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PCC (Iran) HDPE HD6070UA

    • Product Name: PCC (Iran) HDPE HD6070UA
    • 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 664025
    Product Name PCC (Iran) HDPE HD6070UA
    Manufacturer PCC (Iran)
    Polymer Type High Density Polyethylene (HDPE)
    Grade HD6070UA
    Application Blow molding
    Density 0.960 g/cm³
    Melt Flow Rate 0.07 g/10 min (190°C/2.16 kg)
    Melting Point 134 °C
    Vicat Softening Temperature 126 °C
    Tensile Yield Strength 26 MPa
    Elongation At Break >600%
    Flexural Modulus 1200 MPa
    Environmental Stress Crack Resistance >1000 h
    Uv Stabilization Yes
    Form Pellets
    Color Natural
    Bulk Density 0.55 g/cm³
    Hardness 60 Shore D
    Thermal Stability Good
    Odor Odorless
    Toxicity Non-toxic
    Molecular Weight Distribution Broad

    As an accredited PCC (Iran) HDPE HD6070UA factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing PCC (Iran) HDPE HD6070UA is supplied in 25 kg PP woven bags, typically 55 bags per pallet.
    Container Loading (20′ FCL) PCC Iran HDPE HD6070UA in 20′ FCL: 25 kg bags, 17 MT net, dry, secure, weather-protected stowage.
    Shipping PCC (Iran) HDPE HD6070UA is a non-hazardous high-density polyethylene. It ships in 25 kg PE bags or jumbo bags, palletized and stretch-wrapped, in 20'/40' FCL containers by sea from Iranian ports. Store dry, away from sunlight, heat, and moisture. HS code: 3901.20. No special DG requirements; use clean, dry containers.
    Storage Store PCC (Iran) HDPE HD6070UA in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and strong oxidizers. Keep original bags sealed, palletized, and off the floor to prevent moisture and contamination. Avoid prolonged UV exposure and high stacking loads that may deform pellets. Follow local fire and safety regulations.
    Shelf Life Shelf life is 24 months when stored in original packaging, dry, ventilated, away from direct sunlight, heat, and moisture.
    Application of PCC (Iran) HDPE HD6070UA

    In returnable beverage crate moulding, HD6070UA is processed at a melt temperature of 210–240 °C against a mould face maintained at 20–35 °C. The grade’s nominal melt flow rate of 7.0 g/10 min under ISO 1133-1:2022 and nominal density of 0.960 g/cm³ under ISO 1183-1:2019 provide the shear-dependent viscosity needed to fill multi-cavity stack moulds with projected area clamp requirements of 0.6–0.8 t/cm². Compliance for this downstream route is normally assessed against EN 13117-1:2000 for reusable rigid plastics distribution boxes and 94/62/EC Annex II heavy-metal concentration limits, which restrict the sum of lead, cadmium, mercury, and chromium VI to 100 mg/kg. Formulations in production often run 2.0–3.0 wt% white masterbatch to obtain consistent opacity in side-wall sections of 2.5–4.0 mm; when crates are stored outdoors beyond typical return-loop cycles, an additional concentrated UV masterbatch at 1.5–2.5 wt% may be compounded into the feed throat, while antioxidant masterbatch is held between 0.05–0.15 wt%. Moulders using hot-runner valve gates or edge gates observe that shorts at the base grid depend on gate diameter; gates below 1.5 mm can freeze before packing, while gates above 2.5 mm extend cycle time. Stackable bottle crates and 12/24-bottle beverage trays are the terminal items, with linear mould shrinkage after 24 h generally recorded between 1.6% and 2.4% when measured on plaques prepared to ISO 294-4:2018.

    What Processing Window Governs Thin-Wall Food Containers and Dairy Cups?

    Compliance for thin-wall food-contact articles is an article-level verification rather than a resin-level certificate. Dairy cups, margarine tubs, and single-serve food containers made from HD6070UA must satisfy EU Regulation (EC) No 10/2011 Annex V overall migration limits of 10 mg/dm², while in the United States the finished article falls under FDA 21 CFR 177.1520(c) service-condition categories 3.1a and 3.2a when the intended use covers aqueous, acidic, and low-alcohol foods at hot-fill or room-temperature conditions. Formulation loading is intentionally lean: titanium dioxide-based white masterbatch is metered at 1.5–2.5 wt%, antioxidant at 0.05–0.10 wt%, and mineral filler is excluded because it raises density and can impair side-wall impact at ring-stiffened rim sections. The downstream process is high-speed injection moulding on accumulator-equipped machines with screw L/D ratios between 22:1 and 25:1, using melt temperatures of 230–250 °C and chilled mould temperatures of 10–25 °C. Wall sections commonly range from 0.5 mm to 1.2 mm, and cycle time is controlled by gate freeze and part ejection rather than plasticating capacity; production experience on 6- to 12-second cycles shows that inconsistent mould temperature across the cavity leads to warped rims after shrink film tunnel heating. Terminal finished products include dairy pots, spreadable-fat tubs, ice cream cups, and food service containers with denesting lugs.

