| HS Code | 715160 |
| Melt Index | 6.0 g/10 min (190 °C/2.16 kg) |
| Density | 0.960 g/cm3 |
| Tensile Strength At Yield | 27.6 MPa (4,000 psi) |
| Tensile Strength At Break | 24.1 MPa (3,500 psi) |
| Elongation At Break | 600% |
| Flexural Modulus | 1.10 GPa (160,000 psi) |
| Notched Izod Impact | 53 J/m (1.0 ft-lb/in) |
| Shore D Hardness | 66 |
| Vicat Softening Point | 127 °C (261 °F) |
| Heat Deflection Temperature | 78 °C (172 °F) at 0.45 MPa |
| Melting Point | 132 °C (270 °F) |
| Coefficient Of Linear Thermal Expansion | 1.2E-4 /°C |
| Thermal Conductivity | 0.50 W/m·K |
| Volume Resistivity | >1E15 ohm-cm |
| Dielectric Constant | 2.3 at 1 MHz |
| Water Absorption | <0.01% |
| Mold Shrinkage | 0.015-0.025 cm/cm |
| Processing Temperature | 200-230 °C (392-446 °F) |
| Mold Temperature | 20-60 °C (68-140 °F) |
As an accredited Formosa Plastics HDPE TAISOX LH606 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Formosa Plastics HDPE TAISOX LH606 is supplied in 25 kg bags or 1,000 kg jumbo bags, palletized and stretch-wrapped. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with Formosa Plastics HDPE TAISOX LH606, 25 kg bags, palletized, shrink-wrapped, securely stowed for ocean shipment. |
| Shipping | Formosa Plastics HDPE TAISOX LH606 is shipped as non-hazardous polymer pellets in 25 kg bags, 1,000 kg jumbo bags, or bulk trucks/containers. Transport in cool, dry, ventilated conditions away from direct sunlight, ignition sources, and moisture. Handle with clean equipment to prevent contamination. |
| Storage | Store Formosa Plastics HDPE TAISOX LH606 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, sparks, flames, and oxidizing agents. Keep original bags or containers tightly closed, palletized off the floor. Prevent moisture, dust, and contamination. Use first-in, first-out rotation, avoid excessive stacking, and control static buildup. Store separately from incompatible materials. Follow local regulations and SDS guidance. |
| Shelf Life | Shelf life is typically 24 months when stored unopened in a cool, dry, well-ventilated area away from direct sunlight and moisture. |
Extrusion blow molding of UN-certified large-part packagings from HDPE TAISOX LH606 is executed on single-station accumulator machines with screw diameters of 80–120 mm, L/D ratios of 20:1–30:1, and clamp force settings from 1,000 kN upward for multi-diameter parison dies. The grade’s high molecular weight, with a melt flow rate typically reported below 0.1 g/10 min under ASTM D1238 at 190°C/2.16 kg and a density in the 0.940–0.950 g/cm³ range under ASTM D1505, supplies the parison hang strength required for closed-head and open-head drums from 20 L to 220 L. Compliance for transport of dangerous goods is maintained under UN Model Regulations Chapter 6.1, ADR 6.1.5, IMDG Code 6.1, and 49 CFR Parts 171–178, with packaging designations 1H1, 1H2, 3H1, and 3H2 applicable. A production-validated formulation uses LH606 as the sole structural resin at 100 parts by weight, with carbon black masterbatch at 2.0–4.0 wt% for ultraviolet opacity and surface charge dissipation, or non-black color concentrate at 1.0–2.5 wt% for product identification. Internal lubricants and processing aids are restricted to ≤0.3 wt% because surface migration from excess additive reduces pinch-off weld strength at the mold parting line. Downstream processing requires axial or radial parison programming to redistribute wall thickness at the top skirt, chime, and base corner; barrel temperatures are set at 180–210°C, mold cooling water at 10–30°C, and blow air pressure at 0.6–0.9 MPa. Cycle times depend on shot weight and range from 60 s for 20 L jerrycans to 180 s for 220 L L-ring drums. Terminal products include UN-rated 20–30 L jerrycans, 60 L and 120 L tight-head drums, 200–220 L L-ring drums, and open-head drums with clamp-ring closures.
