Products

PCC (Iran) HDPE 5000S

    • Product Name: PCC (Iran) HDPE 5000S
    • 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 551465
    Density 0.954 g/cm³
    Melt Flow Rate 190 C 2 16 Kg 0.9 g/10 min
    Melting Point 131 °C
    Vicat Softening Point 122 °C
    Crystallinity 70-80%
    Tensile Strength At Yield 27 MPa
    Elongation At Break >600%
    Flexural Modulus 1100 MPa
    Notched Izod Impact Strength 30 kJ/m²
    Shore D Hardness 62
    Water Absorption <0.01%
    Thermal Conductivity 0.42 W/m·K
    Dielectric Constant 2.3
    Volume Resistivity >10^16 Ω·cm
    Brittleness Temperature < -70 °C
    Environmental Stress Cracking Resistance >1000 h
    Molecular Weight Distribution Wide
    Form Pellets
    Color Natural/White
    Odor Odorless

    As an accredited PCC (Iran) HDPE 5000S factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing PCC (Iran) HDPE 5000S is packaged in 25 kg PP woven bags with PE liner, 1,000 kg per pallet (20 MT per 20-ft container).
    Container Loading (20′ FCL) Container loading (20′ FCL) of PCC (Iran) HDPE 5000S: 25 kg bags, palletized, shrink-wrapped, secured, approximately 22 MT net.
    Shipping PCC (Iran) HDPE 5000S is shipped as non-hazardous general cargo, typically in 25 kg PP woven bags, palletized and stretch-wrapped. Standard 20' containers hold about 17–18 MT. Keep dry, away from heat, sunlight, and moisture; moisture-barrier liners are recommended. Suitable for sea freight under normal conditions.
    Storage Store PCC (Iran) HDPE 5000S 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 contact with strong oxidizers. Protect pallets from physical damage and stack securely. Do not expose to prolonged UV radiation. Maintain clean, dry conditions; no special temperature control required under normal storage.
    Shelf Life PCC (Iran) HDPE 5000S shelf life is typically 24 months when stored unopened, cool, dry, well-ventilated, away from direct sunlight and heat.
    Application of PCC (Iran) HDPE 5000S

    PCC (Iran) HDPE 5000S is supplied as a high-density polyethylene injection moulding grade with a published melt flow rate of 0.9 g/10 min at 190 °C/5 kg per ISO 1133-1:2022 and a density of 0.952 g/cm³ per ISO 1183-1:2019. The downstream route with the largest installed base is heavy-duty industrial containers, pallets, and distribution crates. In tools producing parts with masses above 3 kg and nominal wall stock from 6 mm to 14 mm, the material is moulded on reciprocating-screw machines with clamp forces from 800 t to 2,500 t, polyolefin screws of L/D 20:1–25:1, and compression ratios between 2.5:1 and 3.0:1. The low MFR imposes melt temperatures at the nozzle of 200 °C to 220 °C for complete rib fill-out. When environmental stress cracking resistance in detergent-exposed crates is prioritized, nozzle melt temperature is often reduced to 190 °C to 200 °C, accepting an increase of 10–20 bar in peak hydraulic pressure. Mould temperature is maintained at 10 °C to 30 °C to shorten the conduction-limited cooling plateau. Total cycle time for a pallet deck with 10–15 mm nominal thickness typically falls between 180 s and 300 s; common on-line defects are ejector pin marks, sink marks at rib intersections, and bottom-side flash at the core pins.

    Mechanical acceptance of these pallets follows ISO 8611-1:2021 for rated loads and, where relevant, ISO 8611-2:2021 for performance requirements. Tensile yield strength of HDPE 5000S is typically reported in the 22–26 MPa range under ASTM D638-14 at 50 mm/min, with elongation at break above 500%. Weld lines formed downstream of multiple gates or hot-runner drops in pallet grids are the main mechanical weak points. For this grade, weld-line strength retention improves when melt temperature is raised to 220–230 °C, holding pressure is set at 60–80% of peak injection pressure, and gate positions shift the weld line to low-stress floor areas. Cooling below 10 °C is not recommended because weld-line elongation may fall below the level required for racking impact under cold-chain loading.

