| HS Code | 132977 |
| Melt Flow Rate | 4.0 g/10 min at 190°C/2.16 kg |
| Density | 0.957 g/cm³ |
| Tensile Strength At Yield | 27 MPa |
| Tensile Strength At Break | 20 MPa |
| Elongation At Break | 800% |
| Flexural Modulus | 1100 MPa |
| Izod Impact Strength Notched | 50 J/m |
| Shore D Hardness | 65 |
| Vicat Softening Point | 124°C |
| Heat Deflection Temperature | 70°C at 0.45 MPa |
| Brittleness Temperature | -70°C |
| Environmental Stress Crack Resistance | 100 h |
| Mold Shrinkage | 1.5% to 3.0% |
| Water Absorption | <0.01% |
As an accredited Formosa Plastics HDPE TAISOX 8041 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Formosa Plastics HDPE TAISOX 8041 comes in 25 kg woven bags, 40 bags per 1,000 kg pallet. |
| Container Loading (20′ FCL) | 20′ FCL loaded with Formosa Plastics HDPE TAISOX 8041 in 25 kg bags, floor-stacked and securely braced for ocean transport. |
| Shipping | Formosa Plastics HDPE TAISOX 8041 ships as non-hazardous high-density polyethylene resin pellets. It is not regulated for transport, with no UN number. Standard packaging includes 25 kg bags or 500–1,000 kg jumbo bags, palletized and stretch-wrapped in containers. Store dry, away from direct sunlight and excessive heat. |
| Storage | Store Formosa Plastics HDPE TAISOX 8041 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, sparks, and ignition sources. Keep bags or containers tightly closed, palletized, and off the floor to prevent moisture and contamination. Avoid contact with strong oxidizers. Maintain clean, stable conditions and follow first-in, first-out stock rotation. Protect from UV degradation and physical damage. |
| Shelf Life | Formosa Plastics HDPE TAISOX 8041 typically has a two-year shelf life when stored cool, dry, and away from direct sunlight. |
Dairy tubs and thin-wall lids are injection moulded from Formosa Plastics HDPE TAISOX 8041 at melt temperatures of 190–220°C, with mould temperatures held at 12–25°C to shorten cooling time while limiting sink marks. The grade’s melt flow rate of 4.0 g/10 min under ASTM D1238 at 190°C/2.16 kg and density of 0.960 g/cm³ under ASTM D1505 support filling of 0.8–1.2 mm walls in stack moulds with fan gates, but the narrow processing window requires shut-off nozzles to prevent drooling at the nozzle tip. A food-contact formulation typically meters a 60% TiO₂ masterbatch at 2.0–3.0 wt%, yielding 1.2–1.8 wt% final pigment; erucamide slip is withheld because it can interfere with snap-lid sealing and organoleptic neutrality. Hot-runner tip temperatures are maintained at 210–230°C, injection speeds at 180–250 mm/s, peak injection pressures at 90–120 MPa, hold pressures at 45–60 MPa, and back pressure at 0.7–1.2 MPa; screw geometry of L/D 20:1–24:1 with a compression ratio of 2.0:1–2.5:1 is used on production lines, and vent depths of 0.015–0.025 mm prevent burn marks at the end of fill. Compliance for the finished article falls under FDA 21 CFR 177.1520(c) for olefin polymers and EU Regulation (EC) No 10/2011, with overall migration testing to 10 mg/dm² under EN 1186-1:2002; extractive limits are checked using n-hexane according to FDA 21 CFR 177.1520. Terminal articles include yogurt cups, margarine tubs, deli containers, and snap-on lids. Pre-drying is not required for moisture absorption, but pellets stored in cold silos and transferred to a humid plant above 60% RH may accumulate surface condensation; a hopper dryer at 60°C for 1 h removes surface moisture without altering the polymer.
