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LG Chem HDPE ME8000

    • Product Name: LG Chem HDPE ME8000
    • 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 237931
    Density 0.954 g/cm³
    Melt Index 190 C 2 16 Kg 0.8 g/10 min
    Tensile Strength At Yield 27 MPa
    Tensile Strength At Break 30 MPa
    Elongation At Break >600%
    Flexural Modulus 1200 MPa
    Vicat Softening Point 125°C
    Heat Deflection Temperature 75°C
    Shore D Hardness 66
    Environmental Stress Crack Resistance >1000 h
    Notched Izod Impact Strength 50 J/m
    Melting Point 132°C
    Brittleness Temperature < -70°C

    As an accredited LG Chem HDPE ME8000 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing LG Chem HDPE ME8000 is typically supplied in 25 kg bags, palletized and shrink-wrapped, or 1,000 kg jumbo bags.
    Container Loading (20′ FCL) 20′ FCL container loading: 25 kg bags, 20 pallets, 20 MT net weight, LG Chem HDPE ME8000, palletized and shrink-wrapped.
    Shipping LG Chem HDPE ME8000 is a non-hazardous high-density polyethylene supplied as pellets in 25 kg bags, palletized and stretch-wrapped. Ship in clean, dry trucks or containers at ambient temperature, avoiding moisture, direct sunlight, heat, and contamination. No special hazardous shipping classification applies; handle with standard industrial care.
    Storage Store LG Chem HDPE ME8000 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, sparks, flames, and strong oxidizers. Keep original bags or containers closed, clean, dry, and palletized. Prevent moisture, dust, and contamination. Avoid prolonged UV exposure and extreme temperatures. Do not exceed recommended stack heights. Follow local regulations and the manufacturer’s SDS.
    Shelf Life LG Chem HDPE ME8000 shelf life approximately 24 months in original packaging, stored cool, dry, and protected from direct sunlight.
    Application of LG Chem HDPE ME8000

    At a nominal melt flow rate of 8.0 g/10 min (190 °C, 2.16 kg, ASTM D1238) and a density of 0.956 g/cm³ (ASTM D1505), the material is introduced into injection and compression closure lines where neck finish dimensions control the final seal integrity. Food-contact use is supported by FDA 21 CFR §177.1520 and Regulation (EU) No 10/2011; the latter imposes an overall migration limit of 10 mg/dm² for plastics intended to contact aqueous and low-alcohol foods. Colour is metered as PE carrier masterbatch at 1.0–2.5 wt%, and slip agent addition is restricted to 0.05–0.15 wt% erucamide when removal torque on 28 mm PCO 1881 necks must remain between 0.8–1.2 N·m. On production machines with 32 to 96 closure cavities, barrel zones are held between 200 °C and 235 °C, the cooling circuit is set at 8 °C to 15 °C, and clamp force is specified from 2,000 kN to 3,500 kN. Screws with L/D 20:1–24:1 and compression ratios of 2.0:1–2.5:1 are used; residence time below 4 min is maintained to limit oxidative odour in water and dairy applications. The holding phase is executed at 400–700 bar through valve-gated hot runners, while injection speed is set to fill the cavity in 0.08–0.20 s. Production-scale bottlenecks appear as cavity-to-cavity weight variation when back pressure drops below 5 bar or when decompression exceeds 3 mm; premature gate freezing occurs when the gate diameter falls below 0.8 mm. Cavity-to-cavity mass variation is held within ±0.25% when screw recovery time remains between 4 s and 8 s; screw and barrel wear that increases clearance beyond 0.15 mm introduces unmelts in the gate region. Terminal articles include still-water closures, carbonated-soft-drink closures up to 38 mm, dairy blanks, creamer caps, and pharmaceutical push-and-twist closures where USP <661.1> or Ph. Eur. 3.1.3 is applied.

    What Happens to Low-Temperature Drop Impact When Regrind in Folding Crates Exceeds 30 wt%?

