| HS Code | 704985 |
| Density | 0.956 g/cm³ |
| Melt Flow Rate 190 C 2 16 Kg | 0.05 g/10 min |
| Tensile Strength At Yield | 26 MPa |
| Tensile Strength At Break | 30 MPa |
| Elongation At Break | 600% |
| Flexural Modulus | 1200 MPa |
| Notched Izod Impact Strength | 200 J/m |
| Vicat Softening Temperature | 125°C |
| Heat Deflection Temperature | 70°C |
| Shore D Hardness | 65 |
| Environmental Stress Crack Resistance Escr | >1000 h |
| Mold Shrinkage | 2.0% |
| Melting Temperature | 133°C |
| Brittleness Temperature | < -70°C |
As an accredited Formosa Plastics HDPE TAISOX 8001U factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Formosa Plastics HDPE TAISOX 8001U is packaged in 25 kg polyethylene-lined woven bags, palletized and shrink-wrapped for shipment. |
| Container Loading (20′ FCL) | 20′ FCL loading: Formosa Plastics HDPE TAISOX 8001U, 25 kg bags, palletized, stretch-wrapped, and secured for safe ocean shipment. |
| Shipping | Formosa Plastics HDPE TAISOX 8001U is shipped as non-hazardous polyethylene resin pellets in 25 kg bags, jumbo bags, or bulk containers. Use clean, dry trucks or containers, avoiding moisture, heat, and contamination. No dangerous goods classification applies; keep packaging sealed, labeled, and stored in a dry, ventilated area. |
| Storage | Store Formosa Plastics HDPE TAISOX 8001U indoors in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and flames. Keep original bags or containers closed to prevent moisture, dust, and contamination. Avoid prolonged UV exposure and excessive stacking. Segregate from strong oxidizers. Protect from physical damage. Follow the manufacturer’s SDS and local regulations. |
| Shelf Life | Shelf life is approximately two years when stored cool, dry, well-ventilated, sealed, and protected from direct sunlight. |
Formosa Plastics HDPE TAISOX 8001U is a high-density polyethylene injection-molding grade with a nominal melt flow index of 8.0 g/10 min determined according to ISO 1133-1:2022 at 190 °C under 2.16 kg load and a density of 0.960 g/cm³ measured per ISO 1183-1:2019. The material is processed in conventional screw injection machines and thin-wall high-speed tools; its narrow molecular weight distribution supports high-speed filling of thin and thick sections but also creates process sensitivities in weld-line areas and rapid gate freeze-off. The resin does not require pre-drying under normal dry-flow conditions, but surface condensation on granules stored at relative humidity above 60% may cause splay; hopper drying at 70–80 °C for 1–2 h eliminates this without degrading the stabilizer package. The application scenarios below address only those downstream sectors where this grade is actually used: industrial open-head pails, beverage closures, returnable transport crates, thin-wall food storage, outdoor seating shells, and irrigation micro-fittings.
A 25-L open-head pail injection molded from TAISOX 8001U in a single-cavity or dual-cavity tool is qualified as a UN 1H2 open-head plastics drum when the wall stock distribution, handle configuration, and gasketed lid closure satisfy the UN Model Regulations chapter 6.1 design-type test sequence, including drop, leakproofness, hydraulic pressure, and stacking tests. The grade’s density of 0.960 g/cm³ measured per ISO 1183-1:2019 and melt flow index of 8.0 g/10 min per ISO 1133-1:2022 allow production of thick rims and bases without excessive melt pressure, but the solidification window is narrow enough that bosses, handle lugs, and latch undercuts develop sink marks when local wall thickness exceeds the nominal 2.5–3.5 mm sidewall by more than 40%. For dark blue or black chemical pails, the resin is let down with 2.0–4.0 wt% of a high-load carbon black or organic pigment masterbatch carried in an HDPE or LLDPE base, while 0.05–0.15 wt% of a migratory slip/antiblock package is added where pails are nested and denested on automatic filling lines; clean in-house regrind from sprues and rejected parts is incorporated up to 20–30 wt% without measurable loss of UN drop performance when the regrind stream excludes mineral oil melt lubricants and silicone mold-release agents, which act as stress-concentration sites at the gate weld region. The pail is molded on a hydraulic or hybrid injection molding machine with clamp force between 600 t and 1,000 t for single-cavity tools, using a direct hot sprue or valve-gated hot runner into a diaphragm gate; barrel melt temperature is maintained between 190 °C and 230 °C, and coolant inlet temperature is kept below 10 °C to freeze the thick rim before ejection, because premature ejection at surface temperatures above 60 °C produces rim ovality and lid sealing failures. Terminal articles include open-head chemical pails, paint pails, and food-grade shortening buckets, usually fitted with injection-molded lids and tamper-evident tear strips; food-contact versions use a food-grade antioxidant system and comply with 21 CFR 177.1520 and EU Regulation (EU) No 10/2011.