When a 20-L pail is moulded for dangerous goods service under UN 1H2, the critical threshold is not tensile yield but ductile-to-brittle transition after conditioning at -18°C; a pail that survives ambient handling may split under drop impact at 1.2 m for Packing Group II. TAISOX 8041 is processed at melt temperatures of 180–210°C and mould temperatures of 10–30°C, with injection speeds deliberately reduced to 40–80 mm/s in 2.5–4.0 mm sidewall sections to prevent oriented skin layers that lower peel and impact strength. The compounding recipe for industrial pails commonly includes 0.25–0.50 wt% HALS, 0.10–0.25 wt% phenolic antioxidant, and 1.5–2.0 wt% carbon black masterbatch; clean post-industrial regrind is limited to 20–30 wt% because higher regrind fractions shift the melt flow rate beyond the UN qualification envelope. Hold pressure of 60–80 MPa and cooling time of 18–30 s are typical for 4.0–5.0 mm base sections; clamp force is calculated at 5–7 kN per cm² projected area. Drop testing is conducted under UN Model Regulations Chapter 6.1 with plastic packaging conditioned at -18°C or lower, and stack load performance is verified under the applicable ADR/RID chapter. For cleaning-chemical and bleach service, environmental stress cracking resistance is the dominant incompatibility: qualification in 10% Igepal CO-630 under ASTM D1693 Condition B is mandatory, and published data for this specific grade in aggressive detergent environments is limited, so finished pail ESCR testing is required before specifying the resin for oxidiser or hypochlorite packaging. Acceptable terminal parts include 5-gal paint pails, 20-L jerricans, and food-ingredient pails with liner or gasketed closure.
The tamper-evident band bridge in a 28 mm PCO 1881 water closure is 0.10–0.20 mm thick; TAISOX 8041 fills these bridges at melt temperatures of 200–230°C, but excessive tip temperature above 240°C drops melt viscosity enough to produce flash at the lower bridge surface and shortens bridge break time in assembly. Mould temperatures are kept at 8–18°C to chill the band before ejection, and injection speeds are set to 150–250 mm/s with hold pressure at 35–50 MPa. Formulation for beverage and dairy closures uses 0.05–0.10 wt% erucamide as a slip agent and 0.02–0.05 wt% synthetic silica antiblock to prevent bulk-handling blocking; a nucleating masterbatch at 0.05–0.15 wt% is added in multi-cavity tools to reduce differential shrinkage across the band. Tight bridge dimensions demand valve-gated hot runners or submarine gates with 0.6–1.0 mm land lengths; gate vestige outside 0.10 mm above the top surface is a common rejection point on closure production lines. Compliance is required with FDA 21 CFR 177.1520 and EU Regulation (EC) No 10/2011 for food-contact water and dairy closures; odour and taste transfer is assessed by the beverage OEM rather than a single published ISO standard. Torque retention protocols are set by closure brand specifications; bridge break torque and removal torque must be generated on the exact closure geometry and cavity count. Terminal components include water closures, dairy cap closures, and cosmetic flip-top caps with tamper-evident bands.
Returnable beverage crates and transport trays require a different processing logic: wall sections of 3–6 mm and rib intersections generate knit lines at gussets. Low melt temperature of 190–210°C combined with moderate injection speed of 50–100 mm/s is used with chemical blowing agent metering at 0.3–0.6 wt% to produce a 8–15% density reduction in structural-foam sections; gas counterpressure is applied at 0.3–0.7 MPa in the mould to eliminate surface swirl. The formulation for outdoor logistics parts includes 2–3 wt% colour masterbatch, 0.3–0.5 wt% HALS, 0.1–0.2 wt% processing stabiliser, and 20–30 wt% clean post-industrial regrind from the same grade; higher regrind levels reduce low-temperature crack arrest and should not be used for rack-supported pallet decks. Mould temperature is held at 20–35°C, hold pressure at 70–90 MPa, and clamp force is sized for projected area at 6–8 kN/cm². Pallet performance is qualified under ISO 8611-1:2021 for flat pallets, with static stack load and dynamic impact tests; crate dimensional stability is checked after 48 h at 40°C per user specification. The main operational boundary is low-temperature brittleness: at -20°C, the notched impact energy of an injection moulded HDPE crate can fall below the acceptable threshold for pallet racking without support beams, so a full prototype drop test at 0°C and -20°C is required. Terminal products include bottle crates, fish crates, collapsible bulk containers, and export pallets with anti-slip surface texture.