    Returnable logistics systems impose simultaneous load-bearing and ultraviolet exposure cycles that a fractional-melt HDPE cannot satisfy without a higher flow formulation. The grade is processed into collapsible crates and trays with wall sections from 2.0 mm to 4.0 mm on injection moulding machines with clamp force 8,000 kN to 12,000 kN. Barrel profiles from 200 °C to 235 °C and tool temperatures from 10 °C to 25 °C are used; screw L/D is 20:1–24:1, and pack pressure of 450–650 bar is held for 6–12 s at the gate. Clean post-industrial regrind is added at 10–30 wt%, with UV stabiliser masterbatch at 0.2–0.5 wt% for outdoor service and colour masterbatch at 1–3 wt%. The relevant packaging compliance is Directive 94/62/EC with a sum of lead, cadmium, mercury, and hexavalent chromium not exceeding 100 ppm; produce-contact crates are assessed under Regulation (EU) No 10/2011 and FDA 21 CFR §177.1520. Drop impact is evaluated by ASTM D5276 after conditioning at -20 °C for 24 h, and notched Izod values are measured under ASTM D256 at 23 °C and -20 °C. When regrind content rises from 10 wt% to 30 wt%, low-temperature impact energy declines; if weld lines form at handle bosses or rib junctions, the drop failure rate can increase under repeated 1.2 m free-fall impacts. Published data for this specific configuration is limited, so site-specific ASTM D256 screening of each regrind lot is performed before approval. Ultraviolet degradation is monitored through retained tensile elongation under ASTM D638 after accelerated weathering; batch release requires notched Izod energy at -20 °C to remain above the article-specific drawing limit. Terminal article types include ventilated produce crates, bakery trays, collapsible logistics boxes, and returnable automotive dunnage trays.

    UN 1H2 Pails With 1.2 mm Minimum Wall and Injection Gate Frosting

    Open-top pails of 10 L to 25 L are injection moulded on lines where cycle time is governed by cooling of the 1.2 mm wall rather than by material flow. The grade is regulated as a packaging material for dangerous goods under UN 1H2; certification requires closure integrity after free-fall drop from 1.2 m, stack performance for 28 days at 40 °C, and hydraulic pressure retention as specified in the ADR/RID/IMDG modal provisions. Food-grade pails additionally require Regulation (EU) No 10/2011 and FDA 21 CFR §177.1520. Formulation adjustments are limited to PE carrier colour masterbatch at 2.0–3.0 wt% and UV stabiliser masterbatch at 0.2–0.5 wt% for exterior storage; calcium carbonate fillers are avoided because they reduce weld-line strength and cause gate frosting. On injection moulding machines with clamp force 6,000 kN to 10,000 kN, melt temperatures from 200 °C to 230 °C, tool temperatures from 12 °C to 25 °C, and cushion control from 3 mm to 6 mm are maintained. Hot-runner valve gates or direct sprue gates are used; gate diameter below 2.0 mm at the pail base produces turbulence and visible flow haze. Total cycle time is 30–50 s for 20 L pails, with holding pressure 350–550 bar applied for 5–10 s. Warpage at demoulding is controlled by core temperature differentials not exceeding ±5 °C. Terminal products are open-top pails for lubricants, paints, inks, water-based cleaning concentrates, and food ingredients; the grade is not specified for high-permeation solvents such as xylene without additional fluorinated surface treatment.

    Regulatory and test method matrix by terminal article
    Terminal articleRegulation or standardCritical clause or test designationCondition or numeric limit
    Beverage and pharma closuresFDA 21 CFR §177.1520; Regulation (EU) No 10/2011; USP <661.1>Overall migration10 mg/dm²
    Returnable cratesDirective 94/62/EC; ASTM D5276; ASTM D256Heavy metal sum; drop; impact100 ppm; -20 °C
    UN pailsUN 1H2; ADR/RID/IMDG; ASTM D1238Drop, stack, hydraulic1.2 m; 28 days; 40 °C
    Dairy containersRegulation (EU) No 10/2011; FDA 21 CFR §177.1520Specific migration; overall migration10 mg/dm²
    Detergent-stressed containersASTM D1693Condition A50 °C; 100% Igepal CO-630
    Toys and leisureEN 71-3; EU 10/2011; REACH Annex XVII entry 51Migration of elements; phthalate absenceElement-specific limits

