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PCC (Iran) HDPE HB0035

    • Product Name: PCC (Iran) HDPE HB0035
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    VTB
    Specifications
    HS Code 527195
    Density 0.954-0.958 g/cm3
    Melt Flow Rate 0.35 g/10 min at 190°C/2.16 kg
    Melting Point 130-135 °C
    Crystallinity 70-80%
    Tensile Strength At Yield 25-30 MPa
    Elongation At Break >600%
    Flexural Modulus 1000-1400 MPa
    Izod Notched Impact Strength 20-60 kJ/m2
    Vicat Softening Point 120-125 °C
    Heat Deflection Temperature 75-85 °C
    Shore D Hardness 60-65
    Escr >1000 h
    Water Absorption <0.01%
    Thermal Conductivity 0.40-0.45 W/m.K
    Coefficient Of Linear Thermal Expansion 1.0-1.5 x 10^-4 /°C
    Dielectric Constant 2.3-2.4
    Volume Resistivity >10^16 ohm.cm
    Mold Shrinkage 2-3%
    Processing Temperature 180-220 °C

    As an accredited PCC (Iran) HDPE HB0035 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing PCC (Iran) HDPE HB0035 is typically packaged in 25 kg PP woven bags, 55 bags per pallet (1,375 kg).
    Container Loading (20′ FCL) Container Loading (20′ FCL): PCC (Iran) HDPE HB0035 in original 25 kg bags, palletized, shrink-wrapped, and ready for export.
    Shipping PCC (Iran) HDPE HB0035 is a non-hazardous high-density polyethylene resin. It is shipped as odorless pellets in 25 kg PP bags or 1,000 kg jumbo bags, palletized and stretch-wrapped, in 20-foot containers. Store dry, away from direct sunlight and heat; no special DG documentation required.
    Storage Store PCC (Iran) HDPE HB0035 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, sparks, and flames. Keep original packaging closed, clean, and palletized off the floor. Protect from moisture, dust, oils, and chemical contamination. Avoid prolonged UV exposure. Use first-in, first-out stock rotation, maintain good housekeeping, and do not stack excessively.
    Shelf Life PCC (Iran) HDPE HB0035 shelf life is typically 24 months when stored in unopened original packaging, away from sunlight, heat, and moisture.
    Application of PCC (Iran) HDPE HB0035

    What Governs Drop-Test Consistency in 200-L Tight-Head Drum Pinch-Off Zones?

    Drop-test consistency in 200-L tight-head drums blown from HB0035 is governed by flash trim temperature, parison thickness at the base pinch-off, and accumulator-head decompression. The resin is processed on single-station blow moulders with a clamp force of 1800–2200 kN and an extruder screw diameter of 120–150 mm. Barrel temperatures are profiled from 180 °C at the feed throat to 210 °C at the die; die head temperature is maintained at 190–205 °C. The accumulator head uses a diverging die gap of 2.5–5.0 mm and parison programming with 10–20 points to thicken the pinch-off and chime regions. Blow pressure is 0.6–0.8 MPa and mould cooling water is kept at 14–20 °C. A 200-L drum cycle is 180–240 s. Formulation often contains 2.0–2.5 % carbon black masterbatch for UV opacity and 0.8–1.5 % antioxidant additive package; regrind is limited to 25 % because higher levels reduce low-temperature drop performance at -18 °C. Drums are tested under UN 1H1 closed-head and UN 1H2 open-head provisions. Stack load is applied at 40 °C for 28 days under ADR 6.1.5.6. The base weld is the limiting defect location; if parison temperature at pinch-off drops below 190 °C, incomplete fusion produces cracks under the 1.2 m PG II drop test. A mould exhaust system with vacuum slots of 0.8–1.2 mm is required to prevent air entrapment at the drum rim.

