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North Huajin (Liaoning) HDPE HD5010EA

    • Product Name: North Huajin (Liaoning) HDPE HD5010EA
    • 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 205735
    Density 0.950 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 10 g/10 min
    Tensile Strength At Yield 24 MPa
    Tensile Strength At Break 28 MPa
    Elongation At Break 500%
    Flexural Modulus 1100 MPa
    Izod Notched Impact Strength 23 C 50 J/m
    Vicat Softening Temperature 124 °C
    Heat Deflection Temperature 0 45 Mpa 75 °C
    Shore D Hardness 62
    Mold Shrinkage 1.5-3.0%
    Water Absorption 24 H <0.01%
    Volume Resistivity >10^16 Ω·cm
    Dielectric Constant 1 Mhz 2.3
    Dielectric Loss Tangent 1 Mhz <5×10^-4
    Brittleness Temperature -70 °C
    Melting Point 130-135 °C
    Environmental Stress Crack Resistance F50 >1000 h

    As an accredited North Huajin (Liaoning) HDPE HD5010EA factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing North Huajin (Liaoning) HDPE HD5010EA is supplied in 25 kg woven bags, with 1000 kg jumbo bags available.
    Container Loading (20′ FCL) North Huajin (Liaoning) HDPE HD5010EA loaded in 20′ FCL: 25kg bags, 25MT without pallets or 18MT palletized.
    Shipping North Huajin (Liaoning) HDPE HD5010EA is a non-hazardous polyethylene resin, typically shipped in 25 kg woven bags or 1,000 kg jumbo bags, palletized and stretch-wrapped. It is not regulated for transport. Ship by truck, rail, or sea in clean, dry containers; store away from heat, moisture, and direct sunlight.
    Storage Store North Huajin (Liaoning) HDPE HD5010EA in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, and ignition sources. Keep original bags or containers closed to prevent moisture, dust, and contamination. Avoid prolonged UV exposure and contact with strong oxidizers. Stack securely to prevent collapse. Follow local regulations and the supplier’s safety data sheet.
    Shelf Life North Huajin (Liaoning) HDPE HD5010EA has a shelf life of 2 years when stored cool, dry, ventilated, away from direct sunlight.
    Application of North Huajin (Liaoning) HDPE HD5010EA
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    In thin-wall food packaging lines running cycle times below 6 seconds and cavity wall sections of 0.45 mm to 0.80 mm, HD5010EA is processed at a melt temperature of 190°C to 220°C and a mould coolant inlet temperature of 8°C to 18°C. The grade’s nominal melt flow rate of 10 g/10 min under ISO 1133-1:2022 at 190°C with a 2.16 kg load and density of 0.950 g/cm³ under ISO 1183-1:2019 define the pressure-loss profile in multi-cavity stack tooling with clamp forces from 8,000 kN to 30,000 kN. Field data from high-cavitation lines indicate that a ±1.5°C shift in hot runner tip temperature can alter part mass by 0.8–1.2%, which is sufficient to create lid-seal interference on containers with a 0.35 mm peripheral sealing land. The processing window at the recommended melt temperature is bounded at the upper limit by oxidation gel formation after 15 minutes at 230°C, observed as black specks on extrudate in the plant gel-count procedure, and at the lower limit by short shots in 0.50 mm flow lengths when the material remains below 185°C during the fill stage.

    The food-contact qualification for this application is governed by overlapping regulatory frameworks rather than a single standard. The matrix below summarizes the minimum compliance set.

