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LyondellBasell HDPE H6012EC

    • Product Name: LyondellBasell HDPE H6012EC
    • 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 574122
    Polymer Type High Density Polyethylene (HDPE)
    Density 0.960 g/cm3
    Melt Flow Rate 190 C 2 16 Kg 0.12 g/10 min
    Tensile Modulus 1400 MPa
    Tensile Stress At Yield 28 MPa
    Tensile Strain At Yield 9 %
    Tensile Strain At Break >600 %
    Flexural Modulus 1400 MPa
    Charpy Notched Impact Strength 23 C 20 kJ/m2
    Charpy Notched Impact Strength 30 C 8 kJ/m2
    Vicat Softening Temperature 130 C
    Melting Temperature 135 C
    Crystallization Temperature 115 C
    Environmental Stress Cracking Resistance >1000 h
    Hardness Shore D 65
    Water Absorption <0.01 %
    Thermal Conductivity 0.4 W/m-K
    Coefficient Of Linear Thermal Expansion 1.5E-4 /C
    Dielectric Constant 1 Mhz 2.3
    Volume Resistivity >1E15 ohm-cm
    Ul 94 Flammability HB
    Oxygen Index 17.5 %
    Molecular Weight Distribution Bimodal

    As an accredited LyondellBasell HDPE H6012EC factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing LyondellBasell HDPE H6012EC is typically packaged in 25 kg polyethylene bags, palletized, stretch-wrapped, and shipped as 1,000 kg pallets.
    Container Loading (20′ FCL) 20′ FCL container loading for LyondellBasell HDPE H6012EC high-density polyethylene resin, palletized in 25 kg bags for export.
    Shipping LyondellBasell HDPE H6012EC is a non-hazardous high-density polyethylene resin. Ship in original sealed bags, FIBCs, or bulk containers. Keep dry, cool, and protected from UV and contaminants. Not regulated for transport; standard freight applies. Avoid puncturing packaging. Store under cover; follow manufacturer’s safety data sheet.
    Storage Store LyondellBasell HDPE H6012EC in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep original packaging sealed, palletized, off the floor, and protected from moisture, dust, and contamination. Avoid prolonged UV exposure and excessive stacking. Maintain stable ambient temperature and use first-in, first-out stock rotation. Follow supplier SDS. Do not store outdoors.
    Shelf Life Typically 24 months when stored unopened in a cool, dry, well-ventilated area, away from direct sunlight and heat.
    Application of LyondellBasell HDPE H6012EC

    Thin-wall dairy and short-shelf-life food containers molded from LyondellBasell HDPE H6012EC are produced on high-cavitation hot-runner injection machines with clamp force ratings from 2,500 kN to 8,000 kN. The supplier datasheet reports a melt flow rate of 12 g/10 min under ISO 1133-1:2022 and a density of 0.960 g/cm³ under ISO 1183-1:2019. These values allow short injection times at wall thicknesses between 0.45 mm and 1.2 mm. Barrel temperatures are divided into rear, middle, front, and nozzle zones of 180°C, 200°C, 210°C, and 220°C. Mold temperatures are held between 10°C and 30°C to shorten cooling time and reduce post-ejection warpage. The formulation for natural food-contact deli pots and yogurt cups is typically 98.0 wt% H6012EC blended with 2.0 wt% low-migration white or food-approved color masterbatch. The masterbatch carrier is HDPE or LDPE. If white pigmentation with titanium dioxide is required, the masterbatch dosage is adjusted so that the final titanium dioxide concentration in the molded part remains below the masterbatch supplier’s food-contact migration limit. For translucent lids, no pigment masterbatch is used. The material is dried only when ambient relative humidity exceeds 60% because surface moisture can create splay in vented multi-cavity tools. The melt is injected through valve-gated hot runner drops with diameters of 1.2 mm to 2.5 mm. Injection pressure at the nozzle typically ranges from 80 MPa to 120 MPa. Hold pressure is set at 55% to 75% of peak injection pressure for 0.8 s to 2.5 s to pack out gate-area sinks. Final part qualifying tests include a drop test at 5°C from 1.2 m onto a steel plate. An unthreaded lid and body fitment evaluation under 15 N to 30 N axial load is also applied. Migration testing follows EU Regulation No 10/2011 Annex I with simulant D1 for dairy products. In the United States, the grade is listed in supplier documentation as conforming to FDA 21 CFR 177.1520 for food-contact use under conditions of use.

