Products

PCC (Iran) HDPE 62107

    • Product Name: PCC (Iran) HDPE 62107
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    VTB
    Specifications
    HS Code 335755
    Density 0.957 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 7.0 g/10 min
    Tensile Strength At Yield 30 MPa
    Tensile Strength At Break 20 MPa
    Elongation At Break >600%
    Flexural Modulus 1200 MPa
    Notched Izod Impact Strength 23 C 50 J/m
    Shore D Hardness 65
    Vicat Softening Temperature 125°C
    Heat Deflection Temperature 0 45 Mpa 75°C
    Melting Point Dsc 132°C
    Crystallization Temperature 115°C
    Water Absorption <0.01%
    Bulk Density 0.58 g/cm³
    Moisture Content <0.05%
    Ash Content <0.05%

    As an accredited PCC (Iran) HDPE 62107 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing PCC (Iran) HDPE 62107 typically supplied in 25 kg PP bags, 40 bags per pallet (1,000 kg), shrink-wrapped.
    Container Loading (20′ FCL) Container Loading (20′ FCL): PCC (Iran) HDPE 62107, 25 kg bags, palletized, shrink-wrapped, securely stowed in container, loaded and sealed.
    Shipping PCC (Iran) HDPE 62107 is a non-hazardous high-density polyethylene resin. It is shipped in 25 kg PP woven bags or 1 MT jumbo bags, palletized and stretch-wrapped, in dry sea containers. Not UN-regulated; keep dry, away from heat, sunlight, moisture, and contamination.
    Storage Store PCC (Iran) HDPE 62107 in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep original bags/containers closed to prevent moisture and contamination. Avoid contact with strong oxidizers. Protect from UV exposure and physical damage. Use first-in, first-out stock rotation. Ground equipment during bulk handling to control static. Do not store outdoors for prolonged periods.
    Shelf Life PCC (Iran) HDPE 62107 shelf life is typically 12 months when stored unopened, cool, dry, and away from direct sunlight.
    Application of PCC (Iran) HDPE 62107

    PCC Iran supplies HDPE 62107 as an injection-moulding high-density polyethylene with a nominal melt flow rate of 7 g/10 min determined by ASTM D1238 at 190°C/2.16 kg and a nominal density of 0.962 g/cm³ determined by ASTM D1505. The processing window is controlled by a competition between flow length, crystallisation-driven shrinkage, and environmental stress crack resistance. That makes it suited to rigid injection-moulded dairy packaging, closures, open-head industrial pails, logistics crates and pallets, and carrier-resin compounding. The following scenarios treat these applications separately because the failure hierarchy changes with part geometry. Published data for this specific configuration is limited and should be validated against the supplier certificate of analysis and the individual mould.

    What Changes When Wall Thickness Falls Below 0.80 mm in High-Speed Dairy Packaging?

    Thin-wall dairy packaging converts HDPE 62107 in stackable cups, tubs, and lids with wall sections from 0.60 mm to 1.20 mm, but the critical shift begins below 0.80 mm. At that point, flow length and pressure drop dominate. A flow length-to-wall-thickness ratio of 100:1 to 150:1 requires melt temperature between 215°C and 235°C, injection velocity from 100 mm/s to 180 mm/s, and peak injection pressure from 80 MPa to 120 MPa. Above 235°C the free-flow behaviour creates a false sense of processability; the added fluidity is paid for by surface streaking, gate-stringing, and an increased risk of plate-out on exhaust vents. Dropping below 210°C forces the cavity to freeze before packing, and uncontrolled volumetric shrinkage appears as sink marks at the stacking shoulder and rim distortion. Gate selection follows from the freeze-off condition. Hot-runner valve-gate systems use gate diameters of 0.8 mm to 1.5 mm, with valve-pin delay held below 0.3 s to prevent melt freezing in the gate land. Cold-runner tunnel gates are kept above 1.2 mm; smaller gates freeze in under 1.5 s and block pack pressure from reaching the cavity. The tool is normally maintained at 10°C to 25°C. The lower end of that range shortens cooling time but increases the risk of stress cracking at the rim when the container is later exposed to chilled dairy cream or acidic whey. Targeted cooling time for 0.80 mm wall is 4.5 s to 6.0 s; for 0.60 mm it falls to 2.5 s to 3.5 s, and for 1.00 mm it rises to 8.0 s to 12.0 s. Pack pressure is maintained at 30 MPa to 60 MPa for 0.8 s to 2.5 s. The end product is a stackable dairy pot, lid, or single-serve dessert cup in which the critical release criterion is not tensile yield but drop impact at 0°C to 5°C after filling. Finished-container testing commonly uses ASTM D5276 for free-fall drop and ASTM D2463 for impact damage evaluation. Slip and anti-block levels are masterbatch-controlled and are not fixed by the base resin specification, so the dairy line must qualify the material under EU No 10/2011 and FDA 21 CFR 177.1520(c) before pack-out.

