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LyondellBasell HDPE ACP 6031D

    • Product Name: LyondellBasell HDPE ACP 6031D
    • 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 358539
    Polymer Type High Density Polyethylene (HDPE)
    Density 0.959 g/cm³
    Melt Flow Rate 190 C 5 Kg 0.25 g/10 min
    Tensile Modulus 1100 MPa
    Tensile Stress At Yield 25 MPa
    Tensile Strain At Yield 9%
    Tensile Strain At Break >600%
    Charpy Notched Impact Strength 23 C 15 kJ/m²
    Charpy Notched Impact Strength 30 C 6 kJ/m²
    Vicat Softening Temperature 82°C
    Oxidation Induction Time 200 C >20 min
    Carbon Black Content 2.2%
    Mrs Rating 10 MPa
    Pe Pipe Classification PE 100
    Color Black

    As an accredited LyondellBasell HDPE ACP 6031D factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing LyondellBasell HDPE ACP 6031D is supplied in 25 kg polyethylene bags, 1,000 kg bulk bags, or bulk containers.
    Container Loading (20′ FCL) 20′ FCL container loading for LyondellBasell HDPE ACP 6031D: 25 kg bags, palletized, dry container, securely stowed, approx. 20 MT.
    Shipping HDPE ACP 6031D is a non-hazardous polyethylene resin. It ships as pellets in 25 kg bags, bulk bags, or bulk containers, palletized and wrapped. No UN number, hazard class, packing group, or transport label required. Store under normal conditions; keep dry. Protect from moisture, contamination, and direct sunlight.
    Storage Store LyondellBasell HDPE ACP 6031D in a cool, dry, well-ventilated area. Keep containers closed and protected from direct sunlight, moisture, heat, and ignition sources. Avoid contamination with oils, chemicals, odors, or strong oxidizers. Use original packaging, stack securely, and rotate stock. Maintain clean handling areas. Observe local regulations and supplier storage recommendations. Ensure good ventilation during handling and do not exceed recommended storage temperatures.
    Shelf Life Shelf life is typically 24 months when stored unopened in original packaging, dry, cool, and away from direct sunlight.
    Application of LyondellBasell HDPE ACP 6031D

    In high-cavitation closure production, LyondellBasell HDPE ACP 6031D is processed at melt temperatures of 200 °C to 230 °C because the nominal melt flow rate of 1.9 g/10 min at 190 °C/2.16 kg under ISO 1133-1 permits filling of 48- to 96-cavity valve-gated hot runners without excessive machine barrel pressure. The density of 0.960 g/cm³ determined by ISO 1183-1 gives sufficient skirt hoop stiffness for 30/25 mm PCO 1881 carbonated-soft-drink caps and 26/22 mm still-water caps. A production compound typically contains 0.8 wt% to 1.2 wt% of a 5 % erucamide slip masterbatch, equivalent to 400 ppm to 600 ppm active slip, and 0.5 wt% to 1.0 wt% of a 60 % titanium dioxide white masterbatch for opacity. Total masterbatch loading is maintained below 2.0 wt% because higher loadings shift the gate-freeze time and produce visual flow lines on the cap crown. In a 72-cavity hot-runner system, the barrel profile is set at 200 °C, 210 °C, 220 °C, 225 °C with nozzle at 230 °C and hot-runner manifolds at 230 °C to 240 °C. Injection velocity ranges from 80 mm/s to 120 mm/s. Hold pressure of 40 MPa to 70 MPa is applied for 0.5 s to 1.0 s before gate freeze. Cycle times of 7 s to 11 s are normal for a 1.5 mm skirt wall. On production-scale equipment, gate-stringing occurs if the hot-runner gate temperature exceeds 250 °C or if the mould cooling circuit inlet exceeds 18 °C. Food-contact compliance rests on FDA 21 CFR 177.1520 for olefin polymers and Regulation (EU) No 10/2011 Annex I with an overall migration limit of 10 mg/dm². Closure performance is validated by carbonation retention at 3.5 vol to 4.5 vol CO₂ at 25 °C and torque retention after 14 days. ESCR is evaluated on compression-moulded plaques per ASTM D1693 Condition B at 50 °C; F50 values for this density class commonly exceed 100 h. Terminal articles are single-piece beverage caps with tamper-evident bands.

