Equate Hdpe Hdf3000

EQUATE HDPE HDF3000

    • Product Name: EQUATE HDPE HDF3000
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 966935
    Density 0.954 g/cm³
    Melt Flow Index 0.30 g/10 min (190°C/2.16 kg)
    Melting Point 131 °C
    Vicat Softening Point 122 °C
    Tensile Strength At Yield 26 MPa
    Tensile Strength At Break 37 MPa
    Elongation At Break 600%
    Flexural Modulus 1100 MPa
    Notched Izod Impact Strength 50 kJ/m²
    Shore D Hardness 62
    Water Absorption <0.01%
    Thermal Conductivity 0.45 W/m·K
    Dielectric Constant 2.3
    Volume Resistivity >10^16 ohm·cm
    Brittleness Temperature <-70 °C
    Environmental Stress Crack Resistance >1000 h

    As an accredited EQUATE HDPE HDF3000 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing EQUATE HDPE HDF3000 is packaged in 25 kg polyethylene bags, with 55 bags per pallet, totaling 1,375 kg net.
    Container Loading (20′ FCL) 20′ FCL container: EQUATE HDPE HDF3000, 25kg bags, 40 bags/pallet, 18 pallets, 18 MT net, securely loaded.
    Shipping EQUATE HDPE HDF3000 is shipped as non-hazardous high-density polyethylene resin pellets, typically in 25 kg bags, octabins, or bulk trucks/containers. Store in a dry, clean area away from direct sunlight and ignition sources. No UN hazmat classification required. Transport per local regulations; maintain package integrity to prevent spills.
    Storage Store EQUATE HDPE HDF3000 in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep original bags or containers sealed and palletized off the ground to prevent moisture and contamination. Avoid prolonged UV exposure, extreme temperatures, and contact with oxidizing agents. Stack securely to prevent deformation or package damage. Maintain good housekeeping and follow local regulations.
    Shelf Life Shelf life is typically 12 months when stored in original packaging, cool, dry, well-ventilated, and away from direct sunlight.
    Application of EQUATE HDPE HDF3000

    In 220 L tight-head drum manufacture, EQUATE HDPE HDF3000 is processed on an 80 mm single-screw extruder with 30:1 L/D and a grooved-barrel feed section. Barrel zones from feed to adapter are set at 180°C, 190°C, 200°C, 210°C, and 215°C, while die zones are held at 205–210°C. A 15 kg accumulator head delivers a 9.2 kg parison at a shot rate of 1.3–1.5 kg/s. Parison programming uses die gap 3.6 mm at the top, 2.7 mm in the centre, and 4.8 mm at the bottom to offset swell and sag gradients across the 880 mm cylindrical body. Mould close speed is set at 500 mm/s, pre-blow is delayed 0.3 s after mould contact, and blow air enters at 7.5 bar. The finished 220 L tight-head drum maintains a minimum wall of 4.0 mm on the cylinder, 5.2 mm at the top chime, and 5.8 mm at the bottom chime. The product is a UN 1H2/Y1.9/150/24 container for bulk liquid chemicals, detergents, and agricultural emulsions.

    Regrind ratio for non-UN packaging may reach 30–40 wt% when post-industrial regrind is screened to 3–5 mm granules and blended in-line before the hopper. For UN-certified drums, regrind addition is limited to 25 wt% and drawn exclusively from the same HDF3000 lot family, because ASTM D1693 Condition B F50 shifts below 300 h when the blend contains lower-molecular-weight high-density polyethylene. Colouration is controlled with 2.0–2.5 wt% of a linear low-density polyethylene-based masterbatch; outdoor-stored containers require an additional 0.5–1.0 wt% UV stabiliser concentrate. Moisture on pellet surfaces from high-humidity silos is removed with a hopper dryer at 70°C for 2 h only when the pellet surface condensation exceeds 0.2 wt%. The vented barrel and grooved feed zone reduce the risk of melt-pressure fluctuation, but accumulative shot weight control is held within ±0.15 kg to avoid bottom-chime thinning.

    Density, 23°CISO 1183-1:20190.952 g/cm³
    High-load melt index, 190°C/21.6 kgISO 1133-1:20225.8 g/10 min
    Tensile yield, 50 mm/minISO 527-227 MPa
    Flexural modulusISO 1781100 MPa
    Charpy notched impact, 23°CISO 179-122 kJ/m²
    Environmental stress-crack resistance, F50ASTM D1693, Condition B600 h minimum
    Food-contact statusFDA 21 CFR 177.1520Olefin polymer, no migration above 0.5 mg/in²

    The certified 220 L drum is drop-tested at 1.9 m and −18°C under UN Chapter 6.1 procedures, with no leakage after two drops. Stacking performance is validated according to ISO 2234 using a 3-high stack held for 24 h at 40°C. The seam flash is reduced to 1.5–2.0 mm after deflashing, and the L-ring chime is compressed with a post-mould pressing station to limit ovality below 1.5% of nominal diameter.