    Where open-top pails are specified for water-based paints, adhesives, and construction chemicals, the injection moulder normally balances flow length against side-wall rigidity. HD6070UA is processed at 210–240 °C with a mould temperature of 15–35 °C; the pail body is produced with a nominal wall of 2.0–3.0 mm and a tapered side wall of 0.5–1.0° for de-nesting. Regulatory compliance for dangerous goods pails uses the design-type tests in UN Model Regulations Chapter 6.1 and ADR/RID 6.1.5, including drop tests at -18 °C, stack tests, and hydraulic pressure tests of 100 kPa for certain packing groups; non-dangerous paint pails are usually assessed against the same drop and stacking benchmarks by customer specification. Compound formulations in this segment commonly incorporate 2.5–4.0 wt% calcium carbonate masterbatch to reduce visible sink marks at handle lugs, with pigment masterbatch at 1.0–1.5 wt% and antioxidant at 0.08–0.15 wt%. Excessive filler above 5 wt% is avoided because it introduces notch sensitivity at the rim and reduces Charpy impact in conditioned samples. Conversion lines use multi-cavity open-hot-runner or cold-runner tools; handle parts are either integrally moulded or assembled by post-mould snap-in lugs. Terminal part types are cylindrical pails from 1 L to 25 L, including tamper-visible tear-tab lids and side-handle paint buckets.

    Pigment Loading and Hot-Runner Behaviour in High-Cavitation Cap Moulding

    Closure production at 48-cavity and 96-cavity tools changes the relevance of standard HDPE processing data because shear heating in hot-runner tips raises melt temperature independently of barrel set points. For HD6070UA, melt temperature is maintained between 220 °C and 250 °C, while mould temperatures of 10–20 °C are used to shorten thread cooling and prevent ovality after ejection. Formulation ratios in cap and closure moulding are lower than in thick-section items: slip/antiblock masterbatch is introduced at 0.5–1.0 wt%, pigment at 0.5–1.5 wt%, and antioxidant at 0.05–0.10 wt%. Higher slip loadings are avoided because erucamide migration can change torque retention on tamper-evident bands and cause cap-on-thread stress cracking in detergent bottles. Compliance for food-contact closures uses EU Regulation (EC) No 10/2011 and FDA 21 CFR 177.1520; child-resistant closures for agrochemical or pharmaceutical applications are additionally tested to ISO 13127:2012. The injection process uses valve-gated hot runners; gate seal time is typically 0.3–0.8 s after injection hold pressure is set to 500–800 bar hydraulic. Terminal finished products include detergent bottle caps, cosmetic jar closures, agrochemical screw caps, and tamper-evident lids for nutritional powder containers.

    For kerbside wheeled bins and garden storage boxes, long-term ultraviolet exposure rather than short-cycle injection fill is the controlling design parameter. Weathering compliance in this segment is typically benchmarked against EN 840-1:2020 for two-wheeled mobile waste containers and accelerated weathering exposure to ISO 4892-2:2013 cycle 1 or equivalent; outdoor parts are expected to retain impact strength after 4 000–8 000 h of xenon-arc exposure depending on colour and climate. EU market access additionally requires compliance with Regulation (EC) No 1907/2006 Annex XVII restrictions for articles, with particular attention to polycyclic aromatic hydrocarbons in carbon black masterbatch. HD6070UA is processed on two-platen injection moulding machines with melt temperature 210–240 °C and mould temperature 20–40 °C; large components with wall sections from 3 mm to 6 mm require cycle times of 40–70 s, with cooling dominated by the thick corner bosses and wheel brackets. In black parts, carbon black masterbatch is added at 1.5–2.5 wt% to provide UV screening; coloured outdoor parts generally require 3.0–4.0 wt% of a stabilised pigment masterbatch plus 0.1–0.2 wt% antioxidant. Recycled post-industrial regrind is often blended at up to 20–30 wt% in non-load-bearing panels, but the proportion is reduced when the part must pass low-temperature drop impact at -20 °C. Terminal products include 240 L two-wheeled bins, garden storage chests, compost bins, and outdoor seat shells.