Windshield washer reservoirs and atmospheric cold-fluid tanks are injection moulded from TAISOX 8041 with a direct gate into the thickest boss region to reduce knit-line formation at inserts and weld bosses. Melt temperature is set at 190–220°C, mould temperature at 15–30°C, injection pressure at 70–100 MPa, and hold pressure at 50–70 MPa; screw decompression is limited to 2–4 mm because higher decompression draws air into the melt and creates splay. The formulation for underhood service uses 2.0–2.5 wt% carbon black masterbatch for UV stabilisation, 0.2–0.4 wt% phenolic-phosphite antioxidant package, and 0.05–0.10 wt% processing aid; copper-bearing pigments are avoided because copper catalyses oxidative degradation in hot alcohol-water mixtures. The critical chemical boundary is ethanol and methanol in washer fluid: immersion or constant tensile strain testing in 30% ethanol at 60°C for 48 h under ISO 22088-2 is recommended because high-flow HDPE can exhibit stress cracking at moulded-in bosses and weld lines. Weld-line tensile strength is checked across the boss junction under ASTM D638-14; pressure-cycle requirements are OEM-specific rather than ISO-defined, with typical washer reservoirs tested at 0–0.15 MPa cyclic air pressure. The grade is not rated for pressurised fuel contact and should not be used for fuel reservoirs because HDPE hydrocarbon permeability exceeds automotive evaporative emission requirements; continuous hot coolant exposure above 80°C is also outside the recommended operating window. Terminal parts include windshield washer reservoirs, auxiliary cold-fluid tanks, and pump-interface housings.
Stackable storage bins and drawer organizers are moulded in high-cavitation tools where wall thickness is 1.8–3.0 mm, melt temperature is 200–220°C, mould temperature is 15–25°C, and the control variable is flatness after ejection. Flatness below 1.0 mm per 500 mm span is controlled with jig cooling at 40–60°C for 2–4 min; hold pressure is kept at 40–60 MPa with a cushion of 3–5 mm to avoid sink opposite rib roots. The housewares formulation typically includes 1–3 wt% coloured masterbatch and 0.05–0.10 wt% antistatic additive for dry warehouse handling; amine-based antistatic packages are avoided because they can yellow in light and increase odour in closed storage articles. For children’s article configurations sold in the EU, migration of elements is assessed under EN 71-3:2019, and all finished articles remain subject to REACH Regulation (EC) No 1907/2006. The operational incompatibility is dynamic hinge flex: TAISOX 8041 is not recommended for living hinges or load-bearing snap arms beyond 10,000 flex cycles because HDPE exhibits lower flexural fatigue resistance than impact copolymer PP. Terminal products include under-bed storage bins, drawer trays, stackable crates for home use, and waste containers.
Horticultural trays and nursery pots demand thin-cell filling and outdoor weathering in the same part. TAISOX 8041 is processed at 190–220°C, mould temperatures of 15–30°C, and injection speeds of 180–240 mm/s for 0.7–1.0 mm cell walls; hold pressure is 30–50 MPa, and cooling time is limited to 5–8 s per cycle. For black trays, carbon black masterbatch is metered at 1.5–2.0 wt% to give a final carbon black level near 2.0%, below which ultraviolet degradation can embrittle thin cell walls after 2–3 y of outdoor exposure; HALS is added at 0.3–0.5 wt% with a phenolic antioxidant at 0.10–0.15 wt%. White or light-coloured trays require 2.5–3.0 wt% TiO₂ masterbatch plus 0.5 wt% HALS because ultraviolet exposure can cause surface chalking and embrittlement; the TiO₂ grade must be rutile with an inorganic coating to reduce photocatalytic degradation under ISO 4892-2 xenon arc testing. Pesticide and fertiliser contact imposes a compatibility boundary: finished trays are soaked in 1% sodium hypochlorite and 10% calcium nitrate solutions at 23°C for 72 h to detect surface crazing; published data for this specific grade under commercial horticultural chemical exposure is limited, so compatibility must be validated on finished trays. Terminal products include seed trays, nursery pots, propagation trays, and hydroponic net pots.