    Can the low-MFR rheology pass UN packing group II drop conditions in open-head pails?

    Open-head pails injection moulded from HDPE 5000S generally use sidewall thicknesses between 2.0 mm and 3.5 mm and capacities up to 30 L. The grade's high melt strength reduces flash at the lid-sealing lip and permits a broad process window, but its low MFR demands elevated injection pressure to fill the circular sidewall and handle bosses. Production lines typically set barrel temperatures from 210 °C to 240 °C at the nozzle and injection velocities sufficient to maintain flow-front speed above 100 mm/s; speeds below this threshold generate premature gate freeze and short moulded hinge pins. Holding pressure is staged downward from 50 bar to 35 bar over 5–8 s. Mould temperature is clamped between 12 °C and 25 °C to control radial shrinkage of the lid channel.

    For pails intended for dangerous goods, the moulded part is qualified under the UN performance tests referenced in ADR/RID Chapter 6.1 and the UN Manual of Tests and Criteria, Part III. Packing group II liquid containers are drop-tested from 1.2 m on the bottom, top edge, and seam; leakage after impact constitutes failure. The environmental stress crack resistance of HDPE 5000S, evaluated by ASTM D1693-15 Condition B in 10% Igepal CO-630 at 50 °C, supports post-drop hydraulic leakproofness, but the low MFR can reduce molecular orientation in thin sidewalls. Processors therefore use a central valve gate and higher injection velocity to preserve orientation. Sidewall thickness below 2.0 mm should be avoided where stacking loads exceed 250 kg; the bottom corner radius is maintained above 2.0 mm to prevent notch-induced environmental stress cracking near the gate.

    Food-contact pails further require compliance with FDA 21 CFR 177.1520 and, in the EU, Regulation (EU) No 10/2011 with overall migration below 10 mg/dm². Only approved stabilizers and colour concentrates are permitted, and external lubricants that can induce stress cracking or lid-seal leakage are excluded. The lid gasket, if present, is moulded from a flexible elastomer rather than HDPE 5000S; the pail sealing lip is held to a diametric tolerance of ±0.3 mm to maintain compression. Temperature control of the mould is therefore a first-order variable, and cycle-time reduction is curtailed when the lip tolerance is narrow.

    Outdoor waste-container moulding shifts the technical risk from short-term tensile overload to long-term environmental stress cracking and ultraviolet degradation. Moulded waste bins with capacities from 120 L to 1,100 L are produced from HDPE 5000S in injection machines up to 4,000 t clamp force, frequently with a single injection point at the bin bottom and sequential valve gates along the tall sidewalls. Melt temperature is set at 200 °C to 220 °C, mould temperature at 10 °C to 20 °C, and total cycle times run from 240 s to 420 s depending on wall thickness from 4 mm to 8 mm. UV stabilization is obtained with carbon black loadings of 2.0–2.5 wt% for black bodies, or hindered amine light stabilizer packages for coloured mouldings; both additive routes raise melt viscosity slightly and require 5–10 bar of additional injection pressure.

    Mechanical acceptance often references EN 840-1:2020 for mobile waste containers, including body, lid, and drop tests, and ASTM D256-23 Izod impact at −18 °C for low-temperature toughness. The high molecular weight of HDPE 5000S gives better sub-zero impact than MFR > 2 g/10 min grades; notched Izod values are expected above 15 kJ/m² in sound sections, but values below 10 kJ/m² are observed when weld lines coincide with hinge bosses. Accelerated weathering validation is conducted under ASTM G154-16 UVA-340 cycles with 0.77 W/m² irradiance at 60 °C black panel, and colour shift is evaluated per ASTM D2244-16. The main moulding defect is inner-wall sink marks opposite thick handle attachment points; gas-counterpressure or increased packing pressure suppresses them. Because HDPE 5000S is unfilled, long-term creep under bin-lifting arms must be controlled by ribbing and wall-stock design rather than by fibre reinforcement.

