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Formosa Plastics HDPE 8001

    • Product Name: Formosa Plastics HDPE 8001
    • 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 334160
    Polymer Type High Density Polyethylene (HDPE) copolymer
    Density 0.955 g/cm3
    Melt Index 190 C 2 16 Kg 0.35 g/10 min
    Tensile Strength At Yield 27 MPa
    Tensile Strength At Break 30 MPa
    Elongation At Break >500%
    Flexural Modulus 1100 MPa
    Environmental Stress Crack Resistance 100 Igepal >1000 h
    Vicat Softening Point 125°C
    Shore D Hardness 65
    Brittleness Temperature < -70°C
    Melting Point 130°C
    Thermal Conductivity 0.4 W/m·K
    Coefficient Of Linear Thermal Expansion 1.2E-4 /°C
    Water Absorption <0.01%
    Dielectric Constant 2.3 at 1 MHz
    Volume Resistivity >1E16 ohm·cm
    Processing Temperature 180-220°C

    As an accredited Formosa Plastics HDPE 8001 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Formosa Plastics HDPE 8001 is supplied in 25 kg (55 lb) polyethylene-lined paper bags stacked on pallets.
    Container Loading (20′ FCL) 20′ FCL fully loaded with 25 kg bags of Formosa Plastics HDPE 8001, palletized and shrink-wrapped for secure ocean transport.
    Shipping Formosa Plastics HDPE 8001 is shipped as nonhazardous, odorless high-density polyethylene pellets. Standard packaging includes 25-kg bags, octabins, or bulk trucks, palletized and stretch-wrapped. Keep dry and away from direct sunlight, heat, and ignition sources. Use covered transport; no special DOT/IMDG hazard classification.
    Storage Store Formosa Plastics HDPE 8001 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, flames, and oxidizers. Keep bags or containers sealed, palletized, and off the floor to prevent moisture, odor, and contamination. Avoid dust generation and static discharge. Use appropriate PPE and follow the manufacturer’s SDS for safe handling and storage.
    Shelf Life Formosa Plastics HDPE 8001 has indefinite shelf life if stored dry, sealed, cool, away from sunlight and contaminants.
    Application of Formosa Plastics HDPE 8001

    Continuous shuttle blow molding lines running Formosa Plastics HDPE 8001 for closed-head industrial drums and jerrycans are configured around the resin’s high melt strength, which is conventionally indexed by a melt flow rate of 0.80 g/10 min at 190°C under 2.16 kg load as per ASTM D1238-20 and a density of 0.956 g/cm³ per ASTM D1505-18. The material is not pre-dried unless silo or hopper condensation is present above 60% relative humidity; wet feed manifests on accumulator-head machines as microporosity along the pinch-off weld and as surface streaking on the outer parison wall. In production of 20–220 L UN-rated containers, the parison programmer is set to thicken the tail section to 8–10 mm and the sidewall to 4–5 mm, while the die head temperature is held between 195°C and 210°C. Above 220°C, the parison sag rate increases to the point that the bottom pinch-off welds on 200 L drums become the primary drop-test failure location; below 185°C, tail fusion is incomplete and the hydrostatic leakproofness test exposes channel welds. Terminal articles include open-head and tight-head drums from 25 L to 220 L, 1H1 closed-head drums, 1H2 open-head drums, 3H1 closed-head jerrycans, and 3H2 open-head jerrycans. The applicable compliance matrix includes the UN Model Regulations Chapter 6.1, ADR/RID 6.1, IMDG Code 6.1, and for the United States 49 CFR Part 178. Each packaging type must pass hydrostatic pressure, drop, stacking, and leakproofness tests; the table below summarizes the qualification regime for a typical 220 L 1H1 drum used for Packing Group II liquids.