    Fuel Tank Coextrusion with Post-Mould Fluorination Lives and Dies by Parison Geometry

    In automotive fuel tank production, HB0035 functions as the structural HDPE layer in six-layer coextrusion blow moulding. The layer structure from outer wall to inner wall is typically virgin HDPE, maleic anhydride-grafted LLDPE tie layer, EVOH barrier, regrind layer, tie layer, and virgin HDPE inner layer. Extruder diameters are 90–120 mm with L/D ratios of 30:1; melt temperatures for the HDPE layers are kept between 205 °C and 220 °C. The die head is designed for a 250–400 mm parison diameter with wall-thickness programming over 32 axial points. Blow pressure is 0.8–1.0 MPa; mould temperature is 8–15 °C. Post-mould fluorination is applied when monolayer tanks are produced without an EVOH barrier. The fluorine-containing process gas reacts to form a fluoropolymer-like barrier layer on the inner surface. Evaporative emission performance is evaluated by the SHED test under EPA 40 CFR Part 86 or ECE R34; published data for this specific HB0035 configuration is limited, so tank manufacturers validate permeation on production-intent parts. HB0035 is also used for SCR urea tanks and coolant reservoirs when coextruded with EVOH. The formulation excludes conductive carbon black unless a separate conductive layer is specified. Melt temperatures above 225 °C degrade the HDPE molecular weight and reduce weld-line fracture resistance in saddle inserts. The pinch-off line around the tank equator must be compression-cooled to below 120 °C before demoulding to prevent post-mould warpage.

    HB0035 from PCC Iran is a high-molecular-weight high-density polyethylene blow-moulding grade with a nominal melt flow rate of 0.35 g/10 min under ISO 1133-1:2022 at 190 °C/2.16 kg and a density range of 0.953–0.957 g/cm³ under ISO 1183-1:2019. For 20-L to 30-L UN-rated jerrican production, the material is processed on accumulator-head extrusion blow-moulding machines with screw diameters from 60 mm to 90 mm and L/D ratios of 24:1 to 30:1. Barrel zone settings from hopper to die are typically 170 °C, 190 °C, 205 °C, and 195 °C; melt temperature is held between 180 °C and 210 °C. The parison is programmed with a die gap of 1.8–3.2 mm and blown at 0.7–0.9 MPa into aluminium or beryllium-copper moulds chilled to 12–18 °C. Cycle time for a 25-L jerrican is 70–90 s depending on wall-stock distribution. Formulation uses 100 % virgin HB0035 or up to 20 % internally generated regrind from trimmed flash; outdoor-stable grades incorporate 1.5–2.5 % carbon black masterbatch and 0.1–0.3 % hindered amine light stabilizer. The resulting containers are tested as UN 3H1 jerricans for packing groups II and III. Drop testing at -18 °C from 1.2 m for PG II and 0.8 m for PG III is required by ADR 6.1.5.3; hydrostatic pressure testing at 95 kPa for 30 min and leakproofness testing are conducted on production samples. HB0035 is not specified without validation for strong oxidizing acids such as 98 % sulphuric acid or 30 % hydrogen peroxide. Regrind containing surface moisture should be predried at 80 °C for 2 h before reintroduction to prevent splay and pin-hole defects. Melt temperature above 220 °C for more than 20 min accelerates molecular weight loss and reduces environmental stress crack resistance.

    ApplicationMelt temperature °CDie head temperature °CBlow pressure MPaCycle time s
    25-L UN jerrican180–210185–2000.7–0.970–90
    200-L drum195–215190–2050.6–0.8180–240
    1000-L IBC inner bottle190–210185–2000.7–0.8300–420
    60-L fuel tank205–220200–2150.8–1.0150–210
    1–10-L pesticide bottle180–200175–1950.6–0.810–28

    The production of 1000-L IBC inner bottles from HB0035 is carried out on shuttle-type blow moulding machines with two or four stations. A typical inner bottle weighs 13–16 kg and has a wall thickness from 2.5 mm to 4.5 mm. Accumulator-head shot volume ranges from 15 L to 20 L; screw diameter is 120–150 mm and L/D ratio is 24:1 to 30:1. Barrel temperatures are 175–205 °C, die head temperature is 185–200 °C, and blow pressure is 0.7–0.8 MPa. Mould temperature is held at 10–16 °C to control surface finish and post-mould shrinkage. Cycle time is 300–420 s. For food-grade IBC liners, 100 % virgin HB0035 is required; for industrial chemical liners, up to 15 % dry internal regrind is accepted only if sieved through a 2 mm screen. The inner bottle is assembled into a steel tube frame and tested as UN 31H1. Food-contact compliance is referenced to FDA 21 CFR 177.1520 and EU Regulation 10/2011 only when the specific lot is confirmed by the producer. The main process defect is pinch-off flash tearing at the base; a die gap of 3.0–5.0 mm and parison programming with base thickening of 25–35 % reduce short-shot failure and sidewall thinning. HB0035 is not specified for concentrated ketones without immersion testing at 23 °C and 50 °C for 30 days in accordance with ASTM D543.

