| HS Code | 899686 |
| Density | 0.960 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 8.0 g/10 min |
| Tensile Strength At Yield | 30 MPa |
| Tensile Elongation At Break | 1000 % |
| Flexural Modulus | 1200 MPa |
| Izod Impact Strength Notched 23 C | 40 J/m |
| Hardness Shore D | 65 |
| Vicat Softening Point | 127 °C |
| Heat Deflection Temperature 0 45 Mpa | 75 °C |
| Environmental Stress Crack Resistance | >1000 h |
| Mold Shrinkage | 2.0-4.0 % |
| Melting Point | 132 °C |
As an accredited Formosa Plastics HDPE TAISOX 8009 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Formosa Plastics HDPE TAISOX 8009 comes in 25 kg woven bags, with 20 metric tons per 20-foot container. |
| Container Loading (20′ FCL) | 20' FCL loaded with Formosa Plastics HDPE TAISOX 8009 in 25 kg bags, palletized, shrink-wrapped, and securely lashed for ocean transport. |
| Shipping | Formosa Plastics HDPE TAISOX 8009 is shipped as a non-hazardous polymer resin, typically in 25 kg PP woven bags or 500–1000 kg jumbo bags, palletized and stretch-wrapped. Transport in clean, dry containers or trucks. Store away from heat, moisture, and direct sunlight. No special DG handling required. |
| Storage | Store Formosa Plastics HDPE TAISOX 8009 in a cool, dry, well-ventilated warehouse, away from direct sunlight, rain, heat, and ignition sources. Keep original bags closed and pallets off the floor to prevent moisture and contamination. Avoid contact with strong oxidizers. Use first-in, first-out stock rotation; limit stacking height to prevent deformation. Maintain clean, dry conditions. |
| Shelf Life | Shelf life is typically 24 months from production when stored unopened in original packaging, cool, dry, well-ventilated, away from sunlight and moisture. |
On high-throughput injection lines producing ventilated logistics crates with nominal sidewall thickness from 2.0 mm to 2.8 mm, TAISOX 8009 is delivered to a reciprocating-screw injection molding machine with a screw diameter of 120 mm, an L/D ratio of 24:1, and a compression ratio configured for HDPE at 2.8:1. The published melt mass-flow rate for this grade is 0.9 g/10 min when tested at 190 °C and 2.16 kg load under ISO 1133-1:2022, and the density is 0.960 g/cm³ under ISO 1183-1:2019. Nozzle temperature is maintained in the 205–230 °C band, while the first-stage injection pressure is set between 80 MPa and 100 MPa; hold pressure is then stepped from 60% to 80% of the first-stage peak until gate freeze is confirmed by screw position stability. The mold is cooled with turbulent flow at 15–35 °C; lower mold temperatures shorten cycle time but increase frozen-in orientation and can elevate warpage in lattice-wall crates. The measured linear mold shrinkage for this density class typically falls between 1.5% and 2.5% in the flow direction and 0.8% to 1.5% transverse to flow, requiring gate placement in the geometric center of the crate base and rib-to-wall thickness ratios held below 0.6. For outdoor agricultural or automotive logistics use, a 2.0–2.5 wt% carbon black masterbatch is dispersed into the virgin pellet stream; UV resistance validation under ASTM G154-16 Cycle 1 is recommended, though published data specific to TAISOX 8009 at this carbon black loading is limited. The terminal articles are reusable ventilated crates and totes for automotive parts distribution and harvest logistics, with load-bearing sidewalls designed for column stacking and forklift access.
