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Versalis HDPE COM75HF1

    • Product Name: Versalis HDPE COM75HF1
    • 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 235223
    Density 0.950 g/cm3
    Melt Flow Rate 190c 2 16kg 7.5 g/10 min
    Tensile Modulus 1000 MPa
    Tensile Stress At Yield 22 MPa
    Tensile Strain At Break 600 %
    Charpy Notched Impact Strength 23c 6 kJ/m2
    Charpy Notched Impact Strength Minus20c 3 kJ/m2
    Vicat Softening Temperature 120 °C
    Heat Deflection Temperature 0 45mpa 70 °C
    Shore D Hardness 60
    Melting Temperature 130 °C
    Water Absorption <0.01 %
    Mold Shrinkage 1.5-2.0 %

    As an accredited Versalis HDPE COM75HF1 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Versalis HDPE COM75HF1 is packaged in 25 kg polyethylene bags, with 40 bags per 1,000 kg pallet.
    Container Loading (20′ FCL) Versalis HDPE COM75HF1 loaded in 20′ FCL: 25 kg bags, palletized and shrink-wrapped, securely stowed; approximately 24–25 metric tons net.
    Shipping Versalis HDPE COM75HF1 is a non-hazardous high-density polyethylene resin supplied as solid pellets. It is typically shipped in 25 kg bags or 1,000 kg jumbo bags, palletized and stretch-wrapped, by truck or container. Not regulated for transport; store dry, cool, and away from ignition sources.
    Storage Store Versalis HDPE COM75HF1 in original, closed packaging in a cool, dry, well-ventilated area. Protect from direct sunlight, moisture, heat, ignition sources, and strong oxidizers. Avoid dust generation, static discharge, and contamination. Keep away from food and feed. Observe stacking limits, good housekeeping, and local regulations. Use first-in, first-out stock rotation; inspect containers for damage before use.
    Shelf Life Versalis HDPE COM75HF1 has a shelf life of about 24 months when stored dry in sealed original packaging, away from sunlight and heat.
    Application of Versalis HDPE COM75HF1

    Versalis HDPE COM75HF1: Downstream Application Technical Data

    Data boundaries: The processing values in this section are derived from publicly reported high-fluidity HDPE injection-moulding practice and from applicable regulatory texts rather than from a single confidential producer datasheet. Published product-specific data for Versalis HDPE COM75HF1 under every downstream configuration is limited; the melt-flow range, density, and batch-specific additive package must therefore be confirmed against the producer's certificate of analysis under ISO 1133-1:2022 and ISO 1183-1. All numerical windows are presented as engineering reference ranges and are not a substitute for production-line qualification.

    Compliance matrix for selected downstream tracks
    Application trackCited standard or test methodAcceptance condition or test valueProduction line verification
    Thin-wall dairy and margarine packaging(EU) No 10/2011, EN 1186-1, FDA 21 C.F.R. §177.1520Overall migration ≤ 10 mg/dm²; olefin polymer specification complianceMigration test on finished article under worst-case filling and temperature
    Beverage and food closuresFDA 21 C.F.R. §177.1520, (EU) No 10/2011, ISO 13302:2003Food-contact compliance plus no detectable organoleptic transferRaw material certification and sensory panel on sealed bottle/cap assembly
    UN-rated pails and jerricansADR Chapter 6.1, UN Model Regulations Chapter 6.1Design-type drop, stacking, leakproofness and hydrostatic pressure per 3H1/1H1 classificationType approval tests on injection-moulded containers
    Logistics cratesISO 179-1/1eA, ASTM D638-14, ASTM D1693Tensile yield stress and Charpy impact per material specification; environmental stress-cracking resistance Condition BIn-line specimen testing per batch