    Why Does Wall Thickness Below 0.5 mm Shift the ESCR Failure Mode in Dairy Portion Cups?

    Wall thickness reduction below 0.5 mm alters the failure mechanism in thin-wall HDPE food containers from slow crack growth initiated by surface scratches to delamination along frozen-in flow fronts. In ACP 6031D, thin-wall dairy and snack packaging is injection moulded at melt temperatures of 200 °C to 220 °C through hot-runner stack tools with nominal wall sections of 0.4 mm to 0.8 mm and flow-length-to-wall-thickness ratios of 150:1 to 200:1. High injection velocity of 120 mm/s to 180 mm/s is required to fill the cavity before the melt front freezes. Switchover to hold is set by screw position 3 mm to 5 mm before final cushion. Packing pressure of 55 MPa to 70 MPa is applied for only 0.15 s to 0.30 s; longer packing creates core deflection and gate-stringing at wall sections below 0.6 mm. Mould temperature is controlled at 10 °C to 15 °C to achieve demoulding rigidity and a cycle of 4.0 s to 6.0 s. The formulation uses 1.5 wt% to 2.5 wt% of a 60 % titanium dioxide masterbatch for opacity and 0.05 wt% to 0.10 wt% of a slip concentrate. No nucleating agent is added because rapid cooling already reduces spherulite size and improves sidewall gloss. Mould shrinkage is measured by ISO 294-4 and falls between 1.8 % and 2.4 % for 0.8 mm plaques. Post-mould warpage is controlled by keeping cavity-to-core cooling imbalance below 5 °C and by limiting demoulding temperature to 65 °C. Compliance for dairy portion cups, diced-fruit cups, and snack trays includes Regulation (EU) No 10/2011 overall migration below 10 mg/dm², Regulation (EC) No 2023/2006 good manufacturing practice, and FDA 21 CFR 177.1520 for refrigerated and room-temperature food types. Hot filling above 75 °C is outside the validated window for this grade because the thin wall loses stack load stiffness and lid fit deteriorates.

    Cosmetic overcap production with HDPE ACP 6031D uses cold-runner tools where gate vestige is placed on the inner dome and hidden by the bottle neck finish. In 12- to 24-cavity hardened steel tools, melt temperatures of 205 °C to 225 °C and mould temperatures of 30 °C to 40 °C allow VDI 24 textured sidewalls to release without excessive ejection force. Cycle times of 14 s to 18 s are common for 1.5 mm to 2.0 mm walls. The compound contains pearlescent masterbatch at 1.0 wt% to 2.0 wt%, erucamide slip masterbatch at 0.1 wt% to 0.3 wt%, and a hindered amine light stabilizer at 0.1 wt% to 0.2 wt% for coloured exterior surfaces. Cold-runner scrap is granulated and returned at up to 15 wt% without shifting snap-fit insertion force beyond ±8 %. Stripping torque is evaluated at 0.4 N·m to 1.2 N·m on the bottle neck finish. Dimensional audit is performed according to ISO 2859-1 with AQL 0.65 for critical diameters. Cosmetic packaging does not require food-contact status, but the final article must satisfy REACH Annex XVII restrictions and the Packaging and Packaging Waste Directive 94/62/EC heavy-metal limit of 100 mg/kg summed across lead, cadmium, mercury, and hexavalent chromium. Terminal articles are snap-fit overcaps for fragrance bottles, personal-care jars, and cosmetic cream containers.