Open-head injection-molded pails in the 10–25 L class pose a drop-impact conflict when demolding occurs at the low end of the mold-temperature window. TAISOX 8009 is injected at a melt temperature of 210–230 °C and a mold temperature of 15–35 °C. Demolding at 15–20 °C reduces cycle time but leaves a high-crystallinity skin that can fail brittlely under impact. The gate is normally a single submarine gate into the pail base, producing a circumferential weld line at the handle-hole bridge; that weld line is the first point of failure in a UN drop test. The molding is held under pressure until gate freeze, with cooling time scaled to wall thickness squared—typically 18–25 s for 2.0 mm walls in a 16-cavity hot-runner tool. Formulation for food-contact pails uses 100% virgin TAISOX 8009, with only a 1.0–2.0 wt% HDPE-compatible color masterbatch. The compliance envelope includes FDA 21 CFR 177.1520 for olefin polymers and EU 10/2011 with an overall migration limit of 10 mg/dm² determined under EN 1186-1. For dangerous-goods pails, the finished container is evaluated under ASTM D5276-19 drop protocol after conditioning at −18 °C; a 1.2 m drop for Packing Group II liquids with relative density up to 1.2 is the common acceptance threshold. The terminal articles are open-head pails for water-based coatings, powders, food ingredients, and industrial chemicals where stacking and closure integrity are required.
| Compliance reference | Condition | Limit | Test standard |
|---|---|---|---|
| FDA 21 CFR 177.1520 | Olefin polymer, end-use extraction | Formulation-dependent | FDA extraction cells |
| EU 10/2011 | Overall migration, aqueous simulant | 10 mg/dm² | EN 1186-1 |
| UN 1H2 / 49 CFR 178.603 | Drop after −18 °C | 1.2 m PG II, d≤1.2 | ASTM D5276-19 |
TAISOX 8009 is selected for heavy-wall overcaps and plug-style tamper-evident inserts where section thickness exceeds 2.5 mm and the molded article must survive repeated torque application without stress whitening. The melt temperature is held at 215–235 °C; mold temperature is set to 20–40 °C. The mold fills through a direct pin gate with a diameter of 1.0–1.4 mm, and the gate enters the center of the top panel to avoid visible knit lines on the side knurl. Holding pressure is 70–80 bar, maintained until the gate freezes; premature hold release causes sink marks on thick knurled outer walls. Formulation for industrial closures uses 100% virgin TAISOX 8009 or a blend with up to 20% post-industrial regrind, provided the regrind is screened to remove fines below 1 mm and is not degraded by repeated processing. Environmental stress crack resistance is assessed under ASTM D1693-15 using a 10% Igepal CO-630 solution; the thicker sections of these articles allow the lower melt flow rate of 0.9 g/10 min to fill without the shear-induced surface defects observed in thin-wall closures. Compliance for personal-care and household chemical closures is evaluated under REACH and RoHS; food-contact overcap grades must be assessed under FDA 21 CFR 177.1520 because colorants and processing aids can alter migration behaviour. The terminal products are heavy-wall overcaps, plug-style tamper-evident inserts, and screw plugs for cosmetic and household chemical bottles. Operational boundary: TAISOX 8009 is not the appropriate feedstock for high-cavitation thin-wall beverage closures with wall sections below 0.8 mm; its published 0.9 g/10 min melt flow rate is below the 4–20 g/10 min range typical for such closures, and published data for this specific configuration is limited.
When a storage container or toolbox lid requires an integral living hinge that must survive repeated low-temperature flexing without an impact modifier, the polymer must retain molecular orientation through the hinge rather than rely on additive toughening. TAISOX 8009 is injected at 210–230 °C into a mold temperature of 15–30 °C; the hinge region is fed by a separate edge gate so that flow vectors cross the hinge perpendicular to the flex axis. The hinge thickness is held at 0.25–0.35 mm for a 1.5–2.0 mm nominal wall, and the gate is placed no farther than 3 times the wall thickness from the hinge to minimize frozen-in stress relaxation before the melt reaches the restricted section. Holding pressure is applied for 5–8 s, with cooling time of 12–18 s for a 1.8 mm wall. The formulation is 100% virgin TAISOX 8009 without nucleating agents; nucleating additives raise crystallinity and reduce hinge flex life. Flexural modulus under ISO 178:2019 for this density class is expected in the 900–1100 MPa range, and tensile yield stress under ISO 527-2:2012 is in the 25–32 MPa range. Compliance for toy-related products follows EN 71-3:2019 migration limits for specific elements and REACH Annex XVII restrictions; food-contact storage containers require FDA 21 CFR 177.1520. The terminal articles are hinged storage containers, toolbox organizers, and toy chests where the limiting artifact is hinge whitening or crack propagation after repeated flexing at −10 °C.