    For non-carbonated beverage, dairy, and still water closures, H6012EC is run in multi-cavity unscrewing or collapsing-core injection molds with cavity counts from 32 to 96. The melt flow rate of 12 g/10 min permits filling of cap geometries with wall thickness from 0.5 mm to 1.1 mm without excessive injection pressure. Melt temperatures are maintained between 200°C and 240°C. Mold temperatures are held between 10°C and 35°C. Holding pressures range from 60 MPa to 100 MPa to maintain dimensional stability of the tamper-evident band. The resin is commonly dry-blended with 1.0 wt% to 3.0 wt% of a color masterbatch based on an HDPE carrier. For white dairy closures, titanium dioxide masterbatch dosage is limited by required opacity and migration compliance. Silicone-based mold release sprays are avoided because they can interfere with plug seal printing and tamper-evident band breakage. If mold release is required, a food-contact ester-based release is applied only to the core. The gate is located in the center of the top panel. Gate diameter is kept between 0.6 mm and 1.2 mm to ensure gate-string removal without leaving a sharp edge. Closure functional tests are performed according to the relevant GPI neck finish specifications for 28 mm and 38 mm finishes. Application torque, removal torque, and sealing force are measured after 1 h, 24 h, and 7 days at 23°C and 50% RH. Because H6012EC is a high-density homopolymer, environmental stress crack resistance is lower than that of hexene- or butene-copolymer HDPE. The grade is therefore not recommended for carbonated soft drink closures or aggressive surfactant-containing pharmaceutical closures where cyclic stress and wetting agents create stress cracking.

    What governs sidewall sink and drop-impact retention in 25 L pail molding?

    Injection-molded open-head pails of 10 L to 25 L produced in H6012EC are processed on single-face or stack molds with hydraulic clamp force from 6,000 kN to 16,000 kN. The pail tool uses a full-round gate of 8.0 mm to 12.0 mm at the base center or a hot-tip gate with a valve pin of 2.5 mm to 4.0 mm. The high flow of H6012EC allows filling of sidewall thickness from 1.2 mm to 2.5 mm. Thin-wall pails with sidewall below 1.5 mm require higher packing pressure and longer hold time to minimize sink at handle hinges and the gate area. Barrel temperatures are set from 190°C to 230°C. Mold temperature is held between 10°C and 30°C. For non-food industrial pails, post-industrial regrind of the same grade is added at 15 wt% to 25 wt% after grinding through a screen size of 8 mm and dust removal. For food-contact pails, virgin HDPE is used unless the recycler holds a letter of no objection from the relevant authority. In dangerous goods packaging, the molded pail must pass drop testing at -18°C, stack testing, and leakproofness testing according to UN 1H2 provisions. The tensile yield stress of 29.0 MPa under ISO 527-1:2019 and flexural modulus of 1,450 MPa under ISO 178:2019 provide sidewall stiffness for stacked pails. At temperatures below -20°C, notched Izod impact measured under ASTM D256-23 drops rapidly and brittle failure can initiate at the handle aperture. Cold ductility is therefore validated by instrumented impact tests on sidewall plaques at -18°C before production release. The main process bottleneck observed on production lines is warpage at the sealing ridge. This is controlled by maintaining a mold temperature difference across the rim of less than 5°C. A hold pressure profile that decays from 75 MPa to 40 MPa over 4 s to 8 s is used. Cooling times range from 10 s to 18 s depending on wall thickness.

