| HS Code | 424038 |
| Density | 0.950 g/cm³ |
| Melt Index | 6.0 g/10 min |
| Tensile Strength At Yield | 28 MPa |
| Elongation At Break | 1000% |
| Flexural Modulus | 1.2 GPa |
| Hardness Shore D | 65 |
| Vicat Softening Temperature | 124°C |
| Brittleness Temperature | -70°C |
| Melting Point | 130°C |
| Coefficient Of Linear Thermal Expansion | 1.2E-4 cm/cm/°C |
| Thermal Conductivity | 0.45 W/m·K |
| Dielectric Constant | 2.3 |
| Dielectric Strength | 20 kV/mm |
| Dissipation Factor | 0.0003 |
| Volume Resistivity | 1E15 ohm·cm |
| Water Absorption | 0.01% |
| Environmental Stress Crack Resistance | >1000 h |
| Mold Shrinkage | 1.5-3.0% |
| Melt Temperature | 200-260°C |
| Mold Temperature | 20-60°C |
| Ul Flammability Rating | HB |
As an accredited Chevron Phillips Chemical HDPE 9506 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Chevron Phillips Chemical HDPE 9506 is supplied in 25 kg polyethylene bags, palletized and stretch-wrapped for secure transport. |
| Container Loading (20′ FCL) | A 20′ FCL typically loads Chevron Phillips Chemical HDPE 9506 in 25 kg bags, palletized or floor-loaded, about 25 metric tons. |
| Shipping | Chevron Phillips Chemical HDPE 9506 is shipped as non-hazardous high-density polyethylene resin pellets in 25 kg bags or bulk hopper cars/trucks. Pallets are stretch-wrapped and kept dry. No dangerous goods classification is required. Store in a cool, dry, clean area away from heat, moisture, UV, and contamination. Use covered transport. |
| Storage | Store Chevron Phillips Chemical HDPE 9506 in a cool, dry, well-ventilated warehouse, away from direct sunlight, heat, ignition sources, and incompatible materials such as oxidizers. Keep original containers or bags closed to prevent moisture and contamination. Protect from UV exposure and excessive stacking. Use first-in, first-out inventory. Ensure clean, dry storage conditions. Follow the manufacturer’s SDS and local regulations. |
| Shelf Life | Chevron Phillips Chemical HDPE 9506 has no defined shelf life; store unopened in cool, dry conditions away from direct sunlight. |
Where rigid intermediate bulk packaging must survive drop, hydraulic, and stacking loads under UN 1H1/1H2 certification, Chevron Phillips Chemical Marlex HDPE 9506 is specified for tight-head and open-head drum bodies because its high-load melt flow rate, determined under ASTM D1238 at 190 °C/21.6 kg, supports parison integrity at large part weights. Production-scale accumulator extrusion blow molding lines running 100 phr HDPE 9506 with 20–50 wt% in-house regrind, 0.5–2.0 wt% carbon black masterbatch, and 0.1–0.3 wt% hindered amine light stabilizer must hold melt temperature between 200 °C and 230 °C; exceeding 230 °C accelerates oxidative degradation of regrind fractions, while falling below 200 °C increases head pressure and reduces parison wall-thickness uniformity. The parison is extruded through a die gap of 1.5–2.5 mm, preblown to 0.02–0.05 MPa, then captured in a closed mold and expanded at 0.5–0.7 MPa air pressure. Certified drum formulations are conditioned by the relevant inspection body under 49 CFR 178.504 drop criteria and ASTM D1998-21 upright tank design requirements, while environmental stress crack resistance under ASTM D1693 Condition A must be verified when regrind exceeds 30 wt%. Terminal products from this processing route are 55-US-gallon tight-head and open-head drums, including UN-marked 1H1/Y and 1H2/Y configurations used for solvent, lubricant, and hazardous-liquid shipment.