    JurisdictionStandard or regulationTest method / acceptance limitApplication relevance
    United StatesFDA 21 CFR 177.1520(c)3.1aOlefin polymer density not less than 0.94 g/cm³; end-use extraction under 21 CFR 177.1520(d)High-density polyethylene for single-use and repeated-use food containers
    European UnionEU No 10/2011, Annex I and Annex IIOverall migration limit 10 mg/dm² using EN 1186-1:2002 and EN 1186-3:2002Dairy, delicatessen, and fruit packaging contact
    ChinaGB 4806.7-2023Total migration limit 10 mg/dm²; additives limited by positive listDomestic and imported food-contact HDPE articles

    Typical formulation for thin-wall dairy and deli container moulding uses HD5010EA as the continuous phase at 95–100 phr, with 0–20 phr clean in-house regrind, 2–4 phr food-contact-approved polyolefin colour masterbatch, and 0.05–0.15 phr fluoropolymer processing aid where shear-induced melt fracture appears on valve-gate witness marks. Slip and antiblock additives are held below 0.10 phr or omitted because migration to the sealing land can reduce lid adhesion in ultrasonic or heat-seal applications. In-mould labelling formulations may contain 5–15 wt% regrind, but reject fractions above 20 wt% are avoided to limit gloss variation and inconsistent label fusion at the cavity surface.

    Downstream manufacturing uses high-speed two-platen or toggle injection machines with screw L/D of 22:1 to 25:1 and compression ratio of 2.0:1 to 2.5:1. The plasticating unit is operated with back pressure 0.5–2.0 MPa, screw surface speed 20–40 m/min, decompression 3–6 mm before rotation stop, and cushion 2–5 mm to maintain a holding-pressure band of 30–60 MPa. Terminal product types include injection-moulded dairy cups, margarine tubs, deli and meal-prep containers, and fruit trays with wall sections between 0.45 mm and 1.00 mm; these parts are typically sealed with polyester or aluminium lidding film after corona treatment of the sealing land to 38–46 dyn/cm.

    At What Wall Thickness Does HD5010EA Fall Below a 12-Second Cycle in Cylindrical Pail Moulding?

    The transition from a 2.0 mm sidewall to a 2.8 mm sidewall in a 20 L open-head pail changes packing time from 4.0 s to 7.5 s and moves total cycle from 11.2 s to 14.8 s on a 35,000 kN accumulator-assisted injection machine with tiebar spacing of 1,200 mm × 1,200 mm. This threshold is observed in production where the gate freezes before the sidewall centreline reaches 120°C under mould coolant at 15°C. HD5010EA’s high-flow profile reduces filling pressure in a three-plate cold-runner pail tool with a 700 g shot weight and a 5.0 mm diameter side gate, but the limited melt strength at high flow can produce jetting if injection speed exceeds 250 mm/s at the gate.

    Pail formulations for industrial paints, building chemicals, and lubricants start from 100 phr HD5010EA, with 2–3 phr universal masterbatch, 0.1–0.3 phr hindered amine light stabilizer where outdoor storage exceeds 6 months, and 0.05–0.15 phr process stabilizer. Sprue and rejected pails are granulated and returned at 20–40 wt%; higher regrind fractions are permitted only when the cargo is non-food and the end user accepts a widening of Charpy notched impact at -20°C from 5 kJ/m² to 3 kJ/m² in a second-generation control lot. The terminal parts are 5 L to 25 L open-head pails and tapered buckets used for water-based coatings, adhesives, and construction chemicals; they are tested for leakproofness and stacking creep at 40°C for 28 days under 80 kg static top load.

    Where pails are filled with UN-regulated liquids, the completed package is qualified as 1H2 under the applicable UN dangerous goods transport procedure, with leakproofness and drop testing at 1.2 m on closures. The resin itself does not confer UN certification but must maintain sidewall impact integrity at -18°C after a 24 h conditioning soak.

    On high-cavitation closure moulding cells equipped with valve-gated hot runners and cold runner drops from 32 to 96 cavities, HD5010EA is processed at a melt temperature of 200–235°C, a mould coolant inlet temperature of 10–20°C, and a holding pressure of 35–65 MPa. The screw L/D is usually 20:1 to 24:1, with a compression ratio of 2.2:1 to 2.8:1 to avoid pellet slippage with the low coefficient of friction of high-flow HDPE. The centre-gated cap geometry dictates that hold time must be terminated before the 1.2 mm annular gate freezes, otherwise the part weight difference between hot-cycle and cold-cycle cavities exceeds 0.02 g and removal torque variation rises above 0.15 N·m.