    Agricultural Pesticide Packaging ESCR and Light Stabilization Window

    Pesticide bottles from 0.5-L to 10-L are blown from HB0035 on continuous shuttle machines with die-head temperatures of 175–195 °C and mould temperatures of 8–15 °C. The formulation is adjusted for field storage: 75–85 % HB0035, 10–20 % LLDPE-C4 or LLDPE-C6, 2.0–3.0 % carbon black masterbatch, 0.1–0.3 % HALS, and 0.05–0.1 % zinc stearate. The LLDPE addition raises low-temperature drop resistance but reduces top-load stiffness; therefore top-load testing per ASTM D2659 is used to set the minimum shoulder thickness to 1.8–2.2 mm. Environmental stress crack resistance is evaluated by ASTM D1693 Condition B using 10 % Igepal CO-630 at 50 °C; supplier datasheet values for HB0035 should be verified on each production lot. Chemical compatibility is screened by ASTM D543 immersion at 50 °C for 30 days in actual pesticide formulations containing glyphosate, atrazine, 2,4-D, or chlorpyrifos. Leakproofness and drop tests are conducted per ADR 6.1.5 for PG III, with a drop height of 0.8 m at -18 °C. Long-term UV weathering is assessed by ISO 4892-2 Xenon-arc exposure for 500 h; unacceptable chalking or loss of impact indicates insufficient carbon black dispersion. HB0035 is incompatible with high-load nonylphenol ethoxylate surfactants and should not be used for solvent-based pesticide adjuvants unless a coextruded barrier is validated. The processing window is narrow: melt temperatures below 175 °C increase melt-fracture at the neck, while temperatures above 200 °C increase die-swell variation and reduce ESCR.

    When Solvent-Based Adhesive and Ink Bottles Demand Coextruded Barrier Layers in Place of Monolayer HB0035

    For aggressive solvent systems based on methyl ethyl ketone, toluene, acetone, or butyl acetate, monolayer HB0035 packaging may fail due to permeation or environmental stress cracking. In these applications, HB0035 is retained as the structural outer and inner layers in three-layer or five-layer coextrusion blow moulding. A typical five-layer structure consists of 35 % HDPE outer layer, 5 % maleic anhydride-grafted LLDPE tie, 10 % EVOH or PA, 5 % tie, and 45 % HDPE inner layer. The coextrusion die head temperature is 190–205 °C; each extruder is sized to match the layer ratio and equipped with gravimetric feeding. Bottles from 0.5-L to 5-L are blown at 0.6–0.8 MPa into moulds chilled to 10–14 °C. Delamination is controlled by maintaining a tie-layer thickness of not less than 2 % of total wall thickness and by matching melt viscosity at the layer interfaces. Post-mould adhesion is tested by peel testing after hot-fill simulation at 40 °C. These containers are used for offset printing ink, polyurethane adhesive components, and automotive sealant bottles. They are classified under ADR for flammable liquids and require leakproofness testing under UN 3H1 or UN 3H2. Published data for HB0035 in this specific coextruded configuration is limited; each barrier structure must be validated with the intended solvent at 40 °C for 28 days. HB0035 is not recommended for chlorinated solvents such as dichloromethane without a dedicated barrier and compatibility study.

    Heavy-gauge sheet extrusion from HB0035 is used for vacuum-formed chemical containment trays, battery boxes, and industrial dunnage. A 120-mm single-screw extruder with an L/D ratio of 33:1 feeds a flat die with a width of 1600–2200 mm. Melt temperatures at the die lips are 200–220 °C; polished roll stack temperatures are set at 70–90 °C for the upper and middle rolls and 50–70 °C for the lower roll. Sheet thickness is 2–6 mm. The sheet is thermoformed into trays with draw ratios below 1.5:1 to avoid corner thinning. Formulation includes 2.0–2.5 % carbon black for outdoor UV resistance and 0.2–0.5 % antioxidant masterbatch. Weld strength of formed corners is inspected by bend testing at -20 °C. Dimensional stability after forming is checked at 60 °C for 24 h; total shrinkage should not exceed 1.5 %. HB0035 is not used for high-gloss thin-gauge packaging sheet because its high molecular weight raises melt pressure and reduces output. Uneven roll temperatures above 10 °C differential produce warpage and internal stress. Published data for thermoformed HB0035 heavy-gauge sheet is limited outside of custom fabricator validation.