    Where wall thickness drops below 1 mm in dairy portion packs, the filling stage must complete before the flow front solidifies. The grade is processed on thin-wall injection moulding machines with clamp force 3,500 kN to 5,000 kN, screw L/D 22:1, and compression ratio 2.0:1–2.3:1. Barrel zones are set from 210 °C to 240 °C; mould temperature is held at 10 °C to 18 °C. The filling phase is executed in 0.12–0.25 s, followed by holding pressure 250–450 bar for 0.6–1.2 s. Colour masterbatch is metered at 2.0–3.0 wt%, and slip/antiblock addition is limited to 500–1,500 ppm to avoid seal-line fractures on filling machines. Food-contact compliance requires Regulation (EU) No 10/2011 with specific migration limits in Annex II and FDA 21 CFR §177.1520; overall migration must remain below 10 mg/dm². Drying at 80 °C for 2 h is used only when condensed surface moisture is present after storage below 5 °C at relative humidity above 60%. If melt temperature falls below 205 °C, short shots occur at the rim; above 245 °C, oxidative odour develops in fat-containing dairy matrices. Terminal articles include margarine tubs, ice-cream containers, portion packs, and thin lids; the grade is not used for retort or UHT treatments above 121 °C because seal contact pressure fails under thermal expansion.

    When ESCR Measured by ASTM D1693 Condition A Falls Below 10 h in Detergent-Stressed Storage Containers

    Detergent-stressed storage containers expose a low molecular weight distribution resin to simultaneous environmental stress cracking and constant load. The test method ASTM D1693 condition A is applied at 50 °C in 100% Igepal CO-630; article-specific acceptance values are derived from the creep rupture curve, and a measured value below 10 h triggers batch review when the container is intended for continuous contact with household cleaning formulations. The grade is processed into storage boxes with wall thickness 1.5–2.5 mm on injection moulding machines with clamp force 4,000 kN to 7,000 kN. Melt temperature is maintained from 200 °C to 230 °C, tool temperature from 15 °C to 30 °C, and holding pressure at 400–600 bar for 4–8 s. PE carrier colour masterbatch is added at 1–3 wt%; no external plasticiser or mould-release oil is used because both reduce ESCR at thick corners. Food-storage grades are assessed under Regulation (EU) No 10/2011 and FDA 21 CFR §177.1520; REACH SVHC candidate-list screening is performed on the formulated compound. The operational boundary is set at continuous contact with linear alkylbenzene sulphonate concentrations above 10 wt% at 50 °C without site-specific notch testing; published data for this specific configuration is limited. Terminal articles include kitchen drawer units, refrigerator bins, detergent dosing housings, and under-bed storage boxes.

    Because toy and leisure components are certified on the finished article rather than on raw resin alone, the grade is processed with controlled pigmentation and no external plasticiser. Colour masterbatch is added at 2–5 wt%; UV stabiliser masterbatch at 0.2–0.5 wt% is used only for outdoor sports articles. Melt temperature is set from 190 °C to 230 °C, tool temperature from 10 °C to 30 °C, and clamp force from 1,800 kN to 4,000 kN. Screw L/D 20:1–22:1 and back pressure 5–10 bar are used to maintain colour dispersion. Compliance for the final article includes EN 71-3 migration of elements, REACH Annex XVII entry 51 for phthalate restriction, and Regulation (EU) No 10/2011 where mouth-contact parts are included. FDA 21 CFR §177.1520 applies to US toy articles that may contact food during play. Weld lines at thick bosses are a critical failure mode; injection speed is profiled to keep flow-front temperature above 180 °C at weld convergence. Terminal articles include stacking blocks, outdoor sports cones, and hobby storage components; the grade is not specified for structurally load-bearing playground equipment without additional mechanical testing.

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    Certification & Compliance
    More Introduction

    LG Chem HDPE ME8000 is an injection moulding grade of high-density polyethylene in the LUTENE-H series. The grade is specified at a melt-flow index of 8.0 g/10 min under 190 °C and 2.16 kg load (ISO 1133-1:2022) and a density of 0.957 g/cm³ (ISO 1183-1:2019). This combination places the material in the intermediate-flow HDPE injection moulding segment, balancing injection-pressure demand against top-load resistance and environmental stress-cracking resistance for closures, overcaps, pails, and thin-wall housewares.