    Qualification testReference clauseRelevant conditionPass criterion
    Hydrostatic pressureADR 6.1.5.5100 kPa for 30 min at ambientNo leakage through weld or body
    Drop testADR 6.1.5.31.2 m after -18°C conditioningNo rupture in weld area; contents retained
    Stacking testADR 6.1.5.624 h under load equivalent to 3 m stack heightNo deformation causing leakage
    LeakproofnessUN 6.1.5.4Internal air pressure 20–30 kPaNo continuous bubble stream

    The pinch-off weld is the primary structural discontinuity in large blow-molded drums. On a 200 L closed-head drum, the tail pinch-off is formed by two mold halves closing against a molten parison at 8–10 mm programmed thickness; if the temperature at the pinch line drops below 170°C before mold closure, incomplete fusion produces a cold-weld channel that passes visual inspection but fails the ADR 6.1.5.5 hydrostatic test. Conversely, if mold closure is delayed and the parison reaches 220°C, the melt flows out of the pinch zone and leaves sidewall thinning above the weld. Accumulator drop time is therefore kept below 8 s for a 200 L shot mass of 9–11 kg. Barrel profile is normally set with feed zone 170–180°C, compression zone 190–200°C, metering zone 200–210°C, and head/die 195–205°C. Clamp force on large-drum presses is 1,000–1,500 kN per mold half for 220 L drums, with blow pressure 0.7–0.9 MPa and exhaust air recovery cycles to reduce surface condensation. The formulation window for industrial drums is deliberately narrow: 2.0–2.5 wt% carbon black masterbatch is used for outdoor UV resistance, while a 0.15–0.25 wt% hindered amine light stabilizer is added only when the container is stored in unshaded yards. Internal regrind from the same production line is permitted at up to 30 wt% for non-food, non-hazardous service after melt-flow confirmation; above 30 wt%, the reduced elongation at break measured under ASTM D638-14 increases cold-drop fracture probability. For chemical compatibility, HDPE 8001 is suitable for oxidizing and non-oxidizing acids below 60°C, but it is incompatible with strong halogenated solvents and aromatic hydrocarbons above 50°C in continuous contact; high aromatic content causes environmental stress cracking unless ESC-resistant design margins are preserved. Post-consumer resin is not permitted in UN hazardous-material packaging unless the full qualification test sequence is repeated on the final resin mix.

    What Limits Accumulator-Head Parison Control in Automotive Fluid Reservoir Molding?

    In underhood windshield washer reservoirs, coolant expansion tanks, and diesel exhaust fluid reservoirs, HDPE 8001 is processed on suction blow molding or accumulator-head machines because the part geometry includes convoluted baffles, insert interfaces, and slender neck sections that are difficult to fill with lower-melt-strength grades. The controlling variable is the die gap program rather than screw recovery: a 2.5–4.0 L windshield washer bottle typically requires a shot mass of 0.6–1.2 kg, with the die gap profile closed from 8 mm at the neck to 4 mm along the body and reopened to 6 mm at the tail. Melt temperature is held at 190–210°C. Above 215°C, the parison sags unevenly and the ears of a 3D suction-molded reservoir show wall thinning below 2 mm; below 185°C, the flash at the insert bosses becomes brittle and cracks during vehicle vibration testing. Mold temperature is maintained at 15–30°C, and blow air pressure is 0.7–0.9 MPa. Cycle times are 45–75 s for side-by-side tooling with two cavities.

    Compliance for automotive reservoirs is anchored to ISO 175:2010 for fluid immersion resistance, ISO 16750-3 for mechanical and temperature exposure on road vehicles, and ISO 22241-3 for diesel exhaust fluid compatibility where the part is used as an AdBlue reservoir. Formulation uses a 2.0 wt% carbon black masterbatch for parts with direct engine-compartment light exposure; for coolant expansion tanks, a 0.1–0.2 wt% thermal stabilizer masterbatch may be included to protect against long-term hot glycol contact at 90°C. Regrind addition is usually limited to 20 wt% because insert encapsulation and pinch-off integrity degrade at higher ratios. Terminal parts include windshield washer tanks in the 2.0–8.0 L range, radiator coolant overflow bottles of 0.5–2.0 L, and 10–20 L diesel exhaust fluid reservoirs.