    When Cold-Chain Fish Crates Are Demoulded Below the Vicat Softening Plateau

    The cooling stage in vented cold-chain crates is frequently shortened to improve cycle time, but demoulding too close to the Vicat softening plateau creates lip deformation under stack load. For HD6070UA, melt temperature is set at 220–245 °C and mould temperature at 10–25 °C; part weight falls between 1.5 kg and 4.0 kg, with vent slots of 5–10 mm width requiring stable flow fronts. Compliance for direct food contact in fish, poultry, and meat distribution uses Regulation (EC) No 1935/2004, Regulation (EC) No 10/2011, and good manufacturing practice under (EC) No 2023/2006; where exported to North America, FDA 21 CFR 177.1520 is applied. The formulation is limited to 2.5–3.5 wt% white or blue masterbatch and 0.08–0.15 wt% antioxidant; post-consumer recyclate is excluded in single-use food contact layers to control migration of unknown contaminants. Injection tooling integrates stacking ribs, bottom support pads, and drainage channels; filling is sequenced through three or more gates to prevent melt-flow hesitation around the vent slits. Published data for this specific cold-chain configuration is limited, so converters typically establish final mould-opening speed and stack-load deflection by pilot runs rather than by extrapolating generic HDPE databook values. Terminal finished products include seafood transport crates, poultry tray totes, and meat distribution boxes.

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    Certification & Compliance
    More Introduction

    PCC (Iran) HDPE HD6070UA is a high-density polyethylene injection moulding grade with a nominal melt mass-flow rate of 7.0 g/10 min at 190 °C under 2.16 kg load when tested according to ISO 1133-1:2022, and a nominal density of 0.960 g/cm³ measured under ISO 1183-1:2019. Supplier literature places the grade in thin-wall food and non-food containers, caps, closures, crates, pails, housewares, and general-purpose injection moulded articles. The UA suffix denotes a formulated additive package; published compositional data for the exact antioxidant, UV, and antistatic loading is limited. The values in this document are nominal values from supplier technical data and are not a substitute for a production lot certificate of analysis.

    Nominal rheological, thermal, and mechanical property envelope

    The combination of a 0.960 g/cm³ nominal density and 7.0 g/10 min melt mass-flow rate indicates a high-stiffness injection moulding grade with a moderate flow length. At 190 °C the melt temperature lies within the standard processing band for high-density polyethylene, while the MFR value provides adequate melt delivery into multi-cavity tooling without entering the low-melt-strength region of high-flow grades. Thermal and mechanical properties are summarised below.

    PropertyNominal valueTest method
    Melt mass-flow rate, 190 °C, 2.16 kg7.0 g/10 minISO 1133-1:2022
    Density0.960 g/cm³ISO 1183-1:2019
    Tensile yield stress26 MPaISO 527-1:2019, ISO 527-2:2012
    Tensile strain at break>300%ISO 527-2:2012
    Flexural modulus1300 MPaISO 178
    Izod notched impact strength, 23 °C6 kJ/m²ISO 180/A
    Shore D hardness62ISO 868
    Vicat softening temperature, A50123 °CISO 306/A50

    The flexural modulus of 1300 MPa is consistent with a 0.960 g/cm³ density and supports rigid part design, while the notched Izod value of 6 kJ/m² at 23 °C places the resin in the stiff-tough balance typical of injection moulding HDPE. Melt viscosity at shear rates between 100 s⁻¹ and 1000 s⁻¹ is not fully described by the MFR because the MFR is a low-shear measurement; capillary rheometry should be used for gate and runner shear-rate calculations. Published capillary viscosity curves for this exact grade are limited.

    On injection moulding lines, barrel set-point profiles from 180 °C to 230 °C and mould temperatures from 10 °C to 40 °C are typical for HDPE of this flow class. Screw L/D ratios from 20:1 to 24:1 and compression ratios from 2.5:1 to 3.5:1 are accepted in general practice. The material is not hygroscopic in the manner of polyamide or PET, but condensation on cold pellet surfaces should be removed before processing.

    In high-speed thin-wall moulding, holding cushion below 2 mm can destabilise shot weight and final part mass. Back pressure above 1.0 MPa can increase melt temperature and reduce recovery efficiency without improving homogeneity for this grade. Published data for this specific configuration is limited; machine parameters should be established by short-shot studies on the production tool.

    How does HD6070UA differ from fractional-melt blow moulding and extrusion resins?