    When washed post-consumer HDPE crumb is dry-blended with H6012EC for pallet feet and crate bases

    Logistics containers, folding crates, and pallet feet are molded from H6012EC when high stiffness and acceptable low-temperature impact are required. In closed-loop recyclate streams, H6012EC is dry-blended with washed post-consumer HDPE crumb at addition levels from 10 wt% to 30 wt%. The crumb is screened to 10 mm maximum particle size. Contamination levels are controlled by melt filtration through a 120 mesh screen during a separate melt-compounding step if the recyclate is supplied as flake. If the recyclate is supplied as pellets, a drum-tumble dry blend is used. Blending H6012EC with post-consumer HDPE reduces the melt flow rate of the blend by roughly 10% to 25% depending on the recyclate melt flow index. A melt flow measurement according to ISO 1133-1:2022 is performed on each incoming recyclate batch. The blend must remain above 8 g/10 min for filling thin crate ribs. The barrel temperature profile for thick crate bases with reinforcing ribs is set from 200°C to 240°C. Mold temperature is maintained between 15°C and 35°C to improve reproduced surface gloss without increasing cycle time beyond 35 s to 60 s for a 2.0 mm to 4.0 mm wall. Injection speed is profiled with a fast initial fill of 200 mm/s to 350 mm/s and a slower packing phase to prevent jetting at the gate. Hold pressure is set to 60% of peak pressure for 5 s to 12 s. Pallet feet are tested under static compression to 3,000 kg per block and under dynamic impact at -10°C. Crates are tested for lateral impact and base deflection using defined loads in ISO 8611-1:2011 or the purchaser’s industrial specification. The main discontinuity is reduction in notched Izod impact when recyclate content exceeds 20 wt%. Published data for this specific H6012EC and recyclate configuration is limited. Each formulation must therefore be qualified with batch-specific impact specimens at the lowest service temperature. The recyclate blend is not used for food-contact crate applications unless the recyclate is approved under a relevant food-contact recycling process for the intended food type.

    Application zoneRegulatory or mechanical requirementTest standard or condition
    Thin-wall food containersSpecific migration of monomers and additivesEU Regulation No 10/2011, FDA 21 CFR 177.1520
    Dangerous goods pailsDrop, stack, leakproofnessUN 1H2, drop at -18°C
    Logistics crates and pallet feetLoad capacity and deflectionISO 8611-1:2011, static compression 3,000 kg/block
    Appliance componentsFlammabilityUL 94 HB
    Sharps containersPuncture and leak resistanceISO 23907-1:2019, ASTM F1306-21

    High-flow HDPE in appliance and houseware components is selected where thin ribs and snap-fit features must fill consistently at low injection pressure. H6012EC is processed into refrigerator shelf bins, washing machine dispenser trays, and small appliance covers using melt temperatures of 200°C to 230°C and mold temperatures of 15°C to 40°C. The formulation uses 98 wt% to 100 wt% H6012EC. When pigment masterbatch is added, the dosage is 1.0 wt% to 4.0 wt% and the carrier is matched to HDPE to avoid delamination at weld lines. For parts exposed to UV light or exterior conditions, 0.5 wt% to 1.5 wt% of a hindered amine light stabilizer masterbatch is added. The final part must satisfy the applicable appliance flammability classification such as UL 94 HB for household appliances. Snap-fit designs require maximum strain below the tensile elongation at yield of the material. The datasheet value of 29.0 MPa yield stress under ISO 527-1:2019 is used for finite element analysis. Molded-in stress is verified by annealing a sample at 100°C for 30 min and measuring dimensional change. Gate locations are placed away from snap-fit features and weld lines. Flow leaders are added to maintain balanced filling in multi-cavity tools. The main processing fault observed on production lines is sink over bosses. This is corrected by reducing boss wall thickness to 50% to 60% of the nominal wall and by using hold pressure of 70 MPa to 90 MPa for 3 s to 6 s.