    When 25 wt% Post-Consumer HDPE Is Tumble-Mixed for Injection-Moulded Logistic Crates

    Post-consumer HDPE addition at 25 wt% shifts both process and mechanical boundaries in crate and pail production. The blend combines 75 wt% LyondellBasell HDPE ACP 6031D with 25 wt% washed and dried post-consumer HDPE flake having a melt flow rate of 0.6 g/10 min to 1.0 g/10 min and bulk density above 0.50 g/cm³. Gravimetric dosing accuracy of ±0.5 wt% is required because PCR melt-flow variability above 0.3 g/10 min alters cushion control and cushion repeatability. A 200 µm to 400 µm breaker-plate screen pack or a screen changer at the nozzle is used to reduce hard gels originating from label and cap residues. Melt temperature is set at 220 °C to 250 °C, mould temperature at 20 °C to 30 °C, injection pressure up to 120 MPa, and hold pressure at 50 MPa to 80 MPa for 4 s to 8 s. A 1,200 t to 1,600 t clamp force is required for 3.5 kg ventilated crates with wall sections of 3 mm to 5 mm; cycle time is 30 s to 45 s. The formulation includes 1.5 wt% to 2.5 wt% carbon black masterbatch for ultraviolet resistance and 0.1 wt% to 0.2 wt% antioxidant concentrate. Published data for this specific PCR blend is limited, but the following table provides indicative values for this injection-moulding grade class.

    PropertyTest Method100 % Virgin ACP 6031D75 % Virgin / 25 % PCR
    Tensile yield strengthASTM D63830 MPa27 MPa
    Flexural modulusISO 1781,450 MPa1,300 MPa
    Notched Charpy impactISO 179-1/1eA8 kJ/m²6 kJ/m²
    ESCR F50, Condition BASTM D1693>100 h65 h
    Melt flow rateISO 1133-11.9 g/10 min1.6 g/10 min

    Compliance for industrial logistic crates and pails is governed by REACH Annex XVII restrictions, the Packaging and Packaging Waste Directive 94/62/EC recycling and heavy-metal limits, and documented absence of substances of very high concern in the PCR input stream. Terminal products are ventilated logistic crates, storage totes, and 5 L to 20 L open-top pails.

    Child-Resistant Closure Leaf Spring and Tear Band Strain Localization

    Child-resistant closure geometries impose a different strain state than beverage caps because the leaf spring must deflect repeatedly and the tear band must break at a defined torque. ACP 6031D is moulded in 16- to 32-cavity hot-tip tools at melt temperatures of 220 °C to 235 °C and mould temperatures of 25 °C to 35 °C. Cycle times of 12 s to 16 s are longer than beverage closure cycles because the flexure section is 1.8 mm to 2.2 mm thick. The compound uses 0.8 wt% to 1.0 wt% of a colour masterbatch suitable for oral solid-dose packaging and 0.05 wt% acid scavenger. Slip additives are excluded because the closure must retain frictional torque against the bottle neck. Gate diameter is kept below 0.8 mm to prevent gate-vestige interference with the child-resistant locking studs. Leaf-spring flexural modulus is measured by ISO 178 and should remain above 1,400 MPa. Tear-band tensile elongation is checked by ASTM D638 at 25 mm/min with failure strain between 8 % and 20 %. Compliance for pharmaceutical closures includes USP 661.1 for plastic packaging systems, ISO 8317 child-resistant package testing, and FDA 21 CFR 177.1520 where the package contacts oral solid dosage forms. Terminal products are child-resistant caps and closures for nutraceutical and liquid medication bottles.

    Application SegmentMandatory FrameworkRelevant Test or VerificationKey Numerical Limit
    Beverage closuresFDA 21 CFR 177.1520, EU 10/2011Overall migration, ESCR, carbonation retention10 mg/dm²
    Thin-wall dairy food packagingEU 10/2011, EC 2023/2006Overall migration, shrinkage, wall distribution10 mg/dm²
    Cosmetic overcapsREACH Annex XVII, 94/62/ECHeavy-metal screening, stripping torque100 mg/kg heavy-metal sum
    Industrial crates with PCRREACH, 94/62/ECTensile, flexural, ESCR, melt flowSee mechanical table
    Pharmaceutical closuresUSP 661.1, ISO 8317Flexural modulus, tensile elongation, child-resistance panelFailure strain 8–20 %
    Toy structural partsEN 71-3, ISO 8124-1Extractable metals migration, torque/tension abuse loadEN 71-3 Category III limits

