of 6.2 g/10 min under ASTM D1238 at 190°C/2.16 kg. These two values place it in the high-density, moderate-flow segment of rotational moulding resins, distinct from flexible linear low-density polyethylene grades that typically exhibit densities below 0.940 g/cm³ and from fractional-melt extrusion blow moulding HDPE grades that sacrifice flow for parison melt strength. The powder is normally supplied with a particle size distribution targeted for 35 mesh sieving; particles retained on a 500 µm screen are kept low to improve wall-thickness consistency in moulded corners.

    Typical property values published for LyondellBasell HDPE RLLP621; certificate-of-analysis values take precedence for lot-specific decisions.
    PropertyTest methodValueUnit
    Melt flow rate at 190°C/2.16 kgASTM D12386.2g/10 min
    DensityASTM D15050.953g/cm³
    Tensile strength at yieldASTM D63827.0MPa
    Tensile elongation at yieldASTM D6388.0%
    Flexural modulusASTM D7901,400MPa
    Vicat softening pointASTM D1525125°C
    Brittleness temperatureASTM D746-60°C

    What Processing Conditions Govern Rotational Moulding of RLLP621?

    In rotational moulding, the polymer is not pressurised into a cavity; it is sintered against the inner surface of a heated mould under biaxial rotation. RLLP621 is used on carousel and shuttle machines with a rotation ratio commonly set at 4:1 or 5:1 primary to secondary axes, although the optimum ratio depends on part asymmetry. The oven air temperature is usually held between 260°C and 310°C, but the controlling variable is the peak internal air temperature, which is monitored by a through-hole pyrometer or a wireless in-mould thermocouple. For a nominal wall thickness of 3.0 mm, peak internal air temperature is typically 200–220°C; above 230°C, the carbonyl index rises rapidly and notched impact strength after demoulding deteriorates even if the outer wall shows no obvious discolouration. The powder must be ground to a narrow particle-size distribution. Particles coarser than 600 µm tend to remain unmelted in low-shear regions such as the parting-line flange and can form pinholes when internal air pressure during cooling is insufficient to collapse the void. The mould surface temperature at demoulding is normally kept below 95°C because higher temperatures increase thermal contraction after release and can produce warpage greater than 2.0% of long-axis dimension in flat panels. Cooling rate must be controlled as a process parameter: air-only cooling produces lower moulded-in stress but longer cycles; water mist cooling shortens cycles but increases surface shrinkage and can cause differential crystallinity across the wall thickness if the outer surface is quenched faster than the inner surface. On production-scale shuttle lines for 1,000 L tanks, the cooling stage is often staged with forced air first, then water mist, then forced air to limit warpage.

    Production-scale rotational moulding lines in the automotive, agricultural, and industrial sectors specify RLLP621 for diesel exhaust fluid tanks, sprayer tanks, water storage vessels, and material-handling bins. In rotational moulding of 1,000 L vertical storage vessels, the grade is selected where direct contact with aggressive agricultural formulations is less likely and where higher density contributes to greater stiffness against hydrostatic bulging than a linear low-density polyethylene alternative. Published data for the specific configuration of 10,000 L horizontal storage tanks is limited; the designer should therefore validate wall thickness by finite-element analysis using the measured flexural modulus and creep data from ISO 899-2 rather than by linear scaling from smaller vessels. Drop-test acceptance often follows ASTM D6783 or the equivalent purchaser specification after conditioning at -20°C; failure modes in real containers are frequently initiated at moulded-in metal inserts or at unvented air pockets near the filling port. The powder should not be dry-blended with amine-based additive masterbatches because low-molecular-weight amines can accelerate oxidative surface degradation at long oven residence. If a colourant or UV stabiliser concentrate is required, compatibility should be verified by a forced-air oven exposure trial at 290°C for a period equivalent to the full cycle, followed by impact and yellowness-index testing.