    Wall thicknessInjection velocityPeak cavity pressureCooling timeHold pressureMould temperature
    0.60 mm120–180 mm/s90–120 MPa2.5–3.5 s30–50 MPa10–20°C
    0.80 mm100–160 mm/s80–110 MPa4.5–6.0 s30–60 MPa10–25°C
    1.00 mm80–140 mm/s70–100 MPa8.0–12.0 s35–60 MPa15–25°C

    When the Gate Freezes Before Packing Completes in 20 L Open-Head Pails

    Open-head pails from 5 L to 25 L are the most structurally demanding application for HDPE 62107 because the useful wall thickness of 2.0 mm to 2.8 mm lies above the thin-wall regime but below the heavy-section regime used in crates. The process conflict is gate freeze time. With a standard cold sprue gate below 3.5 mm diameter, the gate begins to freeze before the pack phase has transmitted 15 MPa to 25 MPa to the far rim, leaving underpacked areas around the handle lugs. The defect may not be visible immediately after ejection; it appears later as environmental stress cracking at the lug root under stacking load or as leakage after a drop test. For a 20 L pail, the gate diameter is kept between 4.0 mm and 5.0 mm, or a hot-runner valve gate is used with a nozzle tip temperature of 220°C to 230°C. Mould fill time is 2.5 s to 4.0 s, pack pressure is 15 MPa to 25 MPa, and hold time is 8 s to 12 s. Cooling time for a 2.0 mm wall is 18 s to 22 s; for a 2.5 mm wall it rises to 28 s to 35 s. Total cycle time on a 650 t hydraulic machine with a single cavity is 40 s to 55 s. The end product is an open-head pail for lubricants, food ingredients, water-based coatings, and industrial chemicals. Mechanical validation is carried out by stacking top-load tests at 40°C and 80% RH for 7 days, with acceptable failure load above 250 kg per column depending on wall thickness and rim design. Low-temperature drop testing follows ASTM D5276 after conditioning at -18°C for 24 h; the drop height is 1.2 m. The weak feature is rarely the flat wall; it is the weld line around the handle bridge. With a single gate, weld-line tensile strength retention in HDPE is only 50% to 70% of the bulk value, so gate position is biased to move the weld line away from the handle attachment zone and into the base corner. ESCR testing under ASTM D1693 Condition B in 10% Igepal at 50°C is used to screen for stress crack resistance; in this geometry, F50 values below 100 h are considered inadequate for lubricant and detergent pails. Regrind reincorporation is capped at 20 wt% to 25 wt%, because higher ratios reduce ESCR and low-temperature impact disproportionately compared with melt flow index. Shrinkage in a pail with this wall thickness is measurable but manageable: 1.5% to 1.8% in flow and 0.8% to 1.1% cross-flow. The mould designer compensates by increasing the rim diameter and maintaining uniform cooling between the bottom and the rim. If the bottom is cooled faster than the rim, the pail becomes oval and the lid seal fails.