Beverage closures molded from TAISOX 8001U in 48- and 64-cavity hot-runner tools are driven by the melt flow index of 8.0 g/10 min; the resin fills 1.8–2.5 mm top panels and 0.8–1.2 mm tamper-band bridges within injection times of 0.2–0.4 s on accumulator-assisted machines reaching screw forward velocities above 250 mm/s. Compliance for food-contact closures is governed by 21 CFR 177.1520(c) for olefin polymers and EU Regulation (EU) No 10/2011, with an overall migration limit of 10 mg/dm²; closure functionality is validated under ISO 13422 for removal torque, but published data for this specific grade’s torque retention on carbonated beverage finishes is limited and should be verified on the customer’s PCO-1881 finish and liner design. The formulation is dry-blended or compounded with 1.0–3.0 wt% titanium dioxide or color masterbatch for white and custom caps, 0.05–0.15 wt% erucamide slip additive to reduce removal torque after bridge slitting, and 0.05–0.10 wt% phenolic or phosphite antioxidant; slip loadings above 0.15 wt% generate cap surface haze and inkjet coding adhesion failures, while insufficient slip produces removal torques above 1.5 N·m and consumer rejection. Processing uses a cold runner or hot tip gate into the outer top panel, with melt temperature between 200 °C and 240 °C, mold temperature 10–20 °C, and cycle time 5–8 s; after ejection, the closures are slit with rotating blade stations to fracture the designed bridges, and residual closure ovality above 0.4 mm leads to downstream vision-system sortation rejects. Terminal articles include tamper-evident screw caps for carbonated soft drinks, bottled water, and edible oil, typically produced with PE liners or linerless bore-seal geometry; child-resistant closure variants require additional shell redesign and testing under ISO 8317, independent of the base resin.
Returnable beverage crates and logistics trays molded from TAISOX 8001U are subjected to repeated rough handling, compressive stacking, and hot-water washdown cycles; the grade is used at wall thicknesses of 2.5–4.0 mm for sidewalls and 4.0–6.0 mm for bases, but reducing sidewall gauge below 2.0 mm triggers sidewall buckling under compressive loads even though the 8.0 g/10 min melt flow index would permit filling thinner sections. Compliance for returnable transport packaging is evaluated under ISO 8611-1:2021 for pallet and crate load resistance and ASTM D4169-22 distribution-cycle test protocols; food-contact crate formats used in bakeries and produce packing require EU Regulation (EU) No 10/2011 migration testing and 21 CFR 177.1520 for U.S. food handling. UV-stabilized crate formulations incorporate 2.0–4.0 wt% of a hindered amine light stabilizer plus carbon black or inorganic UV masterbatch, along with 15–30 wt% clean internal regrind; higher regrind fractions above 30 wt% lower notched Izod impact energy and increase brittle failure at injection weld lines when crates are dropped at −10 °C. Crates are typically molded on large-tonnage injection presses from 700 t to 1,500 t using multiple hot-tip gates to prevent premature freeze-off in long flow paths; barrel temperatures are held in the 200–230 °C range and fill time is controlled below 1.5 s to avoid flow hesitation at the intersection of rim ribs and base grid structures. Weld line strength is the critical control point, and low clamp force or early transfer from velocity to pressure control produces visible knit lines at the center gate junction that fail during side-impact or drop tests. Terminal articles include 12- and 24-bottle beverage crates, bakery trays, produce field crates, and industrial parts bins; outdoor storage use is common when the formulation includes UV stabilizers and when the finished part is tested under ISO 4892-2:2013.