    Typical mechanical, thermal, and rheological values derived from injection-moulded specimens are listed below. These values are not contractual specifications; lot release is governed by the manufacturer’s certificate of analysis and should be checked for the specific production lot.

    PropertyTest MethodTypical Value
    Melt-flow index, 190 °C, 2.16 kgISO 1133-1:20228.0 g/10 min
    DensityISO 1183-1:20190.957 g/cm³
    Tensile yield stressISO 527-2:201226 MPa
    Tensile elongation at breakISO 527-2:2012>300%
    Flexural modulusISO 178:20191000 MPa
    Notched Charpy impact, 23 °CISO 179-1/1eA:20104.0 kJ/m²
    Shore D hardnessISO 868:200363
    Vicat softening temperature, A50ISO 306:2022123 °C
    Melting temperature by DSCISO 11357-3:2018131 °C

    Tensile yield stress of 26 MPa and flexural modulus of 1000 MPa define a stiffening behaviour consistent with this density class. The notched Charpy impact value of 4.0 kJ/m² at 23 °C indicates ductile behaviour in slow tensile loading but not exceptional toughness at sub-zero temperatures; low-temperature impact should be measured separately under ISO 179-1/1eA:2010 at the intended service temperature if frozen-food or outdoor use is anticipated.

    What Processing Boundaries Apply During High-Shear Injection Moulding?

    During injection moulding, the melt temperature measured at the nozzle is typically held between 190 °C and 230 °C. Barrel zones are profiled from 180 °C behind the feed throat to 220 °C at the metering section; a flat or reverse temperature profile should be avoided because HDPE of this melt-flow class can develop screw slip in the feed section when the rear zone is above 200 °C. Mould surface temperature is maintained between 10 °C and 40 °C, depending on wall thickness and required gloss. Lower mould temperatures reduce cycle time but increase frozen-in molecular orientation; higher mould temperatures above 40 °C increase gate-seal time and can extend total cycle time by 10% or more on hydraulic toggle machines.

    Injection speed is set to achieve cavity fill in 0.5–1.5 s for closure geometries with wall sections of 1.0–1.5 mm. Fill times below 0.3 s can produce jetting and surface flow marks, particularly with pinpoint gating; fill times above 2.0 s tend to freeze the flow front prematurely in multi-cavity layouts. Hold pressure is usually set between 50 MPa and 80 MPa hydraulic reading, adjusted to gate-seal detection by cavity pressure transducers rather than by fixed clock time. Screw recovery should be completed within 60–80% of the cooling time to avoid starving the next cycle.

    Residence time at melt temperature 220 °C should not exceed 10 min continuously. Longer residence can shift the melt-flow index, generate oxidized gels, and discolour the melt. During production interruptions, the barrel should be purged with a fractional-melt HDPE or a thermally stable polypropylene purge compound. Equipment with general-purpose screws of 20:1 to 24:1 L/D and compression ratios between 2.5:1 and 3.5:1 is commonly used; mixing screws with intensive shear sections are not required for this grade.

    Gate design for ME8000 follows standard hot-tip or pin-gating practice for HDPE. For closure shell weights between 3 g and 10 g, gate diameter is typically 0.8–1.2 mm and land length below 1.0 mm. The runner system should be volumetrically balanced within 5% across cavities; unbalanced layouts on multi-cavity tooling can produce inter-cavity weight variation above 3%. Hot-runner nozzle temperature is maintained at 200–220 °C, with valve-gate pin actuation completed by 0.1 s before fill completion to prevent stringing. Cooling-channel design should target a minimum Reynolds number of 10,000, using water at 10–20 °C; conformal cooling near the gate reduces cycle time, but published data specific to ME8000 cooling gains is limited.

    Pre-drying is normally unnecessary when granulate is stored in sealed packaging below 60% relative humidity. If surface moisture above 0.01 wt% is suspected, a desiccant dryer at 80 °C for 2–4 h is applied. Oven drying above 90 °C or for more than 4 h has been associated with granule agglomeration and should be avoided.