    Closure production changes the failure hierarchy from drop impact to stress-crack growth at the thread root and torque loss during repeated resealing. HDPE 62107 is used for beverage, sauce, and pharmaceutical closures with thread diameters from 24 mm to 48 mm. In a 38 mm carbonated soft drink cap, the thread root wall is 0.6 mm to 1.0 mm, and the bridge dimensions of the tamper-evident band are 0.25 mm to 0.45 mm. The mould is typically a 32-cavity hot-runner tool with point gates of 0.6 mm to 0.9 mm. Filling takes 0.5 s to 1.2 s, packing takes 0.5 s to 1.5 s, and cooling takes 2.5 s to 4.5 s. Total cycle time is 6.0 s to 9.0 s. The cap must combine low removal torque with high burst resistance. Erucamide slip is added by masterbatch at 0.05 wt% to 0.15 wt%; above that range the removal torque drops but the outer surface develops haze and the cap may scuff during high-speed capping. Taste and odour are controlled by limiting degradation during extrusion and moulding, but the grade itself is not a barrier polymer; oxygen ingress through the cap gasket should be managed by the liner or valve design, not by the cap body. Carbonated soft drink closure performance is verified on a PET bottle by pressurisation to 5.5 bar at 30°C, and leakage is assessed under ASTM D4991. For pharmaceutical and chemical closures, the restriction is chemical resistance and stress cracking. A 10% Igepal solution at 50°C is used with ASTM D1693 Condition B; the criterion is F50 above 150 h for aggressive surfactant-based products. White cap applications often use titanium dioxide masterbatch at 2 wt% to 5 wt% to increase opacity. The food-contact status is established through EU No 10/2011 overall migration testing and FDA 21 CFR 177.1520(c). The table below summarises the compliance matrix for closure and rigid packaging end-uses.

    End-useReferenceMeasurementAcceptance criterion
    EU food contactRegulation (EU) No 10/2011, EN 1186-1Overall migration<10 mg/dm²
    US FDA food contact21 CFR 177.1520(c)Olefin polymer specificationEnd-test under conditions of use
    Pharmaceutical packagingUSP <661.2>Physicochemical testsMeets plastic container limits
    REACHRegulation (EC) No 1907/2006SVHC screeningNo SVHC above 0.1 wt%
    RoHSDirective 2011/65/EURestricted substancesPb, Hg, Cr(VI), PBB, PBDE below 1000 ppm; Cd below 100 ppm

    Heavy-Duty Crate Weld-Line Placement under 700 t Clamp Force

    Logistics crates and modular pallets represent the upper shot-weight boundary for this grade. HDPE 62107 can fill a 15 kg to 25 kg shot when the projected area is supported by a clamp force of 700 t to 1,200 t, depending on the number of cavities. Wall thickness in load-bearing side walls is 4 mm to 6 mm, and the floor ribs are 5 mm to 8 mm. The dominant moulding problem is not fill but weld-line placement and differential shrinkage. Injection time is 6 s to 12 s, pack pressure is 30 MPa to 50 MPa, and total cycle time is 60 s to 120 s. Barrel temperatures are lower than in thin-wall moulding: 200°C to 220°C, because longer residence time at high temperature causes yellowing and brittleness at the weld line. The tool temperature is 10°C to 20°C; turbulent cooling with Reynolds numbers above 10,000 prevents hot spots in thick bosses. Weld lines in crates should be moved out of the corner columns and handle apertures. If the weld line is forced into a high-stress corner, the part fails at 50% to 70% of the un-welded tensile strength. The finished crate is usually validated by cold chain drop tests at -20°C after 24 h conditioning; the acceptance criterion is no fracture in 10 drops from 0.5 m to 1.0 m depending on the market. Long-term load is evaluated according to ISO 8611-2 for pallet racking stiffness and creep. With high-density crystallinity, shrinkage is 1.6% to 2.0% in flow and 0.8% to 1.2% transverse. Unbalanced cooling of the floor and side walls creates corner lift above 3 mm per 500 mm side length, which causes pallet instability. For outdoor logistics crates, UV stabilization is necessary; unstabilized HDPE loses surface gloss and impact strength after 1000 h of ASTM G154 weatherometer testing, and the stabilizer masterbatch is incorporated at 1 wt% to 3 wt%.

    Masterbatch production uses the same melt flow index as a carrier because the 7 g/10 min flow wetting allows pigment loading from 30 wt% to 50 wt% on a co-rotating twin-screw extruder. Barrel temperature is kept between 160°C and 210°C, die pressure is 3 MPa to 8 MPa, and the extruder is operated at L/D 40:1 with specific energy input 0.15 kWh/kg to 0.25 kWh/kg. Underwater pelletizing at 20°C to 35°C produces uniform pellets for letdown ratios of 1% to 4% in HDPE and PP conversion lines. Above 50 wt% loading, dispersion uniformity becomes dependent on additive surface treatment and rheology; published data for this specific configuration is limited, and a higher MFI carrier is used in practice.