    The following parameter bounds are used on 48-cavity valve-gated closure moulds to maintain dimensional stability across a production run.

    ParameterLower boundCentre setpointUpper boundDeviation outside bounds
    Melt temperature200°C220°C235°CAbove: odour and migration risk; below: gate-stringing and short shots
    Hot runner tip temperature210°C230°C250°CAbove: neck discolouration; below: cold gate hesitation
    Holding pressure30 MPa50 MPa70 MPaAbove: parting-line flash; below: sink at sealing plugs
    Cycle time3.5 s5.5 s8.0 sBelow: insufficient pack; above: economic penalty

    Closure formulations use 100 phr HD5010EA with 1–3 phr colour masterbatch, 0.05–0.20 phr primary antioxidant, and 0.1–0.3 phr erucamide slip concentrate when the customer removal torque target is below 1.0 N·m on a 28 mm PCO 1881 neck finish. For food-contact dairy closures, the formulation must stay inside the positive-list limits of EU No 10/2011 and FDA 21 CFR 177.1520; plant organoleptic panels test cap taint with 1 L of water exposed for 10 days at 40°C using a trained panel under EN 1622:2006 or equivalent sensory methods. Terminal product types are screw caps, snap-on lids, tamper-evident caps, and child-resistant closures where child-resistant functionality is validated under ISO 8317:2015.

    Logistics Crate Moulding Under Low-Temperature Impact and Returnable Packaging Loads

    At mould temperatures above 20°C, the relationship between low-temperature drop impact and moulded-in stress in a returnable bottle crate becomes visible when crates are conditioned for 24 h at -18°C and impacted on the bottom corner; cracks initiate at gate weld lines rather than through unoriented skin layers. HD5010EA in crates is processed at melt temperatures of 200–240°C and mould coolant temperatures of 20–40°C on large two-platen machines with clamp force from 8,000 kN to 30,000 kN. Shot weights for a 1,200 mm × 1,000 mm dairy crate are in the range of 2.2–2.8 kg, requiring a screw diameter of 110–140 mm to keep injection speed in the 80–150 mm/s window.

    The compliance matrix for reusable packaging focuses on packaging waste and heavy-metal restrictions: EU 94/62/EC Article 11 limits the sum of lead, cadmium, mercury, and hexavalent chromium to 100 mg/kg in the packaging or packaging component; reuse logistics operators commonly require ISO 18604:2013 material recycling under packaging and environment criteria for claimed recyclability. Formulations use 100 phr HD5010EA as the base, 1–3 phr colour masterbatch, 0.5–2.0 phr carbon black masterbatch for outdoor UV exposure exceeding 2,000 h under ISO 4892-2:2013 method A, and 0–30 wt% clean post-industrial regrind from returned crates. Terminal product types include stackable produce crates, bottle crates, dairy crates, and foldable plastic pallet boxes with drop resistance to 1.2 m at -20°C and static stacking load capacity of 400 kg.

    Household storage mouldings produced from HD5010EA are typically qualified for room-temperature and light-duty load conditions, not for continuous load above 50°C or prolonged outdoor exposure without additional UV stabilization; these boundaries are set by the resin’s Vicat softening temperature rather than by short-term tensile retention. The manufacturing window is broader than food packaging: melt temperature 180–210°C, mould coolant 10–25°C, screw L/D 20:1 to 24:1, and clamp force between 1,200 kN and 6,000 kN depending on stack height and the number of cavities.