| Compliance area | Standard/test method | Qualification equipment |
|---|---|---|
| Design type drop test | 49 CFR §178.603; UN Model Regulations 6.1.5.3 | Drop frame with fixed release head, conditioning chamber at −18°C |
| Leakproofness test | 49 CFR §178.604; ADR 6.1.5.4 | Differential pressure decay test with full immersion soap film |
| Hydrostatic pressure test | 49 CFR §178.605; IMDG Code 6.1.5.5 | Hydraulic pump with calibrated pressure transducer, hold time 30 min |
| Stacking load | 49 CFR §178.606; UN Model Regulations 6.1.5.6 | Compression stack fixture with load cells, 28 days at 40°C |
High-molecular-weight HDPE TAISOX LH606 is selected as the structural polyethylene phase in automotive fuel tank coextrusion because its melt strength preserves parison integrity during accumulator-head extrusion of six-layer structures, particularly for saddle-shaped tanks exceeding 800 mm in length. Monolayer HDPE cannot meet evaporative hydrocarbon limits under EPA 40 CFR Part 86 and CARB LEV III; a barrier layer is therefore required. Formulation for the coextruded wall uses LH606 compounded with carbon black masterbatch at 2.0–3.0 wt% in the outer layer for UV stability, while the inner conductive layer uses LH606 with conductive carbon black to a surface resistivity of 10⁶–10⁹ Ω/sq. EVOH barrier resin is predried to below 0.03% moisture before feeding, typically at 80°C for 4–6 h, to prevent hydrolysis-induced barrier defects. Processing is performed on six-extruder accumulator-head machines with gravimetric dosing, 20–50 point parison programming, barrel temperatures of 200–230°C for LH606, mold temperatures of 10–40°C, and blow air pressure of 0.7–1.0 MPa. After demolding, pinch-off flash is granulated in-house and reintroduced into the regrind layer up to 45% of total wall thickness. Terminal products include gasoline fuel tank shells from 35 L to 100 L, diesel tank bodies, and coextruded filler neck subassemblies. Published long-term permeation data for methanol-blend fuels above 15% methanol in this specific LH606 configuration is limited; qualification testing under the intended fuel composition is required before serial production.
| Layer function | Material composition | Wall thickness fraction |
|---|---|---|
| Outer HDPE structural | LH606 + carbon black masterbatch 2.0–3.0 wt% | 20–30% |
| Adhesive/tie | Maleated LLDPE | 1.0–2.0% per side |
| Hydrocarbon barrier | EVOH 27–44 mol% ethylene | 1.5–3.0% |
| Regrind structural | Clean in-house flash from LH606 structures | 30–45% |
| Inner conductive HDPE | LH606 + conductive carbon black to 10⁶–10⁹ Ω/sq | 5–10% |
For agricultural containers carrying emulsifiable concentrates and solvent-based pesticides, HDPE LH606 is converted on shuttle blow molding machines with 50–80 mm screws and 22:1–28:1 L/D ratios. Classification is maintained under UN Model Regulations Chapter 6.1 for Packing Group II liquids, EU CLP Regulation (EC) No 1272/2008, and EPA 40 CFR Part 156 labeling and packaging requirements. Barrier performance is achieved either by in-line coextrusion of a polyamide or EVOH layer representing 5–10% of total wall thickness, or by post-molding surface fluorination yielding surface fluorine levels of 0.5–1.5%. The HDPE phase is formulated with 100 parts by weight LH606; carbon black masterbatch is added at 2.0–4.0 wt% to suppress photooxidation during outdoor farm storage, and antioxidant masterbatch is added at 0.2–0.5 wt% only for sustained storage above 35°C. Parison programming controls wall thickness from 1.5 mm at the neck to 4.0 mm at the base chime. Extrusion head temperatures are held at 190–220°C, mold cooling water at 10–25°C, and post-mold leak testing is performed at 0.02 MPa differential pressure. Terminal pack types include 5 L, 10 L, 20 L, and 25 L tight-head herbicide, insecticide, and fungicide containers, as well as 1H1 farm concentrate drums with bung closures.