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Formosa Plastics HDPE TAISOX 8041 is a high-molecular-weight high-density polyethylene specified for extrusion blow moulding of large industrial containers. The grade is differentiated from general-purpose HDPE by a low melt flow rate, broad molecular weight distribution, and elevated environmental stress-cracking resistance. Primary applications include closed-head drums, open-top containers, intermediate bulk containers, and rigid packaging exposed to long-term chemical contact or mechanical stacking loads. The resin is selected where accumulator-head machines must generate high shot weights without unacceptable parison sag or weld-line splitting.
The melt flow rate of TAISOX 8041 places it among low-MFR extrusion-blow-moulding grades. Under ASTM D1238 at 190 °C/2.16 kg, qualified lots are typically controlled within 0.25–0.45 g/10 min, with a nominal value near 0.30 g/10 min. The equivalent melt mass-flow rate method is ISO 1133-1:2022. Density under ASTM D1505 is normally 0.953–0.956 g/cm³; this density window balances stiffness, stacking strength, and slow crack growth resistance in thick-walled mouldings. The representative property envelope is summarised below.
| Parameter | Test standard | Representative qualified-lot range |
|---|---|---|
| Melt mass-flow rate | ASTM D1238, 190 °C/2.16 kg | 0.25–0.45 g/10 min |
| Density | ASTM D1505 | 0.953–0.956 g/cm³ |
| Tensile yield strength | ASTM D638 | 24–28 MPa |
| Flexural modulus | ASTM D790 | 900–1200 MPa |
| Elongation at break | ASTM D638 | 600–900 % |
| Environmental stress-cracking resistance, F50 | ASTM D1693, Condition B, 100 % Igepal | >500 h |
These values are not specification limits. Lot-to-lot control is defined by the manufacturer’s certificate of analysis and product specification revision. Incoming resin qualification should include melt flow rate, density, ash content, and visual contamination checks under the applicable ASTM or ISO methods. Where a converter requires a narrower acceptance interval, the qualification protocol should be fixed against a retained control lot and reference container tooling.
Low melt flow under a 2.16 kg load reflects high average molecular weight, but parison hang time is not controlled by melt flow rate alone. The high-molecular-weight tail of the molecular weight distribution governs zero-shear viscosity, extensional viscosity, and melt tension at the draw-down time scale. On capillary rheometry at approximately 200 °C, shear viscosity of this product class is several thousand pascal-seconds at typical blow-moulding shear rates, whereas injection-moulding HDPE grades with melt flow rates above 8 g/10 min are one to two orders of magnitude lower in viscosity. This rheological separation is the central reason TAISOX 8041 is not interchangeable with injection-moulding resins.
On a 90 mm single-screw grooved-feed extruder with 24:1 L/D, barrel zone settings from 180 °C in the feed zone to 210 °C in the metering zone are typical. Head and accumulator temperatures are normally held between 190 °C and 210 °C. Melt temperature at the die exit should not exceed 230 °C; extended residence above this threshold promotes oxidative chain scission, gel formation, and measurable loss of environmental stress-cracking resistance. In accumulator-head blow moulding, TAISOX 8041 is used in machines with shot capacities from approximately 5 kg to 30 kg, depending on tooling and container size. Parison programming is required for tall containers because high melt strength slows sag but does not eliminate wall-thickness variation caused by differing draw ratios between top and bottom regions.
The principal difference is melt flow rate. General-purpose blow moulding grades for small bottles and thin-walled packaging often operate in the 0.7–2.0 g/10 min range under ASTM D1238. TAISOX 8041 sits below this range, which raises melt strength but also increases extruder backpressure and reduces throughput on a given screw. The trade-off is accepted on large-part accumulator-head tooling because parison sag during transfer determines final wall symmetry. A thin bottle grade cannot sustain a large parison for the same hang time without excessive thinning in the upper wall.
Compared with injection-moulding HDPE grades having melt flow rates of 10–30 g/10 min, TAISOX 8041 is unsuitable for multi-cavity thin-wall injection. Injection pressure required to fill long flow paths would exceed machine clamp capacity or induce jetting and weld-line weakness. Conversely, injection grades lack the melt strength and ESCR required for closed-head drums and chemical-service containers. Attempting to blow-mould a large drum from an injection grade produces short parison hang times, excessive sag, and unacceptable wall-thickness non-uniformity.