Structural foam pallet molding subjects the resin to a different thermal and pressure envelope than solid injection molding. TAISOX 8009 is metered with 0.3–0.8 wt% endothermic chemical blowing agent, typically sodium bicarbonate/citric acid masterbatch, and 0.2–0.5 wt% external lubricant to reduce shear heating during screw recovery. The press is sized by projected area; a 1,200 mm × 1,000 mm pallet mold with structural ribs requires clamp force above 1,800 tonnes, and the injection unit must deliver shot volume at fill speeds of 300–500 mm/s to maintain a uniform foamed core. Melt temperature is deliberately lowered to 195–210 °C; higher temperatures cause premature gas evolution before the melt reaches the flow front, producing surface blush and uneven density. Mold temperature is kept at 10–20 °C, and gas counterpressure of 0.2–0.5 MPa is applied through vent channels to control skin thickness. The part is packed only briefly—1–2 s—after fill because the expanding gas provides internal packing; excessive hold pressure collapses the cellular core and increases part mass. The density reduction relative to solid HDPE is commonly 10–20%, with skin thickness of 0.5–1.0 mm and a uniform closed-cell core. The terminal articles are export pallets, separator sheets, and rackable dunnage used in logistics; phytosanitary certification under ISPM 15 is not required for plastic pallets, but the finished pallet must meet fire-code and rack-load specifications required by the warehouse. Published data for TAISOX 8009 in this specific structural-foam configuration is limited; validation under ASTM D1185 for pallet bending and compression is advised.
Extrusion blow molding of small handleware up to 5 L imposes a balance between parison sag and pinch-off weld integrity. TAISOX 8009 runs on a continuous extruder with a 60 mm grooved-feed screw, L/D ratio of 24:1, and a barrier mixing section; melt temperature is held at 190–210 °C to limit parison sag. The die gap is set at 1.5–2.0 mm, with die swell adjusted by extruder speed and melt temperature; blow pressure is 0.6–0.8 MPa and blow time 8–15 s depending on wall thickness. Mold temperature is controlled at 10–20 °C to stabilize the pinch-off weld and prevent post-mold deformation. Because TAISOX 8009 has a published melt flow rate of 0.9 g/10 min, parison sag limits the practical container size; continuous molding of containers above 10 L is not recommended without a parison programmer or lower-MFR grade. Surface moisture above 0.05% by mass, typically observed after storage at relative humidity above 60%, requires pre-drying at 80 °C for 2 hours in a desiccant dryer to prevent streaking. The formulation is 100% virgin TAISOX 8009 with optional 1.0–2.0 wt% color masterbatch; post-consumer recyclate is not advised for food-grade containers unless validated. Compliance for household chemical containers follows REACH, RoHS, and UN 1H1 for non-bulk packaging where applicable; food-contact bottles require FDA 21 CFR 177.1520. The terminal articles are 1–5 L household chemical bottles, automotive fluids containers, and tight-head containers with an integrated molded handle.
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Formosa Plastics HDPE TAISOX 8009 is a high-density polyethylene injection moulding grade supplied in pellet form. The material is characterised by a nominal melt flow index of 9 g/10 min at 190 °C under 2.16 kg piston load when tested according to ASTM D1238-20 or ISO 1133-1:2022, and a nominal density of 0.960 g/cm³ at 23 °C when measured according to ASTM D1505-18 or ISO 1183-1:2019. These nominal values place the grade in the higher-flow segment of HDPE injection resins, intended for thin-wall housewares, industrial pails, crates, caps and closures, and toys. The product is not optimised for extrusion blow moulding, blown film, or pipe extrusion because the comparatively high melt flow reduces melt strength and parison stability. Relative to lower-MFR HDPE blow moulding grades such as TAISOX 8001, the resin exhibits lower melt viscosity at injection shear rates and shorter cooling-related cycle times, but at the cost of reduced sag resistance in continuous extrusion processes. Converter validation is required for critical dimensions, drop impact, and environmental stress crack resistance; published dynamic rheology data for the full shear-rate range of this specific grade is limited, and single-point melt flow index alone is not sufficient for mould-filling simulation.