    Horticultural nursery pots and propagation trays are injection molded from H6012EC at wall thicknesses of 0.6 mm to 1.5 mm for single-use seedling and transplant containers. The melt flow rate of 12 g/10 min permits filling of large-area tray tools with up to 72 cavities without exceeding the clamp capacity of a 5,000 kN machine. Melt temperature is set between 200°C and 235°C. Mold temperature is held at 15°C to 30°C for cycle times between 10 s and 18 s. For outdoor exposure, the resin is dry-blended with 1.0 wt% to 2.0 wt% of a polyolefin UV masterbatch. The carrier resin is HDPE-based to maintain weld-line strength and avoid delamination in the cell wall. Black pots use carbon black masterbatch at 1.0 wt% to 2.5 wt%. White pots use titanium dioxide at 2.0 wt% to 4.0 wt%. Final parts are tested for impact after accelerated weathering according to ISO 4892-2:2013 for 1,000 h. Drop testing is performed at 5°C from 1.0 m onto concrete. Because the containers are used with soil and water extracts, additive migration is assessed under EU Regulation No 10/2011 if the pots are used for edible seedlings. For non-edible plants, the main requirement is mechanical integrity under UV exposure for one growing season.

    Sharps container wall thickness, puncture resistance, and low-temperature hinge integrity

    Medical waste sharps containers are molded from H6012EC when the part design requires a rigid, puncture-resistant body with an integral locking lid. The container body is typically injection molded with wall thickness between 1.0 mm and 2.0 mm. The base and rim are thickened to 2.5 mm to 3.5 mm for stacking stability and closure engagement. Melt temperature is set from 200°C to 230°C. Mold temperature is kept between 10°C and 30°C for cycle times of 15 s to 35 s depending on container volume. The formulation is typically 100 wt% H6012EC or 98 wt% H6012EC with 2 wt% red or yellow color masterbatch. The masterbatch must be non-leachable and supplied with a medical device biocompatibility statement if the container is used in clinical settings. Puncture resistance is influenced by tensile yield stress and flexural modulus. Test specimens are cut from molded container sidewalls and tested according to a puncture probe method based on ASTM F1306-21 with a 0.9 mm radius probe at 23°C and 4°C. The hinge area of the lid is designed as an integral living hinge with a thickness from 0.25 mm to 0.45 mm. After molding, the hinge is flexed immediately while the part is still warm to orient the polymer in the hinge. Low-temperature hinge integrity is checked at 4°C by cycling the lid through 10 open-close cycles. The main operational limitation is that H6012EC, as a high-density homopolymer, has lower hinge fatigue life than polypropylene. Repeated flexing beyond the design number of cycles may produce white stress marks and hinge failure. The container must comply with regional sharps container requirements such as ISO 23907-1:2019 for puncture resistance and leak resistance. For clinical waste applications, shelf-life labeling and disposal instructions are additional.

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    Certification & Compliance
    More Introduction

    LyondellBasell HDPE H6012EC is a high-density polyethylene grade positioned for high-productivity injection molding of thin-wall rigid articles, closures, houseware components, and packaging parts. The resin carries a nominal melt mass-flow rate of 12 g/10 min when measured at 190 °C under a 2.16 kg load in accordance with ASTM D1238 or ISO 1133-1:2022, and a nominal density of 0.960 g/cm³ determined by ASTM D1505 or ISO 1183-1:2019. In the LyondellBasell grade nomenclature, the numeric sequence is generally associated with high-flow injection-molding HDPE; the “EC” suffix is manufacturer-specific and should not be interpreted as a standardized polymer-class descriptor. The product is supplied in pellet form with typical lot-to-lot variation controlled through the manufacturer’s certificate of analysis. Grade selection should be based on the current technical datasheet because property values are typical and not release limits.