Thin-wall food storage containers manufactured from TAISOX 8001U in high-speed hybrid machines exploit the material’s 8.0 g/10 min melt flow to fill wall sections between 0.6 mm and 1.2 mm at injection speeds above 300 mm/s; the grade is used without plasticizers, and finished articles are tested under 21 CFR 177.1520 and EU Regulation (EU) No 10/2011 for overall migration not exceeding 10 mg/dm², with migration testing according to EN 1186-1 where the container is marketed for microwave reheating. Color and additive packages are kept deliberately lean to preserve organoleptic neutrality: 1.0–2.0 wt% masterbatch in a matched LDPE carrier, 0.05–0.10 wt% phosphite antioxidant, and 0.02–0.05 wt% acid scavenger; no slip agent is used for microwave reheat applications because free erucamide migrates and contributes to off-taste above 60 °C. The process uses thin-wall injection molding with sequential valve gating and conformal cooling inserts to hold mold temperature between 8 °C and 15 °C; clamp force ranges from 350 t to 650 t for multi-cavity tools, and cycle time is dominated by cooling rather than mold fill. Flash formation at parting lines below 0.1 mm is a recurring issue when injection pressure exceeds 1,800 bar on worn platens or when the clamp force is insufficient for the projected cavity area. Terminal articles include reusable food storage containers, microwave-safe lids, kitchen organizers, and disposable thin-wall trays; these products are not intended for carbonated beverage packaging because the thin-wall geometry lacks pressure retention design features.
Outdoor furniture shells molded from TAISOX 8001U in gas-assisted or structural-foam injection processes use the grade’s density and stiffness to produce ribbed seat and back components; the UV-stabilized grade is further let down with 3.0–5.0 wt% of a HALS-plus-benzotriazole UV masterbatch for articles stationed in continuous sun, because unstabilized high-density polyethylene loses impact strength rapidly under ISO 4892-2:2013 xenon arc exposures exceeding 1,500 kJ/m². Compliance for the finished furniture item is assessed per EN 581-1:2017 for general safety and durability of outdoor seating, while plastic components used in playground equipment may require ASTM F1487-21 or regional equivalents. Formulations also use 1.0–2.0 wt% color concentrate and up to 20 wt% clean internal regrind; because outdoor exposure causes HDPE to embrittle, the use of mixed-lot regrind above 20 wt% is avoided in load-bearing seat shells to maintain notched impact energy above 4 kJ/m² at −20 °C. Manufacturing often uses gas-assisted injection molding to core out thick armrest and seat ribs without sink marks; nitrogen gas is injected at 150–250 bar into melt-filled channels after 60–80% volumetric fill, and the mold is held at 20–40 °C. The gas channels must be segregated from gate freeze-off, otherwise gas blow-through occurs and produces microvoids that reduce weathering resistance and load-bearing capacity. Terminal articles include resin outdoor chairs, benches, poolside loungers, stadium seats, and garden storage chests; these products compete with polypropylene but use HDPE where low-temperature impact and detergent washdown resistance are specified.
Drip irrigation emitters, micro-sprinklers, and low-pressure irrigation fittings molded from TAISOX 8001U require dimensional stability for barbed insert retention and leak-free sealing; the grade’s melt flow index of 8.0 g/10 min permits filling small chambers with wall thicknesses down to 0.8 mm without excessive injection pressure. Compliance is linked to potable water contact requirements under ISO 4427-1:2019 and NSF/ANSI 61 where the fitting is used in drinking-water systems, while agricultural irrigation fittings are generally evaluated under regional drip-irrigation standards. Formulation practice uses 2.0–3.0 wt% carbon black masterbatch for UV resistance, and regrind is limited to 10–15 wt% because small orifices in emitters are sensitive to gel particles and dimensional variation. Processing is performed on small- to medium-tonnage injection machines from 120 t to 350 t with hot-runner valve gates because multi-drop emitter bodies have thin diaphragms; melt temperature is held between 190 °C and 220 °C, and melt residence time is restricted to prevent gel formation, which blocks emitter flow paths. Terminal products include drip emitter bodies, barbed connectors, micro-sprinkler heads, and low-pressure irrigation stakes used in greenhouse and field irrigation networks.
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Formosa Plastics HDPE TAISOX 8001U is a high-molecular-weight high-density polyethylene resin supplied in pellet form for blown film extrusion. The grade is specified with a nominal melt flow index of 0.08 g/10 min determined at 190 °C under a 2.16 kg load using ASTM D1238-20 and a nominal density of 0.949 g/cm³ determined by ASTM D1505-18. These two values place the material in the HMW-HDPE film class, where the low melt flow index is accompanied by high melt strength and a broad molecular weight distribution. The resin is intended for high-strength thin-gauge blown film applications, including T-shirt grocery sacks, produce bags, garbage can liners, drum liners, and industrial liners. Compared with conventional medium-molecular-weight HDPE film grades, TAISOX 8001U retains higher zero-shear viscosity and greater bubble stability, enabling down-gauging to 10–25 µm while maintaining load-bearing performance. The low melt flow index also raises extruder head pressure and torque demand, which must be accommodated through screw design and temperature selection.