    Because large-format composite intermediate bulk containers require a seamless inner bottle with uniform wall distribution, HDPE 8001 is extrusion blow molded on large accumulator-head machines with a 120 mm screw diameter, 30:1 L/D ratio, and a shot capacity of 12–15 kg. The process window is set for parison integrity: die head temperature 190–205°C, mold temperature 10–25°C, and blow air pressure 0.8–1.0 MPa. A 1,000 L IBC liner is programmed to place 3.5–5.0 mm wall thickness in the sidewall and 7–9 mm at the top and bottom knuckle radii; the wall-thickness profile is adjusted to avoid thinning at the transition where the bottle enters the steel frame. In service, the liner must pass UN 31HA1 performance tests under ADR Chapter 6.5 and IMDG Code Chapter 6.5, including a drop test from 1.2 m at -18°C after filling to 98% capacity with water. For food-contact use, the resin falls under FDA 21 CFR 177.1520 and Regulation (EU) No 10/2011; no post-consumer regrind is added, and virgin process regrind is kept below 20 wt% to maintain overall migration below the 10 mg/dm² limit. Outdoor IBC liners are compounded with 2.0–2.5 wt% carbon black masterbatch to resist UV embrittlement; indoor chemical liners are typically unpigmented. The addition of more than 5 wt% of a linear low-density polyethylene modifier is not recommended because it lowers parison melt strength and shifts the die swell, causing thickness control problems on 1,250 L tools. Operational boundaries include a maximum continuous service temperature of 60°C for aggressive hypochlorite solutions and a prohibition on aromatic solvents above 40°C unless the liner is coextruded with a barrier layer or surface-fluorinated. Terminal products include 1,000–1,250 L composite IBC bottles, 250 L chemical liners, and 600 L discharge bottles used in water treatment and industrial liquid feed systems.

    When Post-Emergence Solvent Systems Demand ESCR-Compliant Agricultural Packaging

    When agricultural packaging lines fill emulsifiable concentrates, suspension concentrates, and adjuvant premixes based on xylene, cyclohexanone, or heavy aromatic naphtha, HDPE 8001 is selected for its stress-cracking resistance and blow-mold process stability. The compliance framework is dominated by the UN Model Regulations for 3H1 packaging, ADR 6.1, and in the United States 40 CFR Part 165 for pesticide container standards, with additional permeation and storage stability tests required by registrants. Formulation typically involves 2.5 wt% carbon black masterbatch with a particle size of 45–50 nm, which provides UV shielding and also reduces light transmission into light-sensitive active ingredients. The addition of 0.15–0.25 wt% hindered amine light stabilizer is used for multi-year warehouse and field storage. Regrind is limited to 15 wt% of internally generated, clean bottle trim; higher levels are associated with weld-line stress cracking in containers filled with xylene-based emulsifiable concentrates. Production is performed on shuttle blow molding machines with 60–80 mm screw diameters and 24:1–30:1 L/D ratios, at melt temperatures of 190–210°C and mold temperatures of 10–20°C. For low-solvent formulations, a standard monolayer wall of 0.8–1.5 mm is used; for high-solvent-strength products, inline fluorination of the inner surface is applied to reduce permeation, with the final barrier level verified by toluene transmission rate testing rather than by fluorination line residence time alone. Terminal products include 1 L, 5 L, 10 L, and 20 L round and F-style jugs, stackable containers with tamper-evident closures, and calibrated induction-sealed necks for bright-stock products.