    In 1,000 L composite intermediate bulk container liner production, HDF3000 is blow moulded at a shot weight of 15–16 kg and a parison length of 2200 mm. The accumulator head uses a diverging tooling set with die gap 4.2 mm at the tail and 3.2 mm at the shoulder, sequenced through 18 wall-thickness points. A single-station shuttle clamp with 200 t clamp force closes at 450 mm/s. Blow air is applied at 8.0 bar with pre-blow delay of 0.4 s. The liner wall is held to 3.0 mm minimum on the sidewall, 4.5 mm at the base, and 5.0 mm at the top flange. The terminal component is a 1,000 L inner bottle for a composite IBC, certified as UN 31HA2/Y for liquids with relative density up to 1.5 and vapour pressure below 200 kPa at 55°C. Leak testing is performed at 20 kPa air pressure under water immersion.

    The IBC liner formulation uses 20–25 wt% in-house regrind from the same liner production stream, screened to 4 mm maximum particle size. Because the liner must survive rail and road vibration, the regrind source is restricted to lots with ASTM D1693 F50 above 500 h. A blue or natural masterbatch is dosed at 1.5–2.0 wt%. Screw speed on the 90 mm extruder with 30:1 L/D is maintained at 55–65 rpm, with barrel temperatures from 180°C to 210°C and head temperature at 205°C. Cooling water to the mould is supplied at 15–20°C with turbulent flow above 2.5 m/s in the aluminium channels. Cycle time for the liner is 140–160 s, excluding deflashing and top-flange trimming. The liner is integrated into a steel or wire cage, and the filled assembly is subjected to bottom lift, top lift, stacking, and drop tests under UN Chapter 6.5.

    What Limits Cycle Time When Six-Layer Barrier Coextrusion Replaces Monolayer Fuel Tank Blow Moulding?

    When HDF3000 is used as the outer and inner skins of a six-layer automotive fuel tank, the processing envelope is constrained primarily by the residence-time margin of the ethylene-vinyl alcohol copolymer barrier layer. The EVOH layer is pre-dried at 80°C for 4 h to a moisture content below 0.1 wt%, because retained moisture reduces melt strength and creates pinholes at the die lip. The HDF3000 skins require no drying unless the pellet surface has visible condensation. A 90 mm single-screw extruder with 30:1 L/D feeds the outer HDPE layer, while a second 60 mm extruder feeds the inner HDPE layer and regrind stream. The six-layer accumulator head is sized for 10 kg shot weight and is purged after every 48 h of continuous operation to prevent polymer degradation at the manifold boundaries.

    Layer positionMaterialWeight percent range
    Outer skinEQUATE HDPE HDF3000 + 2.0 wt% carbon black masterbatch25–30
    Regrind layerPost-industrial tank regrind from same six-layer structure25–30
    Tie layerMaleic anhydride-grafted polyethylene1.5–2.5
    Barrier layerEthylene-vinyl alcohol copolymer, 32 mol% ethylene1.5–2.5
    Regrind layerPost-industrial tank regrind25–30
    Inner skinEQUATE HDPE HDF3000 + conductive carbon black concentrate15–20

    Outer-layer HDF3000 is processed at 210–220°C melt temperature, while EVOH is held at 190–200°C. Die head temperature is set at 210°C to maintain a viscosity match between HDPE and EVOH within 5% apparent shear viscosity at 100 s⁻¹. Blow air enters at 7.0–8.0 bar with a two-stage pre-blow profile: 0.2 s at 2 bar, followed by 0.5 s at 6 bar. Mould cooling is controlled at 20°C and the clamp force is 200–400 t, depending on tank geometry. The finished tank is subjected to −40°C impact testing, cyclic pressure loading, and permeation measurement under SAE J1737 procedures. Published data for this specific six-layer configuration is limited; tier-specific evaporative emission limits must be confirmed against the applicable CARB or EPA vehicle standard. The inner conductive HDPE layer is compounded to a surface resistivity below 10⁶ Ω/sq under SAE J1645 to dissipate electrostatic charge during fuel filling.