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    Certification & Compliance
    More Introduction

    PCC (Iran) HDPE HB0035 is supplied as a high-molecular-weight high-density polyethylene intended primarily for extrusion blow moulding of large, thick-walled containers. The nominal melt mass-flow rate is 0.35 g/10 min when measured at 190 °C under 2.16 kg load according to ISO 1133-1:2022, procedure A; the nominal density is 0.951 g/cm³ under ISO 1183-1:2019. The combination of low MFR and rigid density places HB0035 among HDPE grades used where parison stability, top-load stiffness and environmental stress crack resistance are production-critical. Typical downstream applications include 5–30 L stackable drums, automotive fuel tanks, industrial chemical containers and blow-moulded parts requiring high wall-thickness uniformity.

    What rheological response is observed at a melt index near 0.35 g/10 min during extrusion blow moulding?

    At 0.35 g/10 min, the melt exhibits higher zero-shear viscosity and longer relaxation time than HDPE blow moulding grades in the 0.6–1.0 g/10 min range. The practical consequence in continuous-extrusion and accumulator machines is reduced parison sag during the open-mold transfer sequence. Sag resistance is governed by extensional viscosity rather than shear viscosity alone; the high-molecular-weight fraction in HB0035 delays thinning at parison lengths above 500 mm, which is critical for 20–30 L container tools. On accumulator blow moulding machines with a 60 mm to 90 mm single-screw extruder and a die gap of 1.5–3.0 mm, die swell is typically higher than for HDPE grades with MFR above 0.7 g/10 min; the die gap and mandrel clearance must therefore be adjusted to maintain wall-thickness distribution. Melt strength is also temperature-dependent: a die-head temperature below 190 °C increases pressure and may cause melt fracture, while a melt temperature above 230 °C reduces parison integrity and increases oxidative degradation. Industrial experience with similar low-MFR HDPE grades shows that die-zone temperature uniformity should be controlled within ±2 °C across the die circumference to avoid spiral weld lines and uneven thickness.

    Where HB0035 is run on single-station shuttle machines producing 20 L containers, the parison programmer is typically set to modify die gap through 60–80 % of the parison length to compensate for weight distribution. The low MFR increases head pressure; at a screw speed of 25 rpm on a 60 mm extruder, die-head pressures in the range of 200–300 bar are common for similar HDPE blow moulding grades, although published data for this specific configuration is limited. Narrowing the die gap below 1.2 mm at this viscosity can generate excessive backpressure, melt fracture and localized overheating. Converters should monitor head pressure and melt temperature at the die entry rather than relying solely on barrel set points; deviations above 250 bar may indicate insufficient die gap or insufficient melt temperature.

    Barrel temperature profiles, die-head pressure, and screw speed on single-screw accumulator machines

    Processing should be initiated with barrel zone set points of 180 °C in the feed section, 190–200 °C in the compression section, and 200–210 °C in the metering section; the head and die zones are maintained at 190–210 °C. The feed throat requires water cooling below 60 °C to prevent premature melting and hopper bridging. Single-screw extruders with L/D ratios of 24:1 to 30:1 and grooved feed bushes are preferred because the higher pressure-generation capacity improves melt homogeneity at low MFR. Screw speeds are typically limited to 20–40 min⁻¹ for a 60 mm screw; higher speeds may raise melt temperature above 230 °C through viscous dissipation, at which point oxidative degradation shifts the molecular weight distribution and reduces ESCR. The melt temperature measured by needle pyrometer at the die exit is preferably between 190 °C and 220 °C; lower temperatures increase head pressure and can roughen the parison surface, while higher temperatures cause parison drawdown and odour. Because the grade is stiff and viscous, melt pumps are not typically used in accumulator blow moulding; the extruder must deliver a homogeneous melt directly to the accumulator head without surging.