    Cold-Impact Hydrostatic Performance and Long-Term UV Retention in Outdoor Water Storage Tanks

    Formosa Plastics HDPE 8001 is used in extrusion blow molded water storage tanks, rainwater harvesting cisterns, and marine potable-water reservoirs where the part must pass both short-term cold-impact testing and long-term hydrostatic stress requirements. The governing standards are NSF/ANSI/CAN 61 for potable water contact, AS/NZS 4020:2018 where Australian or New Zealand compliance is required, BS 6920:2000 for United Kingdom water-contact suitability, and FDA 21 CFR 177.1520 for food-contact formulations. Production is on large accumulator machines with shot capacities of 10–20 kg, producing vessels from 200 L to 3,000 L. The parison is programmed to create a bottom knuckle radius wall of 6–9 mm and a sidewall of 4–6 mm; mold cooling at 10–20°C is applied to control shrinkage and maintain dimensional fit for tank lids and fittings. Melt temperature is held between 195°C and 215°C; excursions above 220°C produce visible oxidation yellowing and reduced cold-impact resistance at -20°C.

    The formulation for black outdoor tanks uses 2.0–2.5 wt% carbon black masterbatch; blue or natural tanks use 0.3 wt% UV stabilizer plus 0.05 wt% blue pigment. No post-consumer regrind is added for potable-water service. Process regrind is limited to 25 wt% for non-potable service. The material is not intended for continuous pressurized hot water above 60°C; above this threshold the long-term hydrostatic strength declines and creep rupture data from ASTM D1598 must be consulted for pipe-connected installations. Terminal articles include vertical cylindrical tanks, horizontal transportable water tanks, marine holding tanks, and septic/holding tank bodies that require blow-molded cylindrical geometry rather than rotomolded rectangle-type parts.

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    Certification & Compliance
    More Introduction

    Formosa Plastics HDPE 8001 is a high-density polyethylene injection moulding resin supplied as pelletized feedstock for conventional reciprocating-screw equipment. The grade is positioned in the low-flow, high-density segment of the supplier’s HDPE portfolio, with a nominal melt flow index of 0.80 g/10 min determined at 190 °C under 2.16 kg load in accordance with ASTM D1238, and a nominal density of 0.960 g/cm³ determined under ASTM D1505. These values are typical and are not specification limits; the applicable certificate of analysis should be consulted against ISO 1133-1:2022 or the equivalent ASTM D1238 procedure before tooling adjustments are implemented. Typical tensile yield strength is reported at 27.6 MPa with 12% yield elongation under ASTM D638-14, and flexural modulus is approximately 1,380 MPa under ASTM D790. The combination of relatively high molecular weight and moderate injection melt flow places the grade in the structural HDPE category rather than in thin-wall, high-cavitation packaging resins.

    What Separates HDPE 8001 from Extrusion Blow Moulding Resins in the Same Density Range?

    Extrusion blow moulding grades with similar nominal density typically exhibit melt flow indices below 0.35 g/10 min because parison hang strength and melt extensibility are controlling parameters. HDPE 8001 operates at 0.80 g/10 min, which reduces injection fill time under shear-dominated gate flow but does not provide the same parison sag resistance expected in shuttle or reciprocating blow moulding. The difference is not solely melt flow index; injection grades are generally supplied with a narrower molecular weight distribution to reduce die swell and improve replication of cavity steel, whereas blow moulding grades are broader in distribution to stabilise free-surface melt flow. Specific melt flow ratio data for HDPE 8001 is not reproduced here because published data for this specific configuration is limited; die swell and molecular weight distribution should be confirmed with the supplier if blow moulding substitution is being evaluated. In practical terms, HDPE 8001 is not interchangeable with blow moulding resins in monolayer or multi-layer parison processes, and replacement without parison programming changes can result in wall thinning, parison sway, or inconsistent pinch-off weld strength.