    Directly behind the accumulator head, open-top drum production imposes a different pinch-off geometry than tight-head containers. HDF3000 is shaped into a 200 L open-top container with removable lid and bolt-ring closure. The top-roll wall is programmed to 8.0 mm to withstand lid compression, while the sidewall is reduced to 3.5 mm minimum. The pinch-off insert is maintained at 15–20°C with internal water circulation, and the flash is trimmed while the polymer is still above 70°C to avoid micro-cracking at the seam. Blow moulding uses a 25 kg accumulator head and a clamp force of 120 t. The open-top drum is tested under UN 1H1/Y1.8/150/24 for removable-head packaging, with drop testing at 1.8 m and stacking for 24 h. Formulation includes 20–30 wt% in-house regrind and 2.0 wt% colour masterbatch. The terminal container is used for pastes, solid intermediates, and food additives where access by lid is required. Food-contact status is covered under FDA 21 CFR 177.1520 and EU 10/2011 when the masterbatch and processing aids meet positive-list requirements.

    When the same grade is transferred to flat-die sheet extrusion at 800 kg/h, the melt curtain exits a 1500 mm wide sheet die with die land length 50 mm and die gap 3.5 mm. The line is configured with a three-roll polishing stack at 80°C, 70°C, and 60°C, followed by a cooling conveyor and a thickness scanner using beta-ray transmission calibrated to ISO 4591. HDF3000 sheet is produced in thicknesses of 2.0 mm, 3.0 mm, and 4.5 mm. Thermoforming of the sheet is carried out at a surface temperature of 160–175°C, with plug assist and mould cooling at 15°C. Deep-draw applications use a draw ratio not exceeding 0.5 because the high molecular weight of HDF3000 reduces hot extensibility and increases the risk of corner thinning beyond 35%. The thermoformed parts include chemical containment trays, secondary spill pallets, and machinery guards. Resistance to stress cracking is validated under ASTM D1693 Condition C for sheet in contact with aqueous detergent solutions. The sheet process requires no pellet drying below 60% RH; above that threshold, surface condensation is removed at 65°C for 2 h before extrusion.

    For 5,000 L vertical storage tank moulding, HDF3000 is processed on a 120 mm extruder with 30:1 L/D and a 30 kg accumulator head. The parison weight is 20 kg and the parison length is 2.5 m. The die gap is programmed from 4.0 mm at the top flange to 8.0 mm at the bottom base to compensate for sag over the extended parison length. Blow air is supplied at 8.5 bar, and clamp force is 300 t. Mould cooling is staged with water at 12°C in the base and 18°C in the sidewall, avoiding differential shrinkage that causes base warp. Tank wall thickness is held to 6.0–8.0 mm on the sidewall, 12.0 mm at corners, and 10.0 mm at the dome. The finished tank is rated for atmospheric storage of sodium hydroxide solution 48 wt%, hydrochloric acid 37 wt%, and liquid fertilizers. Compliance is assessed under EN 13341:2005+A1:2011 for static thermoplastic tanks and under REACH for industrial chemical contact. Formulation includes 15–20 wt% regrind from the same tank production, with weld-line integrity verified by bent-strip testing at 50°C. The tank is assembled with spin-welded flanges, butt-fusion fittings, and a bolted manway. Post-mould conditioning at 23°C and 50% RH for 24 h is required before dimensional inspection.

    When Continuous Extrusion Blow Moulding of Technical Drums Requires Internal Cooling Time Reduction

    In continuous shuttle lines producing 60 L technical drums and rechargeable chemical containers, HDF3000 is processed through a 70 mm extruder with 24:1 L/D and a twin-station shuttle clamp. Parison weight is 2.6 kg, and the cycle time is 45–55 s. Cooling time is reduced by injecting dry compressed air at 7.0 bar through an internal blow pin with exhaust flow at 180 m³/h. The internal cooling air leaves at 10°C, extracting heat from the inner wall. Mould water is maintained at 12°C with a pressure drop of 0.3 MPa across the channels. The container wall is controlled to 2.5 mm minimum, and the handle area is thickened to 4.0 mm by local parison programming. The terminal product is a UN 3H2/Y1.5/100/24 packaging for corrosive liquids, inks, and water-treatment chemicals. The process uses 25 wt% regrind and 1.0–1.5 wt% colour concentrate. Batch-to-batch variation in high-load melt index from 5.5 to 7.5 g/10 min is corrected by closed-loop parison sag control using photocell measurement and automatic die-gap adjustment of ±0.2 mm. This capability is necessary because a change of 10% in parison length at 2.6 kg shot weight shifts the bottom pinch-off thickness outside the 2.5–3.0 mm tolerance band.