    Formulation practice uses 98–100 wt% HD5010EA with 1–3 wt% colour masterbatch and 0.05–0.10 wt% nucleating agent where reduced warpage is required for rectangular storage boxes. Non-food housewares do not require FDA or EU food-contact declarations, but the finished articles must satisfy REACH Annex XVII restrictions and, where the article is marketed to children, migration limits for elements under EN 71-3:2019 + A1:2021 categories I to III. Terminal products include storage boxes, clothes hangers, laundry baskets, drawer organizers, and household bins. Moulded-in stress concentration at the attachment point of a hanger hook has been observed to initiate cracking after repeated bending to 45° at 5,000 cycles if the gate is located too close to the hook root; moving the gate to the centre of the body removes the failure in plant durability audits.

    When Leak Tightness Governs Sharps Container Geometry in Clinical Waste Streams

    When a sharps container is required to survive a 1.5 m drop test at -20°C and a subsequent leakproofness hold of 30 minutes with a fine-particle surrogate, gate position and weld-line design become the primary determinants of HD5010EA performance, not the resin’s tensile yield of approximately 26 MPa under ISO 527-2:2012 or notched Charpy impact of 6–8 kJ/m² at 23°C under ISO 179-1:2023. In this application, the grade is injected at a melt temperature of 190–215°C and mould coolant of 15–30°C into 1.8–3.5 mm nominal wall sections using a two-platen clamp force from 1,000 kN to 8,000 kN; low melt temperature is selected to reduce odour-generating volatiles and to protect downstream ultrasonic welding of the lid rail.

    Regulatory compliance at the resin level is limited to REACH and, where applicable, FDA food-contact status for incidental non-food medical packaging; finished sharps containers are qualified under ISO 23907-1:2019 for puncture resistance, leak resistance, and impact resistance, and the relevant packaging waste restrictions under EU Directive 2008/98/EC may apply when containers are disposed as clinical waste. Published data for HD5010EA in ISO 23907-1-configured sharps containers is limited, so conformance is established by end-article testing at the converter level rather than by resin substitution. Formulations use 100 phr HD5010EA with 2–4 phr colour masterbatch; post-consumer regrind is excluded, and in-house regrind is capped at 10–20 wt% where the device specification explicitly permits regrind. Terminal product types include single-use sharps containers, clinical waste bins, and transport boxes for laboratory specimens with lid-to-body interference fit and ultrasonic weld beads measuring 2.0–3.0 mm in height.

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    Certification & Compliance
    More Introduction

    North Huajin (Liaoning) HDPE HD5010EA is a high-density polyethylene injection-moulding grade positioned in the high-melt-flow segment of the producer’s HDPE portfolio. The grade designation identifies a resin with nominal density 0.950 g/cm³ and a melt mass-flow rate near 10 g/10 min when measured at 190 °C under 2.16 kg. These two coordinates place HD5010EA in the low-molecular-weight region of commercial high-density polyethylene and distinguish it from fractional-melt blow-moulding grades and from bimodal pipe resins. Published third-party documentation for this exact configuration is limited; therefore, supplier certificates of analysis should govern lot acceptance. The technical discussion below uses the test designations ISO 1133-1:2022, ISO 1183-1:2019, ISO 527-2:2012, ISO 178:2019, and ISO 179-1:2010 to define the property envelope.

    What Published Data Define HD5010EA, and What Remains Lot-Specific?

    Under ISO 1133-1:2022, equivalent to GB/T 3682.1-2018, the nominal melt mass-flow rate is 10 g/10 min at 190 °C and 2.16 kg. The corresponding melt volume-flow rate is approximately 10.5 cm³/10 min when corrected for a melt density near 0.950 g/cm³. Density is reported as 0.950 g/cm³ under ISO 1183-1:2019. Tensile yield stress is typically 26 MPa at 50 mm/min using ISO 527-2:2012 type 1A specimens, with elongation at yield close to 9%. Flexural modulus for this density class is near 1000 MPa under ISO 178:2019. Notched Charpy impact strength at 23 °C is normally in the range 3.5–5.0 kJ/m² under ISO 179-1:2010; the value at −30 °C is substantially lower, and sub-zero end-use performance requires part-specific validation.