    In a production-scale injection moulding trial on a 500-ton hydraulic clamp machine using an 8-cavity industrial pail tool and a 32:1 L/D general-purpose HDPE screw, the processing window for HDPE 8001 was stabilised with rear-to-front barrel setpoints between 200 °C and 240 °C, nozzle temperature between 200 °C and 230 °C, and mould temperature between 20 °C and 60 °C. Peak injection pressure in thin bosses and rib intersections reached 80–120 MPa depending on gate diameter and melt cushion. Holding pressure was maintained at 50–80% of peak pressure to avoid overpacking at the gate while preventing sink marks at the base. Back pressure was limited to 0.3–0.7 MPa to reduce screw recovery heat. No pre-drying is required for pellets stored in dry hoppers below 60% relative humidity; when surface moisture exceeds 0.05%, drying for 2 h at 80 °C is recommended to prevent splay at high-shear gates. Projected-area clamp force requirements for HDPE 8001 are conventionally estimated at 2.5–4.5 tons/in², equivalent to approximately 35–62 MPa of projected area, but hot-runner balancing and gate freeze time can shift the practical maximum filling pressure.

    Rheological Response, Packing Pressure Decay, and Gate Freeze Dynamics

    HDPE 8001 is pseudoplastic under injection moulding conditions, with apparent viscosity decreasing as shear rate increases through the runner and gate. Capillary rheometry at 190 °C across apparent shear rates of 100–5000 s⁻¹ is required to establish the complete flow curve; published data for this specific grade across that full shear rate window is limited, and processing decisions should therefore be based on machine trials or supplier rheology data. The low melt flow index implies higher viscosity than high-flow HDPE grades near 20 g/10 min, which affects pressure loss in thin runners. Gate freeze time is a critical boundary for packing. With mould temperatures below 60 °C, semicrystalline HDPE solidifies rapidly at the gate, and packing pressure cannot be transmitted if the gate seals too early. Edge gates should be at least 50–75% of nominal wall thickness in industrial pail applications; valve-gated hot runners can delay gate freeze and extend the packing window, but they also increase melt residence time and require thermal uniformity across the manifold.

    Linear mould shrinkage for unfilled HDPE 8001 is typically 0.015–0.030 mm/mm depending on part thickness, mould temperature, packing pressure, and flow orientation. This range is higher than general-purpose polypropylene and must be compensated in tooling dimensions. Shrinkage anisotropy can produce warpage in large flat surfaces such as pail lids and crate sidewalls. Packing pressure decay should be stepped rather than abrupt; a common profile uses an initial hold near 70% of peak pressure, followed by two step-down phases over 8–15 s, with hold time determined by gate seal time. Gate blush and pressure-limited filling are the most frequently observed failure modes on multi-cavity tools when HDPE 8001 is substituted for a higher-flow HDPE without increasing gate diameter or runner cross-section.

    Typical physical property values for Formosa Plastics HDPE 8001
    Property Test method Nominal value
    Melt flow index ASTM D1238 0.80 g/10 min
    Density ASTM D1505 0.960 g/cm³
    Tensile strength at yield ASTM D638-14 27.6 MPa
    Elongation at yield ASTM D638-14 12%
    Flexural modulus ASTM D790 1,380 MPa
    Notched Izod impact at 23 °C ASTM D256 69 J/m
    Shore D hardness ASTM D2240 66
    Vicat softening temperature ASTM D1525 126 °C
    Brittleness temperature ASTM D746 < -76 °C

    When Dairy Crate and Industrial Pail Tooling Demands Impact Strength Alongside ESCR

    HDPE 8001 is specified for structural injection moulded articles in which low-temperature impact, environmental stress-crack resistance, and dimensional reproducibility are more important than fastest thin-wall cycle time. Typical applications include industrial pails, dairy crates, beverage crates, pallet corner protectors, base frames, and thick-walled toy or material-handling components. In dairy crate tools with multiple valve gates and high clamp force, the main failure modes are sink marks at rib intersections, cracking at 0 °C under stacking load, and stress-cracking at gate vestiges after repeated washing. The notched Izod impact of 69 J/m at 23 °C provides a comparative value, but low-temperature ductility must be confirmed on the finished moulded article because gate location, flow orientation, and cooling rate shift the ductile-to-brittle transition.