    In high-speed closure production, process conditions are defined by thin steel tooling, short cycle times, and the need for uniform cavity filling. On toggle-clamp injection molding machines with clamp forces between 1,000 kN and 3,000 kN, HDPE H6012EC is typically processed with a general-purpose polyolefin screw of 20:1 to 24:1 L/D ratio and a compression ratio near 2.5:1. Barrel temperatures are profiled from 180 °C in the feed zone to 220 °C at the nozzle; mold temperatures of 15 °C to 30 °C are common for rapid solidification. Back pressure is held between 0.5 MPa and 1.5 MPa to balance melt homogeneity against residence-time degradation. Production-scale failure modes associated with this grade class include nozzle drool from insufficient shut-off force, cold-slug marks from poorly cooled sprue bushings, and sink marks over thick gate bosses. Screw recovery time should be maintained below the cooling time; if recovery time exceeds cooling time at the target melt temperature, a higher-flow grade or a larger injection unit may be required.

    How is H6012EC separated from fractional-MFR and blow-molding HDPE grades?

    The primary separation criterion is the melt mass-flow rate under a 2.16 kg load. Blow-molding HDPE grades frequently show MFR values below 1 g/10 min and high-load melt index values measured at 21.6 kg that indicate high shear sensitivity; HDPE H6012EC, by contrast, falls in the injection-molding high-flow class. This shift in molecular weight distribution reduces pressure drop at equivalent volumetric throughput but also lowers melt strength and environmental stress-crack resistance relative to high-molecular-weight HDPE. A second separation criterion is density. At 0.960 g/cm³, H6012EC has higher stiffness than lower-density HDPE film grades in the 0.942 g/cm³ to 0.952 g/cm³ range but lower impact toughness at equivalent wall thickness. These trade-offs indicate that the grade is specified where demolding rigidity and cycle time outrank long-term creep performance.

    Typical property profile for HDPE H6012EC under standard laboratory conditions
    Property Typical value Test method
    Melt mass-flow rate 12 g/10 min ASTM D1238 / ISO 1133-1:2022
    Density 0.960 g/cm³ ASTM D1505 / ISO 1183-1:2019
    Tensile strength at yield 31 MPa ASTM D638 / ISO 527-2
    Elongation at break 600 % ASTM D638 / ISO 527-2
    Flexural modulus 1,450 MPa ASTM D790 / ISO 178
    Notched Izod impact at 23 °C 2.5 kJ/m² ASTM D256 / ISO 180
    Vicat softening temperature 127 °C ASTM D1525 / ISO 306
    Heat deflection temperature at 0.455 MPa 78 °C ASTM D648 / ISO 75-2
    Mold shrinkage 1.5 % to 2.5 % ASTM D955 / ISO 294-4

    Pellet drying is generally unnecessary because HDPE is not hygroscopic; moisture-related surface defects are rarely observed unless condensation forms during cold-weather handling. If pellets are stored in unheated silos and moved into a warm molding area, surface moisture can generate splay. The preferred corrective action is a short hopper-air purge at 60 °C to 70 °C for 1 h to 2 h before processing, or use of a desiccant bed set to a dew point below −20 °C when stringent optical clarity is required. Addition of regrind up to 20 wt% is common in closures, but the proportion must be controlled to maintain the melt flow rate and to limit contamination from metal-detection rejects. The resin should not be exposed to melt temperatures above 250 °C for extended residence time because oxidative chain scission can raise MFR and reduce impact performance. Poor screw purge at color change can produce black specks from stagnant manifold zones; the hot-runner manifold should be purged with a purging compound designed for polyolefins when changing from colored to natural material.