Tank bodies produced from HDPE LH606 for 32.5 wt% urea solution must satisfy low-extractables requirements because ionic contamination accelerates urea decomposition and ammonia outgassing. Compliance is verified under ISO 22241-1, ISO 22241-2, ISO 22241-3, DIN 70070, and AUS 32 specifications. The compound is formulated at 100 parts by weight LH606 with no regrind in the product contact layer; white TiO₂ masterbatch is used at 1.5–2.5 wt% to reduce UV transmittance, and antioxidant masterbatch is used at 0.2–0.5 wt%. Carbon black is excluded from the internal layer because its extractables can exceed DEF conductivity and alkalinity tolerances. Complex on-vehicle tanks are produced by 3D blow molding or suction blow molding to move pinch-off weld lines away from dynamic load areas. Parison wall thickness is programmed between 3 mm and 6 mm, cooling water is maintained at 10–25°C, and all product-contact surfaces are rinsed with deionized water after demolding to remove low-molecular-weight surface residues. Terminal products include 10–30 L underfloor DEF tanks, 5–10 L service portables, and inner liners for DEF IBCs. Copper-containing fittings and brass inserts are avoided in the melt stream and in final assembly unless isolated from urea contact.
Closed-head potable water tanks in the 20–120 L range are blow molded from unpigmented HDPE TAISOX LH606 on accumulator machines with 60–100 mm screws and clamp forces up to 800 kN. Material compliance is anchored to FDA 21 CFR §177.1520(c) olefin polymer clearance, EU 10/2011 overall migration limit of 10 mg/dm², NSF/ANSI/CAN 61, and WRAS for water contact fittings in the United Kingdom. The compound uses 100 parts by weight LH606, with clean in-house flash restricted to ≤10%; blue masterbatch is used at 2.0–3.0 wt% only where customer tinting is specified, and external mold release agents are excluded to avoid surface residue. Melt temperature is maintained at 180–210°C, die tooling is sized to 30–70% of article diameter for interlocking flow fronts, and blow air pressure is held at 0.6–0.8 MPa. Cooling time ranges from 60 s to 180 s depending on shot weight and wall thickness. Post-mold cooling fixtures maintain neck dimensional tolerance before cap torque testing. Terminal products include 20 L carboys, 60 L closed-head drums, 100–120 L water storage vessels, and shells for water treatment expansion tanks hydrostatically tested to 1.1× design working pressure. Continuous service above 60°C is not recommended for load-bearing pressure vessels without a supplementary design factor.
HDPE TAISOX LH606 is processed on twin-station shuttle blow molding machines with 50–80 mm screws and 24:1 L/D ratios for windshield washer reservoirs, coolant expansion bottles, and headlamp cleaning tanks. Low-temperature impact and thermal cycling are validated under ISO 16750-4 with cycling from −40°C to 85°C, and fitting retention is checked after 500 cycles. The compound consists of 100 parts by weight LH606, heat-stabilized color masterbatch at 2.0–3.0 wt%, and antioxidant masterbatch at 0.2–0.5 wt%. Plasticizers or rubber modifiers are not used because environmental stress crack resistance and weld-line elongation are supplied by the base molecular weight. Parison programming controls localized wall thickness from 1.5 mm to 3.0 mm at pinch-off regions; needle blowing is performed at 0.6–0.8 MPa, mold temperatures are held at 10–30°C, and in-mold trimming is followed by hot-plate leak testing at 0.03 MPa. Terminal products include 2–6 L washer bottles, 3–8 L coolant overflow reservoirs, and 4–6 L headlamp cleaning tanks. Molded bosses are preferred over brass inserts in vibration-loaded areas because the differential expansion coefficient of metal inserts creates stress risers at the HDPE boss root after thermal cycling.
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