    Thin-walled dairy and margarine packaging converted from Versalis HDPE COM75HF1 sits at the intersection of two conflicting technical requirements: the melt must fill multi-cavity hot-runner tools at wall sections routinely below 0.8 mm, while the moulded body must retain sufficient stack strength to survive automated filling, sealing, and refrigerated distribution. The governing regulatory framework for EU food-contact output is (EU) No 10/2011, supported by overall migration testing under EN 1186-1; the relevant US framework is FDA 21 C.F.R. §177.1520. Converters supplying the EU market also operate under good manufacturing practice according to (EC) No 2023/2006. The applicable overall migration limit for plastic food-contact materials is normally 10 mg/dm², measured on the finished article rather than on resin pellets. Processing on high-speed injection-moulding lines typically uses melt temperatures of 220–250 °C, thin-wall mould coolant temperatures of 10–25 °C, injection speeds above 150 mm/s, and holding pressures of 40–70 MPa. Multi-cavity tools with 24–96 impressions are standard in this sector; valve-gated hot runners are used to maintain gate freeze-off control and to minimise post-mould warpage. The formulation is compounded either directly on the injection machine or by pre-blend, with base HDPE at 96–100 wt%, a colour masterbatch let-down at 2–4 wt%, and optional nucleating agent masterbatch at 0.1–0.3 wt% where shorter crystallisation time and reduced sink marks are required. Nucleated formulations must be re-qualified for migration and organoleptic properties because nucleation alters crystallinity and surface chemistry. Cycle times of 6–12 s are feasible when wall thickness and part geometry allow; in practice, cycle time is set by the slowest cooling rib, hinge, or lip feature. End products from this route include round dairy pots, margarine tubs, ice-cream containers, deli boxes, and thin-walled dessert cups.

    What Limits High-Speed Closure Moulding for Cold Drink Sealing Systems?

    Closure manufacturing lines running high-fluidity HDPE encounter two failure modes that are not captured by melt-flow ratio alone: tamper-evident band tearing during unscrewing and loss of sealing force after repeated cap application. The material must be processed below high-shear conditions that orient the polymer chain near the thread roots, because excessive orientation produces anisotropic shrinkage and changes release torque. Food-contact compliance is anchored to FDA 21 C.F.R. §177.1520 and (EU) No 10/2011; organoleptic acceptance is evaluated on the sealed package using a trained panel under ISO 13302:2003 or an equivalent internal procedure. Closure lines are split between high-cavitation injection moulding with unscrewing cores and continuous compression moulding. Injection moulding of thin-wall closures uses melt temperatures of 210–245 °C, mould temperatures of 15–30 °C, injection pressures of 80–120 MPa, and cooling times of 5–12 s depending on thread depth and core cooling. Compression moulding runs at melt temperatures of 180–210 °C and cycle times between 4–10 s; it is generally preferred for simple one-part beverage closures because it avoids gate vestige and reduces residual stress. The formulation addition ratio comprises base HDPE at 97–100 wt%, colour masterbatch at 1–3 wt%, and slip agent masterbatch dosed to a final erucamide concentration of 500–1500 ppm. Slip addition must be tuned on the finished cap design and not on resin plaques, because excess slip can cause band tearing, cap doming, and thread skipping on capping machines. Terminal finished products include standard 28 mm and 30 mm still-beverage caps, dairy closures, tamper-evident HDPE closures for juice and edible oil containers, and push-fit closures for UHT milk bottles.

    For pails and jerrycans, the controlling requirement shifts from food-contact migration to transport-container certification, even when the pail will later carry food ingredients. UN certification for plastics packaging is issued only after design-type testing under ADR Chapter 6.1 and the UN Model Regulations Chapter 6.1 for the relevant packaging class: plastics jerricans are designated 3H1, and plastics drums are designated 1H1. The mandatory test sequence includes stack loading, drop impact, leakproofness, and hydrostatic pressure; hydrostatic pressure for small plastic packagings is commonly required at 100 kPa for 30 min, though the exact value is defined by the design type and supervising agency. Containers intended for food use must simultaneously meet (EU) No 10/2011 and FDA 21 C.F.R. §177.1520. Injection moulding of 5–25 L pails is run at melt temperatures of 210–240 °C, mould cooling temperatures of 20–40 °C, injection pressures of 80–110 MPa, and holding pressures established by gate-seal measurements rather than by machine default. The critical processing constraint is weld-line integrity at the handle crossing and the sidewall-to-base transition; a poorly maintained weld line will pass visual inspection but fail the drop test at low temperature. The formulation uses base HDPE at 95–99 wt%, colour masterbatch at 2–5 wt%, and UV stabiliser masterbatch at 0.5–1.5 wt% when outdoor exposure is expected. Terminal finished products from this route include 5 L–25 L open-top pails with injection-moulded bails, 10 L–30 L tight-head jerrycans, and associated tamper-evident lids and plugs.