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    Certification & Compliance
    More Introduction

    EQUATE HDPE HDF3000

    EQUATE HDPE HDF3000 is a high-density polyethylene film resin supplied in pellet form for monolayer and coextruded blown-film structures. The grade designation HDF3000 identifies a nominal density of 0.949 g/cm³ measured under ASTM D1505 and a nominal melt flow rate of 0.30 g/10 min measured under ASTM D1238 at 190°C/2.16 kg. Those values place the material in the high-stiffness HDPE film category rather than in fractional-melt HDPE film grades or high-flow injection molding grades. Typical end uses include T-shirt carrier sacks, general merchandise bags, light-duty trash liners, and core layers in coextruded sacks. The product is specified where down-gauging under stiffness-limited conditions is more critical than high-speed dart impact toughness. The values in Table 1 are typical published values, not batch specifications; the certificate of analysis for each lot controls final acceptance.

    PropertyTest methodUnitTypical value
    Melt flow rate (190°C/2.16 kg)ASTM D1238g/10 min0.30
    DensityASTM D1505g/cm³0.949
    Tensile strength at yield (MD/TD)ASTM D882MPa27/25
    Elongation at break (MD/TD)ASTM D882%650/750
    Secant modulus at 1% (MD/TD)ASTM D882MPa950/900
    Elmendorf tear strength (MD/TD)ASTM D1922g20/150
    Dart impact F50 (25 µm)ASTM D1709Ag150
    Vicat softening pointASTM D1525°C125

    Film properties in Table 1 are published typical values for 25 µm monolayer film produced at a blow-up ratio of 3:1-5:1. Actual values depend on die gap, frost-line height, melt temperature, output rate, and additive package. The tabulated values should not be used as incoming resin specifications.

    What processing boundaries appear during high-stalk film conversion?

    On a 24-30 L/D single-screw extruder with a barrier feed section and mixing pins, barrel setpoints from 180°C to 210°C are common; the die and adapter are held at 200-215°C. The die gap is typically 1.0-1.4 mm, wider than for many LLDPE grades, to accommodate the longer melt relaxation time and to shift the onset of sharkskin melt fracture to higher output rates. Blow-up ratios of 3:1-5:1 and frost-line heights between 5 and 12 die diameters keep the high-stalk neck stable. When the frost-line height is below 5 die diameters, cooling is incomplete and the film may block in the collapsing frame; when it exceeds 12 die diameters, ambient air currents can induce neck oscillation and produce gauge bands. Processing aids based on fluoropolymers at 200-500 ppm are used on some lines to reduce die-lip build-up and melt fracture, but addition must be validated because the additive migrates to the die surface and changes the coefficient of friction of the finished film.

    The melt is moderately shear-thinning. At typical die shear rates the apparent viscosity falls into the range expected for a broad-molecular-weight high-density film resin. Thermal analysis by ASTM D3418 typically shows a melting peak near 131°C and a crystallization temperature near 117°C. Those values fix the cooling-side process envelope: the film must be quenched below the crystallization onset before the collapsing frame to avoid blocking and excessive haze. On lines with internal bubble cooling, frost-line position is controlled by adjusting the chilled-air volume rather than by reducing output alone. The upper melt temperature boundary is 240°C; above this temperature oxidative chain scission can form gel particles and organoleptic defects. The lower practical melt temperature boundary is near 180°C; below this, die pressure rises and the melt may exhibit surface melt fracture. If extruder head pressure rises toward the upper interlock limit, the first corrective action is to raise barrel zone temperatures by 5°C increments and inspect screen pack loading. Increasing screw speed without temperature adjustment can raise melt temperature into the degradation zone and should be avoided.

    Pellets transferred from outdoor silos in cold weather should be allowed to reach 20-25°C before entering the feed throat. If surface condensation is visible, drying at 70-80°C for 1-2 h in a desiccant or hot-air hopper dryer removes surface moisture. No pre-drying is required under indoor storage below 60% RH.

    In 25 µm monolayer blown film, HDF3000 shows the typical anisotropic tear behaviour of high-density polyethylene. Elmendorf tear strength measured under ASTM D1922 is lower in the machine direction than in the transverse direction; the machine-direction value is often below 30 g, while the transverse-direction value can exceed 100 g. Dart impact F50 under ASTM D1709A is typically in the 150 g class, but gauge non-uniformity of ±5% across the flattened web can reduce field impact performance more than the resin’s intrinsic value suggests. On automatic bag-converting lines, fold-line fibre tear and seal-edge nicks are the dominant failure modes. Seal jaw temperatures above 170°C can cause overmelt and orientation release at the seal; temperatures below 140°C may give weak hot-tack. The coefficient of friction of unmodified film may exceed 0.35 under ASTM D1894, so slip/antiblock masterbatch addition of 2-5 wt% is usual for high-speed bag machines. Such masterbatches reduce COF to the 0.15-0.25 band but increase haze and can reduce dart impact by 10-20% depending on the carrier resin and screw dispersion quality.