Within the TAISOX family, lower-MFR blow-moulding grades are selected when shot weight exceeds the comfortable capacity of continuous shuttle machines. The higher-MFR blow-moulding grades are preferred for shorter cycle times, smaller bottles, or foam-core structures where parison weight is lower. The selection boundary is process-specific: accumulator-head lines with long melt residence times and high head capacity shift toward TAISOX 8041 because the grade tolerates the slow parison transfer step.
Environmental stress-cracking resistance is controlled by molecular weight, short-chain branching distribution, and tie-molecule concentration. In blow-moulded walls, residual cooling stress and pinch-off weld lines act as crack initiation sites. The F50 value on compression-moulded plaques under ASTM D1693 Condition B does not fully replicate the stress state at a container weld line. Finished-container evaluations using drop impact, stack creep, and surfactant exposure are therefore required for agricultural chemical packaging and UN-rated industrial containers. Published data for this specific configuration in aggressive solvent service is limited; end users should validate on the final article with the intended chemical contact conditions.
When shot weight exceeds 10 kg or hang time exceeds 5 s, a high-molecular-weight grade with broad molecular weight distribution is specified. Semi-molten parison sag is governed by extensional viscosity, not by shear viscosity alone. TAISOX 8041 maintains a measurable sag plateau during the transfer interval under typical die temperatures. Die swell is managed through die-land length and gap adjustment; on accumulator-head tooling, the resin is commonly run with divergent die gaps and programmed parison thickness profiles. Variations in output rate due to regrind bulk density and particle-size distribution reduce melt pump throughput unless feeder speed and extruder backpressure are actively controlled.
No pre-drying is required for sealed packages. If regrind is stored under relative humidity above 60 %, surface moisture may cause intermittent surging and surface defects; drying at 80 °C for 2–4 h can be applied. The resin should not be processed with amine-based additives that accelerate oxidative degradation at elevated melt temperatures. The high-viscosity melt is also sensitive to screw design: low-shear barrier screws may generate excessive frictional heat in the melt zone despite low melt temperature settings. Therefore, screw speed, backpressure, and head pressure should be monitored as a cluster rather than as isolated variables.
Closed-head 55-gallon drums produced from TAISOX 8041 are typically run on moving-mould accumulator machines with six-point parison programming and top-pinch construction. The bottom pinch-off flap is a known stress concentrator; mould compression settings and pinch-off knife temperature are controlled to minimise notching. For containers requiring UN certification, the resin alone does not provide certification. The finished article must pass drop, leak, hydrostatic, and stack testing under the applicable transport regulations. HDPE alone is permeable to aromatic and low-molecular-weight hydrocarbons. Automotive fuel tank applications therefore use in-line fluorination or multilayer coextrusion with a barrier layer; TAISOX 8041 provides the structural layer but not the permeation barrier.
Olefin polymers may be used in food-contact articles when the composition meets FDA 21 CFR 177.1520 and the finished article meets the conditions of use. Converters should not assume blanket clearance without reviewing the certificate of compliance for the specific lot, because catalyst neutralisers and process stabilisers can vary. European food-contact compliance under EU 10/2011 requires overall migration testing on the finished article. Under REACH and the RoHS Directive 2011/65/EU, article-level declarations for heavy metals and substances of very high concern remain the converter’s obligation.
| Standard/regulation | Scope | Converter verification |
|---|---|---|
| FDA 21 CFR 177.1520 | Olefin polymers in food-contact articles | Certificate of compliance from resin supplier |
| EU 10/2011 | Plastic food-contact materials | Overall migration test per EN 1186 |
| REACH | Registration and SVHC communication | Article-level declaration |
| RoHS Directive 2011/65/EU | Heavy metal restrictions | Supplier analytical data for cadmium, lead, mercury, and hexavalent chromium |
TAISOX 8041 is not formulated for thin-film, fibre, or injection-moulding service. Because HDPE is semi-crystalline, post-weld shrinkage continues for hours after demoulding; dimensional verification should be conducted after conditioning at 23 °C and 50 % relative humidity. Contact with strong oxidisers, aromatic solvents, or low-molecular-weight hydrocarbons may require barrier treatment or alternative polymer selection. Processors should confirm the exact specification revision with the resin manufacturer before requalifying an alternate source.