    In capillary rheometry of comparable 10 g/10 min HDPE grades, shear viscosity at 100 s⁻¹ and 200 °C is commonly between 300 Pa·s and 500 Pa·s, falling to 100–180 Pa·s at 1000 s⁻¹. The power-law index is near 0.55. Melt strength is below 5 cN when measured at 190 °C in Rheotens-type equipment, which is far below the melt strength required for large-part extrusion blow moulding. Lot-specific values for ash content, volatile matter, antioxidant package, and additive composition are not consistently available in open literature and must be obtained from the manufacturer’s certificate of analysis.

    The melt-flow position implies a relatively narrow molecular weight distribution and a reduced high-molecular-weight tail compared with bimodal film and pipe grades. In size-exclusion chromatograms of comparable high-flow HDPE resins, weight-average molecular weight is typically below 100 000 g/mol and polydispersity index is below 6. The low melt elasticity reduces die swell and permits filling of long flow paths in multi-cavity tools, but it also reduces melt strength and environmental stress crack resistance. This structural position is the primary technical differentiator relative to blow-moulding, pipe, and high-strength sheet grades.

    Processing Window, Screw Requirements, and Clamp Force Observations

    On production-scale reciprocating-screw injection moulding machines with clamp forces from 800 kN to 6500 kN, HD5010EA is processed at melt temperatures from 190 °C to 260 °C, with higher settings used when melt-blending colour masterbatch. Typical barrel zone profiles are 180 °C rear, 200 °C centre, 220 °C front, and 210 °C nozzle. Screws with 20:1 to 25:1 L/D and medium compression ratios are sufficient; high-shear barrier screws are not required because of the material’s low viscosity. Hydraulic injection pressures in thin-wall moulds commonly range from 60 MPa to 110 MPa, depending on wall thickness and flow length. Back pressure of 0.3–0.7 MPa and screw speeds of 80–150 rpm reduce splay and improve melt homogeneity.

    No pre-drying is normally required for sealed container shipments. If the resin is exposed to ambient air at relative humidity above 60% for extended periods, hopper drying at 80 °C for 2–4 h minimizes surface defects. Moisture-related splay is uncommon but can appear in high-gloss moulded surfaces when condensed water enters the feed throat. At melt temperatures above 290 °C, molecular weight degradation accelerates and should be avoided. The practical maximum barrel residence time at 240 °C is 10–15 min; longer residence causes yellowing and loss of notched impact strength.

    When HD5010EA Replaces a 0.35-Gram Blow-Moulding Grade in Thin-Wall Converters

    Direct substitution of HD5010EA for a fractional-melt HDPE blow-moulding grade is not process-neutral. The 10 g/10 min melt mass-flow rate is approximately 20 to 40 times higher than that of typical large-part blow-moulding resins, which commonly operate near 0.20–0.40 g/10 min under ISO 1133-1:2022. This difference lowers melt pressure at the die head and reduces sag resistance; therefore HD5010EA is not suitable for continuous extrusion blow moulding of large containers, automotive fuel tanks, or technical parts requiring high parison stability. In injection moulding, the same melt-flow difference reduces cycle time, filling pressure, and cooling time relative to a fractional-melt grade. Converters replacing a blow-moulding grade in thin-wall pails, caps, or food containers observe shorter hold-pressure decay times and fewer short-shot rejections on multi-cavity tools. However, the lower molecular weight also reduces environmental stress crack resistance and low-temperature drop-impact toughness.