    When Polyethylene Tanks Require Chemical Resistance Verification

    When chemical resistance is required, HDPE RLLP621 is evaluated by density, crystallinity, internal stress, and service temperature rather than by a single resin rating. At 0.953 g/cm³, the grade exhibits lower steady-state permeation of aqueous liquids than an LLDPE rotational moulding grade of density 0.938 g/cm³, but the property is not a barrier solution. Resistance to dilute mineral acids, aqueous alkalis, and salt solutions is generally consistent with high-density polyethylene; however, strong oxidising acids such as concentrated nitric acid and chlorinated solvents require pre-validation under ASTM D543 or ISO 4433-1 immersion testing at the actual service temperature. Environmental stress-cracking resistance is assessed by ASTM D1693 with a defined surfactant and stress level; the result is a comparative value, not a guarantee of service life in an agricultural chemical formulation. Field data from stored surfactant-bearing liquids shows that cracks often initiate at stressed bosses or inserts rather than at the dome or flat wall. For such load-bearing insert areas, stress-cracking resistance can be improved by reducing tight-moulded-in stresses through larger insert radii and by avoiding flame treatment on stressed surfaces.

    Service Temperature Limits and Notched Impact Behaviour

    Under low-temperature service, the ductile-to-brittle transition of RLLP621 depends on wall thickness, cooling rate, and moulded-in stress. Under ISO 180, notched impact values of HDPE RLLP621 are lower than those of flexible LLDPE rotomoulding grades because the higher density and crystallinity that provide stiffness reduce energy absorption. The practical ductile-to-brittle transition for a 6.0 mm thick water tank is generally near -40°C, but parts with sharp corners or weld fillets may fail at higher temperatures. Continuous service above 60°C under hydrostatic pressure or other sustained load should be avoided unless creep modulus data under ISO 899-2 support the design. The grade is not recommended for pressurised hot-water service; combined hoop stress and oxidative degradation in hot aqueous contact accelerate creep failure and are not represented by standard short-term burst tests. For outdoor service, the base resin should be stabilised with a UV package suitable for the latitude and service life; accelerated weathering under ISO 4892-2 or ASTM G154 is used to compare pigmented compounds, but is not a replacement for field validation in high-UV environments.

    Comparing RLLP621 with Blow Moulding and Injection Moulding HDPE

    The differentiation from other HDPE grades is process- and part-geometry-specific. RLLP621 is supplied as a powder for low-pressure moulding, whereas blow moulding HDPE is supplied as pellets for extrusion parison formation and injection moulding HDPE is supplied as pellets or granules for high-pressure mould filling.

    Comparative processing and property profile of HDPE RLLP621 against alternative HDPE processes.
    VariableHDPE RLLP621 rotational mouldingExtrusion blow moulding HDPEInjection moulding HDPE
    Melt flow rate at 2.16 kg6.2 g/10 min0.30–0.70 g/10 min large-part grades5.0–8.0 g/10 min similar-flow grades
    Density0.953 g/cm³0.950–0.955 g/cm³0.952–0.960 g/cm³
    Moulding pressure<0.5 MPa internal air0.5–1.0 MPa parison inflation60–120 MPa injection
    Typical wall thickness2.0–8.0 mm1.0–4.0 mm1.0–3.0 mm
    Moulded-in stressLowModerateHigh
    Cycle time30–90 minModerate10–60 s

    Compared with extrusion blow moulding grades, RLLP621 has insufficient melt strength to support a stable parison on a continuous shuttle or accumulator head; its high flow promotes rapid sintering but cannot maintain the dimensional stability required for multi-layer parison walls. Compared with injection moulding grades of similar flow, rotomoulded parts from RLLP621 typically have lower frozen-in orientation and lower peak flexural modulus because the cooling rate is several orders of magnitude slower than in a chilled injection mould. The absence of high injection pressure also allows the use of low-cost cast-aluminium or sheet-metal moulds, but it limits the minimum wall thickness and corner radius that can be reproduced. The grade is not a direct replacement for either process and should be specified only when the part geometry is hollow, the production volume is low to moderate, and the wall thickness is within the process range.

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