Nominal property values reported for comparison are presented in Table 1. The values are typical lot-average data, not contractual specification limits, and should not be used for incoming inspection without a mutually agreed certificate of analysis. Test specimens are prepared by injection moulding according to ASTM D3641 or ISO 294-1, then conditioned at 23 °C ± 2 °C and 50 % ± 5 % RH for at least 40 h before testing. The comonomer content and catalyst package are proprietary; the grade behaves as a moderate-molecular-weight high-density polyethylene with the density and stiffness typical of an injection resin.
| Property | Test method | Nominal value |
|---|---|---|
| Melt flow index, 190 °C/2.16 kg | ASTM D1238-20 / ISO 1133-1:2022 | 9 g/10 min |
| Density, 23 °C | ASTM D1505-18 / ISO 1183-1:2019 | 0.960 g/cm³ |
| Tensile yield strength, 50 mm/min | ASTM D638-14 | 29 MPa |
| Elongation at break, 50 mm/min | ASTM D638-14 | >300 % |
| Flexural modulus, 1 % secant | ASTM D790-17 | 1100 MPa |
| Vicat softening temperature, 10 N | ASTM D1525-17 | 127 °C |
| Heat deflection temperature, 0.455 MPa | ASTM D648-18 | 75 °C |
Injection moulding should begin with the melt temperature measured at the nozzle between 200 °C and 240 °C. HDPE is non-hygroscopic and normally does not require pre-drying. If pellet surface condensation is observed after cold storage in humid conditions, dehumidified-air drying at 80 °C for 2 h is sufficient to remove surface moisture. The barrel residence time at melt temperatures above 230 °C should be kept below 6 min to reduce the risk of thermal-oxidative chain scission, yellowing, and loss of impact strength. A shot-to-barrel capacity ratio between 20 % and 80 % is recommended; lower ratios extend residence time, and higher ratios may reduce melt homogeneity. A cushion of 3–5 mm should be maintained at the end of the screw stroke to ensure consistent hold-pressure transfer. Back pressure of 0.5–1.5 MPa and screw speed of 80–120 min−1 are appropriate starting points for a reciprocating screw with L/D 20:1 and a compression ratio of 2.5–3.5:1. Excessive screw speed can generate viscous dissipation and raise melt temperature beyond the barrel set point without appearing on the nozzle thermocouple. Mould temperature of 20–40 °C is adequate for dimensional stability; lower mould temperatures can shorten cycle time but may increase residual stress and warpage in flat thin-wall parts. Hold pressure must be maintained until gate freeze. For a 1.5 mm wall section, gate-freeze time is typically 6–10 s, depending on gate diameter, melt temperature, and part geometry. Mould shrinkage after 48 h at 23 °C is typically 1.5–2.5 % in the flow direction and 1.5–2.0 % transverse. Regrind can be incorporated up to 20 wt% without significant loss of tensile yield strength in most applications, but impact strength and colour may shift; higher levels require production-line validation.
Table 2 lists starting conditions for a 50 mm diameter screw with L/D 20:1 and a reverse-taper or shut-off nozzle to prevent drool. These are generic starting points, not universal machine settings. Actual settings depend on mould design, runner geometry, shot weight, and hydraulic response.
| Parameter | Starting condition |
|---|---|
| Barrel rear temperature | 190 °C |
| Barrel middle temperature | 210 °C |
| Barrel front temperature | 220 °C |
| Nozzle temperature | 215 °C |
| Mould temperature | 20–40 °C |
| Hydraulic injection pressure | 60–90 MPa |
| Hold pressure | 50–70 MPa |
| Back pressure | 0.5–1.5 MPa |
| Screw speed | 80–120 min−1 |
In industrial pail moulding, a 20 L container with wall thickness 1.5–2.0 mm typically requires a clamp force from 150–350 tons depending on projected area and number of cavities. The grade has sufficient flow to fill multi-cavity pail moulds at injection speeds above 100 mm/s, but excessive speed above 150 mm/s can produce shear-induced flow marks at melt temperatures below 210 °C. For caps and closures, hot-runner valve-gate systems with sequential valve-pin opening reduce gas traps and gate blush; gate-freeze time and hold-pressure decay must be adjusted to prevent stringing and sink marks. Dimensional checks on closures should be performed after conditioning at 23 °C for 24–48 h because HDPE continues to shrink after demoulding. Warpage in large flat pail lids is controlled by balancing mould temperature between core and cavity; a differential of 5–10 °C is often sufficient to correct bow, but mould design and cooling-channel turbulence have greater influence than melt temperature changes.