The suffix U in TAISOX 8001U should be verified against the supplier’s additive statement. Where the U designates UV stabilization, the resin differs from non-UV HMW-HDPE film grades by reduced molecular weight degradation during outdoor ultraviolet exposure and longer film color retention; where the suffix does not carry that meaning on the lot-specific datasheet, the additive package should be assumed limited to processing and thermal stabilizers only. This distinction affects warehouse storage near direct sunlight and any open-air liner use.
Melt flow index is not the only flow parameter controlling processability. Under ASTM D1238-20 at 190 °C and a 21.6 kg load, HMW-HDPE film resins of this class typically exhibit a high-load melt flow index between 6 and 9 g/10 min. The resulting flow ratio, generally stated as HLMI/MI, falls between 80 and 110. This high flow ratio indicates strong shear thinning, which is essential for extruding a low-MI resin through the narrow die lips used in high-density film. At constant shear stress, the molecular weight distribution is broad enough to reduce viscosity in the die while retaining bubble integrity above the air ring.
Capillary rheometry on this polymer class shows apparent shear viscosity near 2,000–3,000 Pa·s at 100 s⁻¹ and below 500 Pa·s at 1,000 s⁻¹ when measured at 190 °C. The extensional viscosity of the high-molecular-weight fraction produces strain hardening under uniaxial extension, delaying bubble rupture at high draw-down ratios. These rheological features permit the wide blow-up ratios and moderate frost line heights used in HMW-HDPE film processing.
On a 75 mm barrier-screw extruder with an L/D of 30:1 and a 150 mm die, stable operation is typically reached at screw speeds between 40 and 70 rpm with a die gap of 1.5–2.0 mm. Head pressure can exceed 350 bar at outputs above 80 kg/h, depending on melt temperature and die gap. Grooved-feed extruders improve feed stability but increase shear heating in the feed zone, requiring more intensive cooling. Batch-to-batch variation in pellet bulk density and particle size distribution can shift output by 3–5% and alter gauge uniformity across the web.
Barrel temperatures for the grade are run in a flat-to-reverse profile: hopper at 170–180 °C, compression at 190–205 °C, metering at 205–220 °C, and die at 210–220 °C. The melt stream should remain between 190 °C and 220 °C. Exceeding 230 °C may deplete the antioxidant package, increase gel formation, and produce off-odor. Running below 180 °C increases screw motor load, reduces output, and may initiate melt fracture at the die lip. Die gap reduction below 1.0 mm at melt temperatures under 200 °C can raise wall shear stress above the sharkskin threshold for this high-molecular-weight resin, producing rough film surfaces. Processors without fluoropolymer processing aid should open the die gap or increase die temperature to clear surface roughness.
Commercial lines running TAISOX 8001U for thin-gauge sacks normally target film thicknesses between 10 µm and 25 µm. Under ASTM D1709-16a Method A, a 25 µm film produced at a 2.0 mm die gap and a 4:1 blow-up ratio typically shows dart impact values between 140 and 160 g. Elmendorf tear values by ASTM D1922-15 are orientation-dependent; machine-direction tear is commonly below 50 gf, while transverse-direction tear exceeds 200 gf. This imbalance is intrinsic to uniaxially drawn HMW-HDPE bubble film and can be shifted by lowering blow-up ratio or increasing die gap. High-speed bag conversion seals are run at jaw temperatures of 130–150 °C, depending on line speed and dwell.
In waste liners, dart impact is not the only criterion. The broad molecular weight distribution contributes to environmental stress crack resistance measured under ASTM D1693-15 Condition B, with HMW-HDPE film grades commonly exceeding 300 h before 50% failure, though exact lot-specific values for TAISOX 8001U must be drawn from the certificate of analysis. Creased film and gusseted liners should be tested on folded sections because orientation at crease lines can reduce crack initiation time. Slow puncture and retained tear after folding are preferred methods for heavy-duty liner qualification.