    When injection speed exceeds 40 mm/s in multi-cavity thin-wall household ware

    Household storage boxes, drawer organizers, and food containers made from HDPE 5000S often use wall stock from 0.9 mm to 2.0 mm, which is at the lower flow limit for a low-MFR grade. Flow-path-to-wall-thickness ratios in multi-cavity tools frequently exceed 150:1, forcing injection speed above 40 mm/s and peak injection pressures near 100–120 bar on hydraulic machines or 80–100 MPa specific pressure at the screw tip. Mould temperature is held at 20 °C to 35 °C and hot-runner manifold temperature at 210 °C to 230 °C to delay gate freeze. Unlike fast-cycling HDPE grades with MFR above 4 g/10 min, 5000S cannot be processed below 190 °C without severe short shots in thin ribs. If melt temperature is raised above 240 °C, warpage increases because differential shrinkage between flow and transverse directions reaches 0.3–0.8% in this grade family.

    Food-contact housewares require compliance with FDA 21 CFR 177.1520 and Regulation (EU) No 10/2011. Dishwasher-exposed articles are cyclically tested at 70–85 °C in a typical household detergent solution for 100–200 cycles; detergent stress cracking is assessed by in-house methods adapted from ASTM D1693-15 because the standard fluid is not a food-contact detergent. Gate position is critical: a tunnel gate into a thin sidewall can produce local shear degradation, visible as yellowing and reduced notched Izod impact. A fan gate into a thickened base is preferred. The practical process floor for this family is narrow, with melt temperature maintained between 200 °C and 215 °C to balance complete filling against post-mould warpage.

    Automotive under-hood reservoirs and glycol contact: post-mould shrinkage and weld-line integrity

    Automotive injection mouldings made from HDPE 5000S include windscreen washer reservoirs, coolant expansion tanks, and battery trays. These parts combine wall thicknesses from 2.0 mm to 4.5 mm with long flow lengths and multiple moulded-in brass or stainless steel inserts. Processing is carried out at melt temperatures of 200 °C to 230 °C and mould temperatures of 15 °C to 30 °C. Post-demoulding shrinkage is normally 1.5–2.5% in the flow direction and 1.0–2.0% transverse; this anisotropy must be compensated in tool steel dimensions. The main defect is weld-line cracking at insert bosses: when the melt front splits around an insert and rejoins, the weld line in HDPE 5000S retains only 40–60% of sound-part tensile strength unless melt temperature is raised to 225–235 °C and holding pressure is maintained until gate freeze.

    Chemical resistance to glycol-water mixtures is evaluated using long-term hydrostatic strength protocols aligned with ISO 9080:2012 and environmental stress cracking assessments under ISO 22088-2:2006. HDPE 5000S is accepted for 50/50 ethylene glycol/water service at 90 °C, but continuous exposure above 105 °C requires a higher-density or crosslinked grade. Unfilled HDPE 5000S limits dimensional stability under bonnet soak temperatures; parts should not be mounted where local air temperature exceeds 95 °C for uninterrupted service. Under-hood vibration tests commonly require bracketed ribs to withstand 10⁶ cycles at 25–50 Hz, and the high molecular weight of the grade provides better fatigue resistance than lower-MFR injection grades. Published data for this specific component configuration is limited; finished-part validation is therefore required instead of direct extrapolation from resin datasheet values.

    As a low-risk application family, solid flat-bottom nesting boxes with wall thickness above 3 mm require only standard injection moulding at 190 °C to 210 °C melt temperature and 15 °C to 25 °C mould temperature, followed by no post-processing other than gate vestige deflashing.

    Industrial cable spools, separator plates, and material-handling trays are injection moulded from HDPE 5000S where processing oil exposure and repeated mechanical handling eliminate glass-filled polypropylene. The spool flanges are 8–12 mm thick and the hub walls are 5–8 mm; injection is performed on machines of 1,000–2,000 t clamp force using a centre sprue or multiple submarine gates in the hub. Because the grade's MFR is low, screw back pressure is maintained at 8–12 bar and the barrel profile is set from 180 °C at the feed throat to 220 °C at the nozzle to avoid excessive shear heating in the compression zone. Mould temperatures are held at 15 °C to 25 °C to control sink marks on the flanges. Resistance to non-aromatic mineral oil is tested by immersion at 70 °C for 72 h per ISO 175:2010; tensile strength retention in HDPE 5000S generally exceeds 80% in this fluid class.