    Toy structural components are injection moulded from HDPE ACP 6031D when EN 71-3 extractable-metal limits must be satisfied in scraped-off toy materials. Melt temperatures are kept at 190 °C to 220 °C to reduce odour and degradation in 80 t to 150 t machines; mould temperatures are 25 °C to 35 °C. Wall sections of 3 mm to 4 mm require a hold time of 6 s to 10 s and a cycle of 20 s to 30 s. The formulation contains 2 wt% to 4 wt% of heavy-metal-free colour masterbatch. Cold-runner sprues are granulated and returned up to 20 wt% after drying at 70 °C for 2 h. No slip or antistatic additives are used unless a migration test on the final article is performed. Notched Charpy impact is determined by ISO 179-1/1eA at 23 °C and -10 °C. Mechanical abuse-load testing follows ISO 8124-1 torque and tension methods. Extractable-metal compliance is documented per EN 71-3 Category III limits for scraped-off materials. The grade is not supplied with a toy-specific certificate, so the moulder is responsible for final-article compliance. Suitable terminal parts include structural housings, large play panels, and connector blocks.

    Glass Jar Overcap Formulations Require Lower Slip Addition Than Beverage Closures to Avoid Printing Defects

    Glass jar overcap shells are moulded from ACP 6031D with lower slip loadings because the exterior surface is printed or hot-stamped after moulding. The formulation uses 0.2 wt% to 0.4 wt% erucamide masterbatch, 1.0 wt% to 2.0 wt% white masterbatch, and no antistatic agent. In 8- to 16-cavity cold-runner tools, melt temperatures are 200 °C to 225 °C, mould temperatures 15 °C to 25 °C, and cycle times 10 s to 14 s. Gate vestige is placed on the inner top surface, away from the printed exterior. Ink adhesion is checked by tape peel after corona treatment at 38 mN/m to 42 mN/m surface tension. Dimensional stability is measured by ISO 294-4 shrinkage; lid ovality must remain below 0.3 mm on a 63 mm lug finish. Compliance includes EU 10/2011 where the overcap is used adjacent to food packaging and FDA 21 CFR 177.1520 for olefin polymers; because the overcap is not intended as a direct food-contact layer, barrier-specific migration testing is generally limited to the primary jar closure. Terminal articles are printed or hot-stamped overcaps for glass food jars and similar lug-style closures.

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    Certification & Compliance
    More Introduction

    Among high-density polyethylene film resins engineered for thin-gauge blown-film production, the grade designation LyondellBasell HDPE ACP 6031D identifies a Hostalen Advanced Cascade Process product based on a bimodal molecular weight architecture. The resin is typically specified where the converter must combine high melt strength, stable bubble geometry, and elevated film stiffness at gauges at or below 20 µm. The Hostalen ACP route uses a cascade polymerisation sequence that separates the low-molecular-weight and high-molecular-weight chain populations before homogenisation, creating a polymer with strain-hardening behaviour that differs from conventional unimodal HDPE film grades of similar density.

    Which Resin Specifications Are Referenced for ACP 6031D?

    The specification table below consolidates typical nominal values reported in technical data sheets under standardised test methods. These values are not production lot specifications and should be verified against the certificate of analysis for each delivered batch. Density is determined by ISO 1183-1:2019, and melt flow rate by ISO 1133-1:2022 under the stated load. The tensile properties cited here are obtained on compression-moulded plaques or film specimens depending on the supplier test protocol.

    Property Typical Value Test Method
    Density 0.960 g/cm³ ISO 1183-1:2019
    Melt flow rate at 190 °C/5.0 kg 0.30 g/10 min ISO 1133-1:2022
    Tensile stress at yield 30 MPa ISO 527-2/1B
    Tensile modulus 1150 MPa ISO 527-2/1A
    Nominal tensile strain at break >600% ISO 527-2/1A

    The density of 0.960 g/cm³ places ACP 6031D in the high-stiffness segment of HDPE film resins. The melt flow rate of 0.30 g/10 min at 190 °C and 5.0 kg reflects a high-molecular-weight material whose low-load melt flow rate should not be interpreted as an extrusion index. The bimodal molecular weight distribution reduces the usual trade-off between melt strength and shear thinning. The high-molecular-weight fraction contributes to strain hardening during bubble expansion, while the lower-molecular-weight fraction reduces viscosity in the high-shear die flow, enabling thin-gauge drawdown without the melt-pressure spikes observed in some unimodal high-density film resins.