    Comparative Property Envelope and Standards Matrix

    PropertyHD5010EA nominal classGeneral-purpose blow-moulding HDPEPE100 pipe HDPETest method
    Melt mass-flow rate, 190 °C/2.16 kg10 g/10 min0.35 g/10 min0.25 g/10 minISO 1133-1:2022
    Density0.950 g/cm³0.955 g/cm³0.959 g/cm³ISO 1183-1:2019
    Tensile yield stress26 MPa27 MPa25 MPaISO 527-2:2012
    Flexural modulus1000 MPa950 MPa1100 MPaISO 178:2019
    Notched Charpy impact, 23 °C4.0 kJ/m²25 kJ/m²60 kJ/m²ISO 179-1:2010
    ESCR, F50, 10% Igepal CO-630<10 h>100 h>1000 hASTM D1693-15B
    Typical conversion routeInjection mouldingExtrusion blow mouldingPipe and profile extrusion—

    The property envelope in the table is presented as a class comparison, not as a batch guarantee. Published data for the exact HD5010EA configuration is limited; values marked as nominal class should be verified against the manufacturer’s certificate of analysis before die design, mould filling simulation, or regulatory submission. The contrast in environmental stress crack resistance is particularly significant where the moulded article is exposed to surfactants, alcohols, or fatty food simulants.

    Limitations That Emerge Under Sustained Environmental Stress

    HD5010EA is not a candidate for applications governed by long-term hydrostatic strength standards such as ISO 9080:2012 or ASTM D2837-22. The low molecular weight and narrow molecular weight distribution reduce resistance to slow crack growth; ESCR testing under ASTM D1693-15B in 10% Igepal CO-630 has traditionally classed this material as low-ESCR. For injection-moulded caps and closures that contact household chemicals, the stress-cracking risk can be managed through design optimisation—specifically reduced residual stress, generous radii, and uniform wall thickness—but no additive package fully compensates for the molecular structure. Exposure to strong oxidisers, aromatic hydrocarbons, or halogenated solvents should be considered incompatible without specific end-use validation. Compliance with food-contact requirements must be confirmed with the supplier for the specific grade and batch; statements in this document do not constitute regulatory certification under EU 10/2011, FDA 21 CFR 177.1520, or corresponding national standards.

    Within the North Huajin HDPE range, HD5010EA differs from lower-flow grades used in blown film or blow moulding by its higher melt mass-flow rate and narrower processing window at the upper temperature limit. It also differs from high-flow HDPE grades with higher density, such as 0.955–0.960 g/cm³ injection moulding resins, because the 0.950 g/cm³ density reduces stiffness but improves toughness and stress-crack resistance relative to density 0.960 g/cm³ grades. Selection between HD5010EA and a 0.956 g/cm³ high-flow grade should follow part stiffness, dimensional stability, cap torque retention, and chemical exposure requirements. Colour masterbatch carriers should be selected from HDPE or LLDPE with melt mass-flow rates close to 10 g/10 min; LDPE carriers below 0.5 g/10 min can create viscosity mismatch and visible streaks. Carbon black masterbatches for UV resistance should be pre-dried at 90 °C for 2 h before dosing. Halogenated flame retardants and acidic filler systems should be avoided because they may accelerate molecular weight degradation and cause mould deposit formation.

    For thin-wall food containers injection moulded in multi-cavity moulds at clamp forces below 3000 kN, HD5010EA supports fill times of 0.8–1.5 s in wall sections of 0.6–1.2 mm when the melt temperature is 230 °C and the mould temperature is 20–40 °C. Mould cooling channels should be placed no more than 12 mm from the cavity surface to maintain cycle times below 8 s; longer cooling is required where ribs or bosses exceed 2 mm. Mould shrinkage in the flow direction is typically 1.5–2.0% and transverse shrinkage is 1.2–1.8% for 2 mm plaques injection moulded at 210 °C; post-mould shrinkage at 80 °C can add 0.2–0.4%. Under the EU REACH regulation and Directive 2011/65/EU on the restriction of hazardous substances, HDPE resins of this class are not generally expected to contain restricted substances above concentration thresholds; nevertheless, the manufacturer’s safety data sheet and REACH registration status for HD5010EA must be obtained for compliance declarations.

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