    Flange flatness is measured after conditioning at 23 °C and 50% RH for 48 h per ISO 291:2008; a tolerance of ±0.8 mm across a 500 mm flange diameter is common in cable spool specifications. Warpage above this limit is usually caused by non-uniform mould cooling or premature ejection. Because HDPE 5000S exhibits mould shrinkage around 1.5–2.0%, tools cut for polypropylene shrinkage produce undersized spools when converters switch from PP to HDPE without retooling. No hygroscopic drying is required, but pellet condensation in unheated silos at RH > 80% can create surface streaks; pellets should be maintained above 15 °C before entering the feed throat. Heavy-metal and phthalate restrictions for export cable components are addressed by REACH Annex XVII and 2011/65/EU RoHS Recast declarations.

    Free Quote

    Competitive PCC (Iran) HDPE 5000S 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 5000S is a high-molecular-weight high-density polyethylene homopolymer classified for blown-film extrusion and heavy-duty packaging. The product is supplied in pellet form and normally characterized by a nominal density of 0.954 g/cm³ under ISO 1183-1:2019 and a melt mass-flow rate in the range 0.25–0.35 g/10 min at 190 °C/21.6 kg under ISO 1133-1:2022. The 21.6 kg high-load condition is used because the standard-load melt flow rate is too low for reliable process-control measurement in this molecular-weight class. Published reactor-specific data for catalyst residue, comonomer content, and molecular-weight distribution are limited; the commercial profile is consistent with a low-pressure slurry-loop HMW film resin. The grade is supplied without slip or antiblock additives, so surface performance and blocking resistance must be introduced downstream by the converter using masterbatch or pre-blended concentrates.

    What nominal specifications and test methods govern PCC HDPE 5000S?

    The following values are typical for commercial HMW film-grade production and are not batch-release specifications. Film property values depend on die gap, blow-up ratio, frost-line height, gauge control, and downstream orientation. Comparative film data below refer to 25 µm blown film produced at a 2:1 blow-up ratio.

    PropertyTest methodUnitTypical value or range
    Melt mass-flow rate at 190 °C/21.6 kgISO 1133-1:2022g/10 min0.25–0.35
    DensityISO 1183-1:2019g/cm³0.953–0.956
    Tensile stress at yieldISO 527-3MPa24–28
    Tensile stress at breakISO 527-3MPa33–40
    Elongation at breakISO 527-3%600–800
    Dart drop impact F50 on 25 µm filmISO 7765-1 method Ag150–200
    Elmendorf tear resistance MD/TD on 25 µm filmISO 6383-2mN250–350 / 400–550
    Vicat softening temperature A50ISO 306:2022°C124–127
    Shore D hardnessISO 868—62–65

    The density of 0.953–0.956 g/cm³ places the resin in the stiffness range required for downgauged heavy-duty sacks. Actual water-vapour transmission rate must be determined on the finished film under ISO 15106-3 or a customer-specific cup test because seal geometry, gauge, and film orientation dominate the barrier contribution. The melt mass-flow rate at 21.6 kg should not be compared directly with injection-moulding HDPE grades measured under 2.16 kg; the high-load value is used as a processing-control indicator for high-molecular-weight film resins.

    On a 63.5 mm grooved-feed single-screw extruder with an L/D ratio of 30:1 and a barrier-type screw, the grade is processed within a barrel-temperature profile of 180–220 °C from feed throat to metering zone; head and die setpoints are normally held at 210–230 °C. Melt pressure measured upstream of the screen changer falls in the range 25–35 MPa depending on screw speed, screen-pack resistance, and melt temperature. A screen-pack combination of 20/40/60 mesh is typical for HMW film-grade HDPE to provide back-mixing and gel retention. The die gap is normally set between 1.2 mm and 2.0 mm; blow-up ratio is maintained between 3:1 and 5:1 to orient the film and develop machine-direction and transverse-direction properties. Frost-line height is typically 6–9 die diameters above the air ring. Under these conditions, the bubble exhibits sufficient melt strength to resist burst and flutter; however, a reduction in melt temperature below 190 °C can produce surface roughness associated with melt fracture, while sustained melt temperatures above 230 °C promote oxidative gel formation and off-odour. The resin does not normally require predrying. If bags have been damaged or pellets are stored under condensation risk, surface moisture can be removed by a 2 h hopper-dryer residence at 70 °C. Flood-fed extruder operation is preferred, and extruder residence time should be kept below 8 min to limit degradation and gel-spot formation.