    General housewares and storage boxes produced from the same grade follow the thin-wall packaging profile; no separate processing window is required beyond a clamp force of 0.4 kN/mm² to 0.6 kN/mm² projected area and a mould temperature of 15°C to 30°C.

    Free Quote

    Competitive PCC (Iran) HDPE 62107 prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8618136850665 or mail to admin@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8618136850665

    Email: admin@ascent-chem.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    PCC (Iran) HDPE 62107 is a high-density polyethylene resin supplied primarily as natural or pigmented pellets in 25 kg bags or bulk containers. Distributor datasheets classify the grade as an extrusion blow moulding material with a melt flow rate of 0.70 g/10 min at 190 °C and 2.16 kg load under ISO 1133-1:2022, and a density of 0.962 g/cm3 under ISO 1183-1:2019. The resin is intended for industrial containers, large-volume packaging, automotive technical parts, and other thick-walled blow moulded articles where stiffness, melt strength, and environmental stress crack resistance must be balanced. The following data are representative distributor-reported values used for machinery sizing and material selection; they are not specification guarantees without the producer’s certificate of analysis.

    What Limits Molecular Weight Response in High-Density Polyethylene 62107?

    Molecular weight response is governed by the resin’s high average molecular weight and the resulting low melt flow. The 0.70 g/10 min melt flow rate places the material in the extrusion blow moulding range, where die swell and parison sag are controlled by chain entanglement and shear thinning. Typical tensile yield stress is 28 MPa under ISO 527-2:2012, elongation at break exceeds 800%, and flexural modulus is approximately 1,200 MPa under ISO 178:2019. Published data for the precise molecular weight distribution parameters of this specific grade are limited; however, the low melt flow and high density indicate a high-molecular-weight resin with a pronounced stiffness contribution. Polydispersity and branching should be verified indirectly through secant tensile modulus, melt strength, die swell, and extruder back-pressure trends on the target machine rather than predicted from melt flow alone.

    PropertyTest methodRepresentative value
    Melt flow rateISO 1133-1:20220.70 g/10 min at 190 °C, 2.16 kg
    DensityISO 1183-1:20190.962 g/cm3
    Tensile yield stressISO 527-2:201228 MPa
    Elongation at breakISO 527-2:2012>800%
    Flexural modulusISO 178:20191,200 MPa
    Notched Charpy impact at 23 °CISO 179-1:202012 kJ/m²
    Vicat softening point A50ISO 306:2022127 °C
    Environmental stress crack resistanceASTM D1693-15Published values vary; verify grade-specific datasheet

    Grade-specific environmental stress crack resistance values should be requested from the producer because the test condition, plaque preparation, and ageing history influence the result more than melt flow or density alone.

    Extrusion Blow Moulding Parameters on Accumulator-Head Tooling

    On accumulator-head machines, melt temperatures from 190 °C to 230 °C are typical; die temperatures are maintained between 200 °C and 220 °C to control die swell and weld-line integrity. Clamp force requirements are normally based on mold area, with blowing pressures in the range of 0.8–1.2 MPa and parison programming used to distribute wall thickness. Pre-drying is not normally required at relative humidity below 60%, but pellet surface condensation should be avoided by storage in unopened packaging; if moisture is suspected, drying at 80 °C for 2–3 h in a dehumidified hopper dryer is acceptable. Screw designs with length/diameter ratios of 24:1 to 36:1 and compression ratios of 2.5:1 to 3.5:1 are commonly recommended for high-molecular-weight HDPE. Grooved-feed sections are usually unnecessary on dedicated blow moulding lines but may be present on recycled-material lines. These values are typical industrial settings for HDPE blow moulding grades; no unique grade-specific optimisation is possible without on-machine trials.