    Environmental stress crack resistance is governed by density and processing history, not by MFR alone

    Under ASTM D1693-15, HDPE blow moulding grades with density near 0.950 g/cm³ typically show F50 values above 100 h in 100 % Igepal CO-630; supplier lot data for HB0035 should be obtained because ESCR varies with comonomer content, molecular weight tail and internal stress from processing. The density of 0.951 g/cm³ is high enough to provide top-load stiffness but lower than high-density grades above 0.960 g/cm³, retaining resistance to slow crack growth in notched areas. Containers moulded from HB0035 are generally suitable for neutral, acidic and caustic packaging at ambient temperature; aggressive organic solvents, strong oxidizing acids and liquid hydrocarbons above 60 °C require specific chemical resistance testing under ISO 175:2021, because a generic compatibility table does not replace immersion testing of the final blow-moulded part. For automotive fuel tanks, HB0035 is typically extrusion blow moulded as a monolayer and then fluorinated or coextruded with an EVOH barrier; neat HDPE does not provide sufficient hydrocarbon permeation resistance for modern evaporative emission limits under UN ECE R34. Wall-thickness distribution in such parts should be verified by ultrasonic thickness mapping, with a minimum wall thickness no lower than 2.0 mm in the pinch-off zone for 20 L drums unless the tool trial establishes otherwise.

    When HB0035 is benchmarked against higher-MFR HDPE grades

    Compared with blow moulding HDPE grades having an MFR of 0.7 g/10 min to 1.0 g/10 min, HB0035 displays a narrower processing window and longer cycle time but improved parison integrity in large-part tools. The lower MFR increases viscosity and head pressure, which reduces throughput per revolution on a 60 mm extruder; processors may need to increase screw speed by 10–20 % or raise barrel temperature by 5–10 °C to match output. In comparison with injection moulding HDPE grades having MFR above 4 g/10 min, HB0035 is unsuitable for thin-wall injection moulding because spiral flow length at a given injection pressure is significantly shorter; published data for this specific configuration is limited, but the difference in MFR is itself a standard indicator of flow-path capability under ISO 1133-1:2022. Stiffness and chemical resistance are similar to those of other pelletized HDPE grades with density 0.951 g/cm³, but the low MFR makes HB0035 less forgiving of poor die-head temperature uniformity or fast clamp transfer sequences.

    Typical property profile from supplier documentation

    PropertyMethodNominal valueUnit
    Melt mass-flow rate at 190 °C/2.16 kgISO 1133-1:20220.35g/10 min
    DensityISO 1183-1:20190.951g/cm³
    Tensile stress at yieldISO 527-2:201226MPa
    Tensile elongation at breakISO 527-2:2012>800%
    Flexural modulusISO 178:20191050MPa
    Charpy notched impact strength at 23 °CISO 179-1:201025kJ/m²
    Vicat softening temperature A50ISO 306:2022127°C
    Shore D hardnessISO 868:200362dimensionless

    Regulatory status under REACH, RoHS, food-contact and potable-water schemes should be verified with PCC lot documentation. Food-contact status is not automatic; the base resin may be evaluated under FDA 21 CFR 177.1520 and EU Regulation 10/2011, but the final article must be tested for migration and organoleptics under the intended conditions of use. If the grade is used in packaging, the converter should request a compliance statement for the specific lot rather than relying on generic grade information.

    Lot certification should include at minimum MFR, density, tensile yield, flexural modulus and Charpy impact. The supplier’s certificate of analysis is expected to show batch-to-batch MFR variation controlled within ±0.03 g/10 min and density variation within ±0.002 g/cm³; if such data are not available, a pre-production trial on the target accumulator machine is required before release. HB0035 pellets are non-hygroscopic; drying is not required if stored at ambient conditions below 50 % RH, but if surface condensation occurs, dehumidified-air drying at 60–70 °C for 1–2 h is recommended to prevent splay. The material should be kept free of contamination from polypropylene, PET and incompatible colour concentrates because melt-phase incompatibility causes delamination, pinholes and reduced ESCR in formed parts. Masterbatches intended for HDPE blow moulding must be evaluated for migration kinetics; additives with high-flow carriers can reduce melt strength at the parison surface and should not exceed 2 % of the total compound unless rheological testing confirms stability.

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