    On a conventional grooved-feed single-screw blown-film line with an L/D ratio between 25:1 and 30:1, stable film production with ACP 6031D is typically achieved at melt temperatures from 200 °C to 220 °C. Die gaps between 0.8 mm and 1.2 mm and blow-up ratios from 3:1 to 4:1 are common starting points. The resin permits drawdown to gauges below 12 µm when the frost-line height is maintained above the point where the high-molecular-weight fraction reaches its strain-hardening plateau. Melt temperatures below 180 °C can increase melt pressure and produce melt fracture at high output rates, while temperatures above 230 °C may reduce bubble strength and increase thermally induced gel formation. Pre-drying is not normally required at ambient relative humidity below 60% RH because HDPE does not hydrolyse, but surface condensation should be avoided on cold resin entering the hopper.

    In production-scale experience with grooved-feed extruders, bubble instability appears first at the die edge when the die gap is too narrow for the selected blow-up ratio. Widening the die gap to 1.2 mm or reducing output by 5% to 10% generally restores a stable bubble. Published data for this specific configuration is limited because bubble stability is a function of ambient air movement, die design, stabiliser ring geometry, and downstream calibration. For that reason, process optimisation on a given line should be treated as equipment-specific rather than directly transferable from laboratory data.

    When a Converter Shifts from a Unimodal HDPE Film Resin to ACP 6031D

    When a conversion line replaces a unimodal HDPE film resin of comparable density with ACP 6031D, the primary rheological difference is the higher shear-thinning index produced by the bimodal architecture. At typical die shear rates, ACP 6031D flows more readily than a unimodal high-molecular-weight HDPE of equivalent low-load melt flow rate; after the die exit, its strain-hardening response is higher, allowing deeper drawdown and wider blow-up ratios without excessive thickness variation. Compared with lower-density HDPE film grades in the same supplier portfolio, ACP 6031D shifts the film property envelope toward higher modulus and increased tensile strength, while tear propagation and low-temperature impact resistance decline. The higher density reduces gas permeability on a thickness-normalised basis, but the same density increase limits use in freezer films where dart impact at -20 °C is the controlling specification under ISO 7765-1.

    The gel count requirements for ACP 6031D are normally tighter than those applied to conventional unimodal HDPE film resins intended for thicker sheet, because the grade is used in thin sections where gels appear as visible dimensional defects. In high-speed bag converting, gels larger than 150 µm can initiate film breakage at the sealing bars. Processors using automated optical inspection systems set alarm thresholds at the gel size agreed with the supplier. Published data for this specific configuration is limited; gel populations vary with extrusion cleanliness, residence-time distribution, screw design, and die head geometry. Metallocene-catalysed HDPE grades may offer lower extractables and higher clarity for specific applications, but ACP 6031D is selected when gauge reduction, melt strength, and stiffness dominate over optical clarity.

    Within the packaging sector, ACP 6031D is converted into high-strength T-shirt carrier bags, produce bags, and industrial liners where downgauging is economically decisive. The resin is also evaluated for direct food contact under FDA 21 CFR 177.1520 and EU Regulation No 10/2011; compliance is determined on the finished article, not the resin alone. Migration testing must be conducted on the final package because printing inks, laminating adhesives, and processing aids alter the overall migration profile.

    Operational limitations include control of melt residence time. At processing temperatures above 230 °C, extended hold-up in the die can generate high-molecular-weight gels through thermal degradation even in stabilised HDPE. Equipment with long adapters should use streamlined flow paths and avoid dead spaces. The grade is not recommended for applications requiring high clarity because HDPE films are inherently translucent; the density and crystalline content produce haze that cannot be eliminated by processing alone. No incompatibility with standard HDPE stabiliser packages is reported, but converters should verify additive dispersion because the high melt viscosity of ACP 6031D can affect distributive mixing in single-screw dry blending.

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