    Mechanical integrity under stacked load is dominated by flexural modulus and creep resistance. The 1,200 MPa flexural modulus supports top-load requirements in 220 L tight-head drums, but creep rupture testing according to ISO 899-2:2003 should be used for legislative stacking performance because short-term modulus alone overestimates long-term container stiffness. Notched Charpy impact at 23 °C is approximately 12 kJ/m² under ISO 179-1:2020, and the low-temperature impact envelope should be confirmed for containers stored below -20 °C. Environmental stress crack resistance values for this grade must be checked against the actual test condition; high-molecular-weight blow moulding grades in this density range commonly show F50 values above 300 h under ASTM D1693-15 condition B in 100% Igepal, but published grade-specific values for this material are limited.

    When Wall Thickness Uniformity Governs Container Collapse Resistance

    Wall thickness distribution in accumulator-head blow moulding depends on parison profiling, die gap adjustment, and melt strength. A low melt flow of 0.70 g/10 min increases parison stability, but the operator must compensate for die swell through gap settings. For a 220 L drum with nominal wall thickness 4–6 mm, thickness variation should be kept below ±15% to avoid buckling under vacuum and hydrostatic load. In-mold calibration of the pinch-off weld is essential; clamping pressure and pinch geometry influence failure at the bottom weld. Published data for container collapse pressure measured on this specific grade are limited, so production qualification with ISO 12048:2001 packaging compression tests is required.

    Auditing Food-Contact and Dangerous Goods Compliance Against Migration Limits

    Food-contact use requires confirmation against resin-specific declarations. Polyethylene homopolymers are generally evaluated under FDA 21 CFR 177.1520 for olefin polymers, and European formulations must meet overall migration below 10 mg/dm² under EU No 10/2011 with simulant D1 or D2 depending on food type. Dangerous goods drum certification typically references UN 1H1 or UN 1H2 design types, with drop, stack, and hydraulic pressure tests under ADR/RID or IMDG requirements. Grade 62107 should not be approved for food or dangerous goods unless the converter’s specific article passes these end-product tests; resin compliance alone is not sufficient.

    Accumulator residence time above 15 minutes changes the molecular weight distribution.

    At accumulator-head machines, molten polymer can remain in the head and manifold for extended cycles. Thermal-oxidative degradation is most likely in the presence of oxygen and at melt temperatures above 230 °C. Gel particles, die lines, and viscosity reduction are early indicators. Purge with a high-density polyethylene purge compound at safe temperatures after each shutdown; titanium dioxide pigmented or carbon black masterbatches should be pre-dried and accurately dosed at 1–3 wt% to prevent agglomerates. No additional processing stabilizer is usually required for standard cycles, but regrind levels above 30 wt% can reduce environmental stress crack resistance and should be validated by bottle-drop and stress-crack testing according to ASTM D2463-15 for actual containers.

    The distinction from other high-density polyethylene grades is in melt strength and stress crack resistance. The 0.70 g/10 min melt flow provides higher parison stability than injection moulding grades with 5–20 g/10 min, which are formulated for short cycle times and thin-wall filling but exhibit lower melt strength. Compared with pipe-grade HDPE, 62107 has higher density and different long-term hydrostatic creep resistance characteristics. Grade-specific comparisons should use ISO 9080:2012 for pipe pressure performance, not blow moulding datasheet values.

    ParameterHDPE 62107Injection moulding HDPEPipe-grade HDPE
    Melt flow rate0.70 g/10 min at 190 °C, 2.16 kg5–20 g/10 min0.2–0.5 g/10 min at 5 kg or equivalent
    Density0.962 g/cm30.952–0.965 g/cm30.948–0.960 g/cm3
    Processing methodExtrusion blow mouldingInjection mouldingPipe extrusion
    Notched Charpy impact at 23 °C12 kJ/m²4–10 kJ/m²20–40 kJ/m²

    Regrind levels and weld-line integrity in commodity drums require particular attention. At pinch-off seams and handle welds, melt streams may carry external lubricants, pigments, or recycled material. A regrind fraction of 20–30 wt% is typical for closed-loop container production, but high-speed lines should validate each article with ASTM D2463-15 drop impact and ASTM D1693-15 environmental stress crack resistance tests. Pigment masterbatches based on incompatible carriers can form delamination layers in the weld zone, so carrier resin compatibility should be confirmed by scanning electron microscopy of the weld region. No claim of food-contact or dangerous goods suitability follows from regrind reuse; end-product certification remains mandatory.

    Top