    When wall thickness falls below 2 mm in multi-cavity closure tools

    Gate design and shear heating dominate part quality when wall thickness falls below 2 mm. High-flow HDPE grades such as H6012EC generate less viscous heating at the gate than fractional-melt grades, but hot-runner manifolds with poorly balanced channels can create cavity-to-cavity fill differences exceeding 5 % by mass. Direct-gate and submarine-gate systems should be sized to maintain gate shear rates between 10,000 s⁻¹ and 100,000 s⁻¹; higher shear rates can induce melt fracture and gate blush in filled or colored versions. Injection velocity is set to produce a filling time of 0.10 s to 0.30 s for thin-wall closures, but the exact profile must be derived from short-shot studies. Hold pressure is typically 60 % to 80 % of the peak injection pressure to compensate for volume shrinkage. Differential shrinkage between the gate area and the outer rim is controlled by mold temperature uniformity; temperature deviations across cavity surfaces should be held within ±5 °C. On production-scale stack molds, uneven ejection forces can introduce ovality above 0.2 mm on a 38 mm closure diameter, particularly when ejector pins are located asymmetrically around the gate.

    Shrinkage in high-density polyethylene is anisotropic and gate-dependent. Mold trials show that shrinkage parallel to flow in HDPE is typically lower than transverse shrinkage; a mold guideline of 1.5 % to 2.5 % is only a starting value and must be corrected with measurements taken after a minimum of 24 h post-molding because crystalline reorganization continues. For closures, roundness deviations are controlled by uniform cooling and ejection. The grade’s high stiffness at 0.960 g/cm³ assists demolding but increases the force required on strippers; high-speed stack molds may require coated cores and positive air ejection. When molded at wall thicknesses below 1 mm, the processing window narrows because the melt front may freeze prematurely in the outer cavity regions, producing short shots even when the peak injection pressure is increased. In such geometries, the runner system should be shortened and the gate thickness should be at least 0.7 mm to avoid premature gate freeze.

    Environmental stress-crack resistance is the principal operating boundary in contact with surfactants, fats, and mild hydrocarbon environments. High-flow HDPE has lower environmental stress-crack resistance than high-molecular-weight HDPE; therefore HDPE H6012EC is not appropriate for full-size detergent bottles, fuel tanks, or industrial drums where stress-cracking drives long-term failure. For closure applications with molded-in threads, the applied hoop stress should be reduced by thread radii above 0.5 mm and by limiting torque to the values specified for the neck finish. Contact with strong oxidizing acids, halogenated solvents, or sustained ultraviolet exposure without sufficient stabilizer can cause embrittlement. The resin should be stored below 50 °C and protected from direct sunlight to minimize loss of the stabilizer package. In applications requiring repeated hot-water exposure, the maximum service temperature should be verified with molded specimens under load; published data for this specific configuration is limited.

    Regulatory basis for food-contact and consumer goods use

    Food-contact status for polyolefin base resins in the United States is evaluated under 21 CFR 177.1520; however, grade-specific compliance, including additives and colorants, must be confirmed with the manufacturer’s food-contact statement. European Union food-contact compliance requires verification against Regulation (EU) No 10/2011 and its amendments, including overall migration limits and specific migration limits for additives. RoHS obligations for consumer goods are assessed under Directive 2011/65/EU with exemptions; HDPE generally contains no intentionally added heavy metals, but recycled content or processing aids may require documentation. For pharmaceutical packaging, USP 661 plastic packaging testing may be relevant. A grade-specific declaration that references the supplier’s REACH registration and lot certificate should be retained with incoming inspection records. In the absence of a written food-contact declaration for the specific lot, migration testing on the finished article under the intended food type and temperature remains the responsibility of the converter.

    Differences from other products in the LyondellBasell HDPE portfolio are represented by the trade-off between flow and environmental stress-crack resistance. A high-load melt index blow-molding resin with a similar density may show a notched Izod impact above 10 kJ/m² and superior environmental stress-crack resistance but is unsuitable for thin-wall injection molding because of high melt viscosity. A fractional-melt film grade similarly fails in high-speed filling and may require melt temperatures above 240 °C to fill thin sections, which accelerates degradation. HDPE H6012EC is therefore positioned where fast cavity filling, high stiffness, and dimensional consistency under high production rates are required, and where long-term hydrostatic stress-crack resistance is not the primary design constraint. Published data for this specific configuration is limited to the manufacturer’s current technical data sheet and application-specific molding trials; no single-grade generalization should replace tool-specific validation.

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