    Crate and Pallet Moulding Parameters Under Cyclic Loading

    Logistics crates produced from this material are not governed by a single food-contact or transport regulation; instead, performance is specified through mechanical test categories and customer loading protocols. Structural acceptance is commonly based on ISO 179-1/1eA Charpy notched impact, ASTM D638-14 tensile yield stress, and ASTM D1693 environmental stress-cracking resistance. Moulders convert the high-flow HDPE on medium-to-large injection machines, with melt temperatures of 220–250 °C, mould cooling temperatures of 15–30 °C, injection pressures of 90–130 MPa, and cooling times of 25–45 s for ribbed crate structures. The processing window is wider than thin-wall food packaging because wall sections are heavier and the main defects are sink marks, ejection distortion, and stress-cracking at sharp ribs rather than short-shot or gate freeze-off. Formulation addition ratio is usually base resin at 94–100 wt%, colour masterbatch at 2–4 wt%, and UV stabiliser concentrate at 0.5–1.5 wt% for outdoor vegetable or bottle crates. Some converters include qualified regrind, but the addition level is bounded by the final notched Charpy impact specification and must be re-validated after changing regrind source. Finished product families include ventilated fruit and vegetable crates, bottle crates, logistics tote boxes, and folding sleeve pack bases for automated distribution centres.

    Indicative injection-moulding processing windows by downstream track
    Downstream trackMelt temperatureMould temperatureInjection pressureCycle/cooling
    Thin-wall dairy packaging220–250 °C10–25 °C40–70 MPa holding6–12 s
    Beverage closures210–245 °C / 180–210 °C compression15–30 °C80–120 MPa5–12 s
    Pails/jerricans210–240 °C20–40 °C80–110 MPaGate-seal determined
    Logistics crates220–250 °C15–30 °C90–130 MPa25–45 s
    Household articles200–240 °C20–35 °C70–100 MPa20–40 s
    Returnable trays210–245 °C15–30 °C90–120 MPa30–50 s

    When High-Fluidity HDPE Replaces Drop-In Bottle Grades in Household Articles

    Household storage articles manufactured from high-flow HDPE require moderate surface appearance and low warpage at minimum cycle cost. Injection moulding is performed with melt temperatures of 200–240 °C, mould temperatures of 20–35 °C, injection pressures of 70–100 MPa, and cycle times of 20–40 s depending on wall thickness and handle geometry. The relevant compliance framework for non-food housewares is primarily REACH Annex XVII; when the article is intended for food utility, the same FDA 21 C.F.R. §177.1520 and (EU) No 10/2011 material requirements apply. Formulation addition ratio is typically 96–100 wt% base HDPE, 2–4 wt% colour masterbatch, and optional antistatic masterbatch at 0.5–1.5 wt% for dust-sensitive retail articles. The product families manufactured in this route include storage boxes, clothes hangers, waste bin bodies, and utility trays.

    In automotive component logistics, returnable transport trays are subject to repeated mechanical handling, oil contact, and dimensional stability requirements that affect automated robot picking. Conversion is by injection moulding on machines with clamp force selected from projected area and part depth; for deep dunnage trays, clamp forces between 1200 t and 2400 t are common but must be calculated from cavity pressure data. Melt temperatures are held at 210–245 °C, mould temperatures at 15–30 °C, injection pressures at 90–120 MPa, and cycle times from 30–50 s depending on rib depth. Dimensional stability is assessed after conditioning for 24 h at 23 °C and 50 % relative humidity under ISO 291. When the tray is used as a VDA small-load carrier, dimensional interchangeability follows VDA 4500; otherwise, automotive logistics specifications are customer-specific. Formulation addition ratio comprises 97–100 wt% base HDPE, 2–4 wt% colour masterbatch, and optional electro-static dissipative or antistatic masterbatch at 0.5–1.5 wt% where electronic component handling requires surface resistivity control. Terminal finished product types include returnable dunnage trays, VDA small-load carriers, robot-picked component trays, and stacking containers for powertrain parts.

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