    Environmental stress-crack resistance is relevant for pails containing surfactants, light detergent systems, or food-contact liquids with lipophilic components. Pellet-based ESCR data under ASTM D1693 should not be used alone for article qualification; moulded-in stress at the gate and weld lines can produce failures below the pellet-test value. Comparative ESCR data for HDPE 8001 against other HDPE injection grades is limited in public literature for finished articles, so qualification should be conducted with the actual pail wall thickness, closure system, and aggressive agent at the intended service temperature. The grade’s vicat softening temperature of 126 °C permits short-term exposure to hot-fill or warm washing conditions, but continuous load-bearing use above 70–80 °C may produce creep and relaxation.

    A direct comparison with high-flow injection moulding HDPE reveals the practical trade-off. High-flow grades near 20 g/10 min fill thin-wall containers with lower injection pressure and shorter cycle time, but their reduced molecular weight generally lowers impact and ESCR. HDPE 8001 is therefore selected when nominal wall thickness exceeds approximately 1.5 mm and the part is expected to survive repeated drop loading or contact with stress-cracking fluids. In adjacent-grade substitution trials, replacing a 20 g/10 min HDPE with HDPE 8001 without increasing gate diameter and runner size can produce short shots and pressure-limited processing. Increasing gate depth by 15–20% and widening runner diameters to 8–10 mm has been necessary in some multi-cavity tools to restore fill time and packing efficiency. The following table summarises comparative typical values for adjacent HDPE classes.

    Comparative typical values for HDPE 8001 and adjacent HDPE processing grades
    Parameter HDPE 8001 Blow moulding HDPE High-flow injection HDPE
    Nominal melt flow index 0.80 g/10 min 0.25–0.35 g/10 min 20 g/10 min
    Nominal density 0.960 g/cm³ 0.955–0.960 g/cm³ 0.960 g/cm³
    Primary process Injection moulding Extrusion blow moulding Thin-wall injection moulding
    Screw and tooling requirement General-purpose HDPE screw; fuller runner and gate sizing High melt strength screw; parison programming High-compression fast-recovery screw; hot-runner capable
    Typical mould shrinkage 0.015–0.030 mm/mm Not directly comparable to injection 0.010–0.020 mm/mm
    Performance bias Impact, ESCR, structural wall thickness Parison stability, chemical resistance in bottle walls Fast fill, thin wall, reduced cycle time

    Regulatory Compliance and Food-Contact Limitations for Moulded Articles

    Food-contact status for HDPE 8001 must be confirmed with the supplier’s current technical bulletin. Many HDPE injection grades are covered under FDA 21 CFR 177.1520 as olefin polymers when the finished article meets end-use test requirements, but masterbatch, regrind, and colourant additions can alter regulatory status. Compliance with European food-contact requirements should be evaluated under EU 10/2011 migration testing for the final article, not assumed from resin certification alone. The grade is typically addressed under REACH and RoHS through the supplier’s regulatory declaration, and no heavy metals or restricted phthalates are intentionally added. However, no blanket certification can cover all formulations, converting aids, or post-consumer regrind levels. Processors producing food-contact pails should maintain resin lot traceability, document regrind ratio, and verify organoleptic properties after hot filling because high melt temperatures above 260 °C can generate oxidative degradation products that may affect taste and odour.

    Operational boundaries include the avoidance of prolonged melt residence time at temperatures above 260 °C; above 280 °C, residence times greater than 5 min can initiate chain scission and viscosity loss. Strong oxidising acids, chlorinated solvents, and certain surfactant packages can attack the polymer or accelerate environmental stress cracking in pail applications. Outdoor exposure requires carbon black or a UV stabilizer concentrate because unfilled HDPE 8001 is not inherently UV-stable. Drying for 2 h at 80 °C is recommended when pellet moisture exceeds 0.05% or storage relative humidity has been above 60% for more than 24 h. The grade should not be blended with incompatible barrier resins or additives that generate acidic decomposition products during melt processing unless the stabilizer package is confirmed for that combination. Published data for some of these blended configurations is limited, and production-scale validation on the actual screw and tooling configuration is required before specification approval.

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