    When HDF3000 is compared with LLDPE, fractional-melt HDPE, and injection grades

    Against a butene-LLDPE with density near 0.918 g/cm³, HDF3000 delivers higher 1% secant modulus, higher yield stress, and lower water vapour transmission, but lower dart impact and lower machine-direction tear propagation. The typical 1% secant modulus in Table 1 is roughly 900-950 MPa; an equivalent-thickness LLDPE film may fall near 180-260 MPa. Under ASTM D1709A, LLDPE monolayer of the same gauge may show dart impact values from 300 g to more than 600 g, while the HDF3000 monolayer value is lower by a factor of two to four. That difference does not make the grade universally inferior; it defines a stiffness and barrier trade-off. Compared with fractional-melt HDPE film grades with melt flow rate near 0.05 g/10 min, HDF3000 processes at lower head pressure and permits higher drawdown, but may sacrifice some dart impact and tear resistance. Compared with HDPE injection grades with melt flow rate of 8-20 g/10 min, HDF3000 is not suitable for thin-wall injection because its 0.30 g/10 min melt flow rate restricts flow length and increases clamp force demand. The intended process is blown-film extrusion; attempts to use the grade in injection molding should be rejected at the design stage.

    Surface treatment is required for printing, lamination, or coating. Untreated HDPE has a surface energy near 30-32 mN/m; corona treatment should raise the film surface to 38-42 mN/m for water-based ink adhesion. The dyne level decays after treatment, particularly if migratory slip additives bloom to the surface. Re-treatment or inline treatment immediately before printing is necessary when the film has been stored for more than 24-48 h after slitting. The actual decay rate depends on additive package, storage temperature, and polymer crystallinity; published data for this specific configuration is limited and should be confirmed by contact angle or dyne-pen measurements.

    Regulatory compliance checkpoints, storage moisture limits, and additive incompatibility

    Food-contact status cannot be assigned solely from the resin grade. The base polyethylene is expected to fall within FDA 21 CFR 177.1520 for olefin polymers in the United States and Regulation (EU) No 10/2011 in the European Union when the finished article contains only compliant additives and is not contaminated during conversion. Under EU food-contact testing, overall migration must not exceed 10 mg/dm² in the intended simulant and time-temperature condition; specific migration limits apply to additives and monomers. The grade is normally considered REACH-registered as a polymer substance under Regulation (EC) No 1907/2006, but the converter must confirm the registration status of all masterbatches and additives. RoHS compliance under Directive 2011/65/EU is a finished-article responsibility and is not a resin-only property.

    CheckpointStandard/regulationCondition or limitation
    US food contactFDA 21 CFR 177.1520Olefin polymers; end-use testing required
    EU food contactRegulation (EU) No 10/2011Overall migration < 10 mg/dm²; simulant-specific
    REACH registrationRegulation (EC) No 1907/2006Polymer-exempt; monomers and additives registered
    RoHSDirective 2011/65/EUFinished-article limited substances

    Storage should be in original bags or sealed silos at 20-30°C, below 60% RH, away from direct sunlight. The resin should not be stored near strong oxidizers, volatile amines, or halogenated compounds. Avoid melt contact with copper or copper alloy surfaces for long residence times because copper catalyses oxidative degradation. If the extruder is stopped for more than 15-20 min with resin in the barrel, the melt temperature should be reduced to 160-170°C or the material purged with a stable polymer to limit thermal history. Reclaimed HDF3000 edge trim and start-up scrap can be re-introduced as in-line regrind up to 15-20% by weight, but higher levels increase gel risk and reduce film gauge uniformity unless the regrind is filtered through a fine mesh screen pack.

    In coextruded sack structures, HDF3000 is typically placed as the core layer between LLDPE skins. The core contributes stiffness and down-gauging, while the skins provide seal initiation, tear propagation resistance, and dart impact. A three-layer structure with 20-40% HDF3000 in the core can achieve a film secant modulus between 500 MPa and 800 MPa, but the exact value is set by layer ratio, film gauge, blow-up ratio, and frost-line geometry. When the core layer exceeds 40%, film tear and dart impact may approach the monolayer HDF3000 values shown in Table 1. The selected die gap and internal bubble cooling settings are more influential than resin grade alone. Because published data for specific production line configurations is limited, qualification trials using a capacitance thickness gauge and dart impact sampling per ASTM D1709A are required to establish the process window.

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