Representative nominal values for this HMW-HDPE film resin class are listed below. The certificate of analysis for each lot prevails over class-level ranges because comonomer, additive package, and reactor conditions can shift results within the specification window.
| Property | Method | Nominal range or value |
|---|---|---|
| Melt flow index, 190 °C/2.16 kg | ASTM D1238-20 | 0.07–0.09 g/10 min |
| High-load melt flow index, 190 °C/21.6 kg | ASTM D1238-20 | 6–9 g/10 min |
| Density, 23 °C | ASTM D1505-18 | 0.948–0.952 g/cm³ |
| Tensile yield strength, MD/TD | ASTM D882-18 | 26–30 / 25–29 MPa |
| Tensile elongation at break, MD/TD | ASTM D882-18 | 550–700 / 600–800 % |
| Elmendorf tear, MD/TD | ASTM D1922-15 | 20–50 / 200–400 gf |
| Dart impact, 25 µm film | ASTM D1709-16a Method A | 120–180 g |
| Vicat softening temperature | ASTM D1525-17 | 122–127 °C |
Tensile and tear values are film-direction dependent. Comparisons between lots should be normalized for gauge, blow-up ratio, die gap, and frost line height. Compression-molded data cannot be substituted for film data in tear and impact evaluations.
Food-contact compliance for polyethylene homopolymer or copolymer film is normally established under 21 CFR 177.1520. TAISOX 8001U may be used in food-contact applications only when the finished article meets the extractive limitations, additive restrictions, and end-use conditions specified in that section. European food-contact approval is not automatic; migration testing under Regulation (EU) No 10/2011 is required on the finished film, because migration levels depend on film thickness, temperature, and food simulant. The resin is subject to REACH Regulation (EC) No 1907/2006. For electrical and electronic equipment, the finished component must comply with Directive 2011/65/EU and any delegated directives; the base polyethylene does not contain regulated heavy metals as intentionally added substances, but masterbatch pigments and concentrates can alter compliance.
Substitution of a conventional medium-molecular-weight HDPE film resin with a melt flow index near 0.25 dg/min by TAISOX 8001U affects pressure, output, and film orientation. The first observed change is usually higher head pressure and lower screw output for the same screw speed. Barrel temperatures may be raised by 5–10 °C to reduce viscosity, but the melt temperature at the die should remain at or below 220 °C. The die gap should be opened from 1.0–1.2 mm to 1.5–2.0 mm to lower wall shear stress and prevent sharkskin. If the bubble breathes or MD tear becomes unacceptable, blow-up ratio may be reduced from 4.5:1 to 3.5:1. These adjustments follow from the higher flow ratio and melt elasticity of high-molecular-weight HDPE; they are not grade-specific but are more pronounced with TAISOX 8001U than with lower molecular weight film resins.
Converters moving in the opposite direction, from HMW-HDPE to medium-molecular-weight HDPE, typically gain output but lose bubble stability and dart impact. Conversion from TAISOX 8001U to a 0.25 dg/min grade may allow lower head pressures and higher screw speeds, but the film may no longer support the same down-gauging without bubble instability or impact failure. The choice between grades should therefore be made on the basis of minimum web thickness, conversion speed, and seal-strength requirements.
High-density polyethylene liners made from TAISOX 8001U are used with aqueous wastes, dilute acids, and alkaline solutions at ambient temperature. The resin tolerates polar solvents and water; however, continuous contact with strong oxidizing acids, aromatic hydrocarbons, and halogenated solvents can soften, swell, or stress-crack the polymer. Under ASTM D543-21, weight and dimension change data for this specific formulation are limited; therefore chemical compatibility for non-aqueous wastes should be verified by immersion testing on the actual film at the relevant temperature and contact time. Environmental stress crack resistance under constant strain is typically better for this HMW-HDPE film class than for medium-molecular-weight HDPE, but the result is modified by comonomer content, additive package, and film orientation. Creased liner sections and heat-sealed seams are the preferred test sites for stress crack initiation because processing orientation and thickness reduction at seals can reduce time to cracking.
Pellet handling follows standard polyethylene practice. TAISOX 8001U is not hygroscopic and does not require desiccant drying when stored indoors. If pellets have been exposed to temperature cycles causing surface condensation, they should be conditioned in a hopper at 20–23 °C before extrusion to avoid surface streaking. The resin should be kept away from ignition sources and strong oxidizing agents. Edge trim and clean regrind can be reused at addition levels up to 20 wt% without substantial gel formation; higher reuse rates can raise film gel count and haze and shift the molecular weight distribution toward lower viscosity.
Published data for high-speed conversion of TAISOX 8001U into printed T-shirt sacks is limited because seal, print, and perforation settings depend on converter-specific equipment. The grade is not intended for injection molding, blow molding, pipe extrusion, or pressure pipe service; these applications require different molecular weight ranges and additive packages. Processors should confirm the grade-specific certificate of analysis and safety data sheet before changing production formulations.