    Fractional-melt high-density polyethylene grades used in extrusion blow moulding and large-part extrusion typically have MFR values below 1.0 g/10 min under ISO 1133-1:2022. Their high molecular weight provides melt strength sufficient for parison control, sheet draw stability, and environmental stress crack resistance. HD6070UA at 7.0 g/10 min is not a direct substitute in those processes because its lower melt strength can permit parison sag and excessive draw in blow moulding operations.

    Conversely, blow moulding and extrusion grades are poorly suited to multi-cavity thin-wall injection tooling because their lower MFR produces higher filling pressure, longer cycle times, and reduced mould-fill consistency at wall thicknesses below 1.5 mm. The flow length of HD6070UA supports thinner walls and shorter cooling cycles, but the trade-off is reduced environmental stress crack resistance relative to fractional-melt HDPE. ESCR testing under ASTM D1693-15 generally trends lower as MFR increases, though published comparative ESCR data for this PCC grade are limited.

    Compared with high-flow HDPE grades above 20 g/10 min, HD6070UA retains a higher density and a more rigid mechanical profile. The 6 kJ/m² notched Izod impact at 23 °C and 1300 MPa flexural modulus indicate a balance intended for structural thin-wall articles that must tolerate demoulding stresses and downstream handling. High-flow grades above 20 g/10 min may fill thinner sections with lower injection pressure, but published data for this specific configuration is limited in whether they can deliver the same flexural modulus at equivalent density.

    When wall thickness falls below 1 mm, gate design and injection velocity dictate warpage

    At nominal wall thickness below 1.0 mm, the processing window narrows because cooling time and pressure transmission become dominated by flow length rather than equilibrium melt temperature. Gate diameters below 0.6 mm can impose high shear rates in the runner and gate region; for HDPE, shear rates above approximately 100,000 s⁻¹ may induce jetting, surface roughness, or gate-related flow instability. The exact threshold depends on melt temperature, die geometry, and additive package.

    Injection velocity for such sections should be set high enough to prevent premature gate freeze-off before packing, but not so high that cavity gas becomes trapped at the melt front. Packing pressure is commonly applied at 40% to 60% of peak injection pressure for semi-crystalline HDPE parts; excessive packing at gate-seal can increase moulded-in stress and degrade dimensional stability. Mould temperature between 10 °C and 20 °C shortens cycle time but may increase differential shrinkage in ribs and bosses. Where warpage is critical, instrumented trials under ISO 294-1:2017 specimen preparation conditions and dimensional audit after 48 h ageing are required.

    High-density polyethylene crystallises rapidly, so crystalline shrinkage and moulded-in anisotropy are not removed by moderate annealing. Published data for this specific configuration is limited when considering annealed dimensional recovery of HD6070UA at temperatures above 80 °C. For load-bearing parts, creep behaviour should be evaluated under ISO 899-1:2017 at the intended service temperature, because short-term tensile yield data do not define long-term deflection.

    Because HD6070UA is a high-density polyethylene, predrying is normally unnecessary unless the resin has been exposed to condensation or stored at relative humidity above 60% with surface moisture. In that case, pellet drying at 70 °C for 2 h is generally sufficient. Regulatory assessment is confined to the final article rather than the resin alone. For food-contact applications, the resin is typically represented as suitable for evaluation under FDA 21 CFR 177.1520(c) and EU Regulation (EU) 10/2011, but overall migration and organoleptic testing must be performed on the finished package because processing aids, colourants, and tooling residues can affect compliance.

    Regulatory domainReferenceAssessment basis
    Food-contact resin statusFDA 21 CFR 177.1520(c)Olefin polymer requirements; final article migration testing may be required
    European food-contact frameworkEU Regulation (EU) 10/2011Overall migration and specific migration limits apply to the finished article
    Restriction of hazardous substancesRoHS Directive 2011/65/EUCompliance at homogeneous material level; supply-chain documentation required
    EU chemical registrationREACH Regulation (EC) 1907/2006Substance registration and candidate list obligations evaluated by the legal entity placing the product on the market
    Chemical resistance testingISO 175:2021, ASTM D543-21Exposure testing on finished part or test plaques for specific chemical classes

    Continuous contact with strong oxidising acids, chlorinated solvents, or aromatic hydrocarbons at temperatures above 40 °C is outside the typical service boundary for high-density polyethylene and requires chemical resistance qualification on the actual part geometry. The resin is not intended for applications where sustained load and aggressive chemical exposure coincide without stress-cracking evaluation under ASTM D1693-15 or an equivalent notched constant-strain test.

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