    When HDPE 5000S Replaces a Conventional Low-MFI HMW Film Resin

    The principal difference from general-purpose injection-moulding HDPE is melt rheology. Injection-moulding grades typically show a standard-load melt flow rate above 8 g/10 min at 190 °C/2.16 kg, whereas HDPE 5000S under the same low-load condition is below the practical detection limit for routine quality control. The high molecular weight of HDPE 5000S provides elevated melt strength and bubble stability in high-BUR blown-film operation, but it produces excessive melt pressure and poor flow in thin-wall injection tooling. A processor replacing a 0.2–0.5 g/10 min high-load-MFR HMW film resin should hold the same blow-up ratio but check die-lip deposit and melt pressure; adjustments of ±5 °C in the barrel and die zones are typical. Compared with high-alpha-olefin LLDPE film grades of density 0.916–0.920 g/cm³, HDPE 5000S exhibits higher yield stress and tensile stiffness under ISO 527-3, but lower dart-impact and Elmendorf tear capacity under ISO 7765-1 and ISO 6383-2. Compared with bimodal HDPE grades used in pressure pipe and specialized film, the product is not formulated with carbon black or UV stabilizer and is not intended for PE100 pressure-pipe hydrostatic design. Within the producer’s grade slate, HDPE 5000S is distinct from blow-moulding HDPE by lower melt flow and from pipe grades by the absence of a long-term stabilizer package.

    Heavy-duty sack applications require dart drop impact above 150 g and machine-direction Elmendorf tear values above 300 mN under ISO 6383-2; typical film produced from HDPE 5000S under the described conditions falls within this envelope for gauges between 20 µm and 60 µm. T-shirt carrier bags produced at 12–18 µm gauge rely on the resin’s melt strength to maintain bubble stability at thin gauge; downgauging below 10 µm without a post-die air ring can lead to gauge variation and die-lip oxidation. Freezer film and industrial liners exploit the density-related puncture resistance and low glass-transition behaviour of HDPE. The brittleness temperature under ASTM D746 is below -76 °C, permitting film flexibility in frozen storage. In secondary conversion, the base resin can be corona-treated to improve adhesives and printing inks; surface tension should be raised to at least 38 mN/m under ISO 8296 for solvent-based lamination. However, the absence of slip and antiblock in the base resin means that blocking force under ASTM D3354 must be controlled by additive masterbatch before rollstock is produced.

    Limits for Moisture Tolerance, Additive Compatibility, and Secondary Conversion

    The base olefin polymer falls under FDA 21 CFR 177.1520 as an olefin polymer, but the finished food-contact article must be validated for migration under the intended conditions of use; no blanket approval applies to added masterbatches, adhesives, inks, or processed regrind. Conformity with EU Regulation (EU) No 10/2011 on plastic food-contact materials must be established on the finished film, not on the raw resin alone. The product should not be dry-blended with high loadings of low-density elastomers such as EVA above 10 wt% without compatibilization, because phase separation reduces tear resistance and creates visible flow marks. Polypropylene contamination from mixed recycling streams should be kept below 5 wt%; higher levels form discrete PP domains that reduce impact strength and film optics. The resin is not designed for intentional crosslinking with peroxide, silane, or irradiation, and oxidative induction time under ISO 11357-6 should be verified when regrind exceeds 30%. Processing with excessive residence time or melt temperatures above 230 °C may produce gel specks and a measurable decline in dart impact. The material is not recommended for injection-moulded closures, rotomoulded tanks, or extrusion blow-moulded containers because the high molecular weight and low melt flow produce excessive backpressure and inadequate volumetric fill in those processes.

    Top