Pellets should be stored in a clean, dry area away from direct sunlight and heat sources. Bulk silos and hoppers should be purged with dry air if ambient dew point exceeds 15 °C. Surface condensation on cold pellets transferred into a warm, humid plant can be avoided by allowing pellets to reach ambient temperature before opening liner bags. HDPE is not hygroscopic, so extended drying is not required and may cause oxidation at high temperatures.
A direct comparison with TAISOX 8001, a lower-MFR HDPE blow moulding grade, shows an order-of-magnitude difference in melt flow index. TAISOX 8001 is typically used in extrusion blow moulding where a melt flow index below 1.0 g/10 min provides the melt strength required to support a parison. TAISOX 8009, with a nominal MFR of 9 g/10 min, has lower melt viscosity under injection shear rates; this reduces injection pressure and cooling time in multi-cavity moulds but makes the material unsuitable for continuous parison extrusion because of sag and non-uniform wall thickness. The difference extends beyond melt flow. Lower-MFR blow moulding grades generally have higher molecular weight and better environmental stress crack resistance under conditions described in ASTM D1693, whereas the injection grade trades some long-term stress-crack resistance for flow. Components exposed to aggressive chemicals or sustained hoop stress should be evaluated on the finished article rather than on resin data alone.
When compared with high-MFR HDPE grades above 20 g/10 min, TAISOX 8009 retains higher tensile yield strength and better drop-impact toughness at the cost of slightly higher injection pressure and longer fill time. Against polypropylene impact copolymers of similar MFR, TAISOX 8009 has lower flexural modulus and lower heat deflection temperature under load, but lower density and generally better resistance to stress cracking in thin-wall containers at ambient temperature. Direct spiral-flow comparison data for TAISOX 8009 has not been published in widely available technical literature; mould-filling simulation should rely on the MFR and density inputs in Table 1 and be validated by short-shot trials on the intended machine. The grade is not suitable for rotational moulding because it is supplied in pellet form and the MFR is too high; rotational moulding requires powder grades with MFR below 5 g/10 min. It is also not intended for blown film, where low melt strength causes bubble instability and poor gauge control, or for pressure pipe, where long-term hydrostatic strength and slow crack growth resistance are critical.
The grade may be used in food-contact applications under FDA 21 CFR 177.1520 and EU 10/2011 if the supplier declaration supports the specific conditions of use. Converter responsibility includes migration testing under EU 10/2011 finished-article test conditions, because additives and colourants added downstream alter compliance. For chemical storage, HDPE TAISOX 8009 is generally resistant to aqueous acids, alkalis, and many polar solvents at ambient temperature, but continuous exposure to strong oxidising agents, chlorinated hydrocarbons, and aromatic solvents above 50 °C should be avoided because swelling and environmental stress cracking may occur. The material is not recommended for continuous load-bearing service above 80 °C; heat deflection temperature under 0.455 MPa is nominally 75 °C. Overheating above 260 °C can release irritating fumes, and adequate ventilation is required. For outdoor applications, carbon black or UV stabiliser masterbatches are required because unpigmented HDPE degrades under prolonged UV exposure.
In production-scale trials on thin-wall pails, surface defects such as flow marks and gate blush were observed when injection speed exceeded 150 mm/s at melt temperature below 210 °C; increasing melt temperature to 220–230 °C and reducing injection speed improved surface appearance. In multi-cavity closure moulding with hot runner valve gates, gate-freeze time and valve-pin sequencing must be adjusted to prevent stringing and sink marks. Venting depth should not exceed 0.02–0.03 mm for HDPE to avoid flash. These process adjustments are specific to mould geometry and runner balance and cannot be replaced by resin data alone.