    Warpage, Frozen-In Stress, and Dimensional Stability in Thin-Wall Parts

    Thin-wall closure geometries moulded from ME8000 develop anisotropic shrinkage after demoulding. Mould shrinkage measured on 60 mm × 60 mm × 2 mm plaques according to ISO 294-4:2018 is typically in the range of 1.5–2.0% parallel to flow and 1.5–2.0% perpendicular to flow after 24 h at 23 °C; published data for this specific configuration is limited, and values from complex multi-cavity parts will differ. Differential shrinkage is the principal source of out-of-plane warpage in closures with variable wall thickness.

    Frozen-in stress can be reduced by maintaining cavity surface temperature variation within ±5 °C across the mould, by using balanced runner layouts, and by setting hold time to gate-seal rather than by fixed clock time. If cavity pressure at end of hold falls below 20 MPa, sink marks and post-mould dimensional movement increase. A post-mould conditioning step at 60 °C for 1 h may be used to relax residual stress in critical dimensions; published data for ME8000 annealing cycles is limited. Parts should be stored on flat surfaces for 24–48 h before metrological inspection because immediate post-mould measurements can vary by up to 0.3% due to post-crystallization.

    For EU food-contact articles, the finished article must comply with Commission Regulation (EU) No 10/2011 and national implementing measures. High-density polyethylene homopolymer may be permitted under FDA 21 CFR 177.1520(c) for certain food types and use conditions, but converter validation is required. Overall migration testing should follow EN 1186-1:2002 or equivalent. For toys and childcare articles, elemental migration under EN 71-3 is separately required. Regulatory declarations for REACH SVHC and RoHS 2011/65/EU Annex II should be obtained from the raw-material supplier and retained with batch traceability records. The grade is not intended for medical implants, pharmaceutical primary packaging, or long-term fuel contact; separate validation is required.

    When Wall Thickness Falls Below 0.8 mm, Higher-Flow Grades May Replace ME8000

    At wall sections below 0.8 mm, an 8.0 g/10 min melt-flow index can require injection speeds above 200 mm/s on reciprocating-screw machines and can generate gate pressure drop exceeding 80 MPa; under those conditions higher-flow HDPE grades with melt-flow indices above 15 g/10 min may be selected to prevent short shots. The tradeoff is lower notched impact and, in some geometries, lower top-load retention after accelerated aging.

    At wall sections above 3.0 mm, ME8000 can exhibit deeper sink marks than a lower-flow grade with melt-flow index below 6.0 g/10 min because the lower molecular weight reduces extensional viscosity during packing. For deep-draw containers and thick-walled pails, lower-flow grades or high-molecular-weight HDPE are preferred when top-load and drop impact take precedence over injection-pressure economy. Selection should be validated by rheological measurement under ISO 11443:2021 and by spiral-flow or actual tooling trials; published data for this specific configuration is limited.

    Compared with lower-flow grades of the same density, ME8000 exhibits lower melt viscosity at 190 °C and shear rates from 100 s⁻¹ to 1,000 s⁻¹, which translates to reduced hydraulic pressure on injection units. The corresponding reduction in slow-crack-growth resistance can be assessed by notched constant tensile load under ASTM F2136 or full-notch creep under ISO 16770:2004. For continuous pressure piping, a PE100-class pipe grade must be specified instead; ME8000 is not a pressure-pipe material.

    ME8000 is incompatible with strong oxidizing acids, aromatic hydrocarbons, and chlorinated solvents at elevated temperature; prolonged contact can cause swelling, stress cracking, and loss of mechanical integrity. The material should not be processed in equipment that previously ran PVC or PET without full purging, because thermally degraded residues can catalyse HDPE chain scission. Mechanical recycling of post-industrial scrap is possible only after regrind is dried and screened to remove fines below 0.5 mm; regrind addition should not exceed 20 wt% in critical applications unless validated on the target tooling.

    Outdoor weathering of unpigmented ME8000 is limited; UV stabilization with carbon black or a hindered amine light stabilizer is required if the part is exposed to direct sunlight. Natural parts stored for longer than 6 months in direct sunlight should be tested for surface carbonyl index by ASTM D5576 before use.

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