Fuel tank systems manufactured from HDPE 9506 in six-layer coextrusion blow molding place the resin in the outer and inner structural layers, while interlayer adhesion is governed by functionalized polyolefin tie resins and EVOH barrier placement. The layer mass distribution commonly falls in the sequence 25–40 wt% virgin HDPE 9506 outer layer, 1–2 wt% tie resin, 1.5–3.0 wt% ethylene-vinyl alcohol copolymer, 1–2 wt% tie resin, 20–40 wt% regrind-HDPE blend, and 15–25 wt% virgin HDPE 9506 inner layer. Compliance requires finished tanks to meet FMVSS 301 fire-resistance and rear-impact integrity, ECE R34 mechanical testing, and evaporative emission limits under applicable EPA and CARB requirements; when EVOH is used, the barrier layer must remain continuous and free from parison pinch-off delamination, which is checked by sectioning molded tanks along the weld seam and inspecting layer thickness under optical microscopy. Process conditions on production lines using multiple extruders feeding a coextrusion head typically maintain HDPE 9506 melt temperature at 210–235 °C while EVOH is kept below 235 °C; exceeding this threshold triggers EVOH gel formation and die lip carbonization. Parison wall thickness is programmed at 2.5–4.0 mm in the body and 5.0–8.0 mm at pinch-off zones to compensate for thinning during blow-up. Air blowing is controlled at 0.5–0.7 MPa, and mold temperature is maintained at 8–20 °C to freeze surface gloss while preventing warpage after fixture cooling. Terminal parts include 45–100 L gasoline and diesel fuel tanks for passenger vehicles and light-duty off-road equipment.
Agricultural chemical packaging requires an HDPE that can withstand prolonged contact with solvent-based emulsifiable concentrates and non-aqueous flowable formulations without panel stress cracking at closure threads and handle pinch-offs. HDPE 9506 is extrusion blow molded into 5–20 L jerrycans on continuous shuttle machines with 100–200 t clamp force, using 100 phr resin, 0.5–1.5 wt% phthalocyanine or carbon black masterbatch, and 0.15–0.30 wt% UV stabilizer that retards photodegradation during outdoor storage. For UN certification, the container must satisfy UN 3H1/Y package tests for drop, leakproofness, hydraulic pressure, and stacking in accordance with the applicable modal regulations such as ADR/RID and 49 CFR 178.603; when aggressive solvents are packaged, surface fluorination or internal barrier treatment is applied to reduce panel permeation, and the treated bottle is tested for barrier continuity before filling. Process conditions include melt temperature 200–220 °C, blow air pressure 0.4–0.6 MPa, and mold temperature 12–25 °C; die swell control is critical at the handle area because HMW-HDPE parison swell can close off the handle flash path and generate pinch-off knits. Terminal products are graduated dosage bottles, closed-head jerrycans, and returnable refill containers for herbicides, fungicides, and crop protection adjuvants.
Extruded sheet from HDPE 9506 is converted into heavy-gauge industrial dunnage and compartment liners where impact energy absorption and resistance to battery acid splash are required. Formulations use 100 phr HDPE 9506 with 0.05–0.15 wt% antioxidant masterbatch and, when color coding is specified, 0.5–1.0 wt% light-stable pigment. Sheet extrusion is run on a single-screw extruder with 30:1 L/D and a flat die adjusted to 2.5–3.5 mm initial gap before entering a three-roll calender stack; roll surface temperature is held at 60–90 °C, and linear draw ratio between die exit and calender nip is maintained below 1.2:1 to prevent molecular orientation that causes anisotropic thermoforming. Thermoforming ovens heat the sheet to 160–180 °C surface temperature before vacuum forming into negative molds at 0.06–0.09 MPa vacuum. Compliance for food-contact packaging, when applicable, relies on FDA 21 CFR 177.1520 and EU No 10/2011 migration limits; for industrial battery trays, the material is commonly evaluated for sulfuric acid resistance by immersion testing under ASTM D543. Terminal products include thermoformed battery nesting trays, truck bed liners, dunnage separators, and material handling covers.
Accumulator blow molding of HDPE 9506 produces seamless vertical and horizontal storage tanks with walls thick enough to meet ASTM D1998-21 hoop stress calculations, while potable water contact compliance is controlled under NSF/ANSI 61 and FDA 21 CFR 177.1520 extraction criteria. Formulation for potable water tanks uses 100 phr HDPE 9506 with 0.1–0.3 wt% heat stabilizer masterbatch and 0.2–0.6 wt% UV stabilizer for outdoor installation; zinc, cadmium, and lead-bearing pigments are excluded. Large-part blow molding machines with 15–30 kg accumulator head capacity plasticate the resin at 210–230 °C and extrude a parison that is programmed for wall thickening near the bottom corners and bung openings; blow air is delivered at 0.5–0.7 MPa, followed by mold cooling at 10–25 °C for 120–300 s depending on wall thickness. Interruption in parison extrusion causes knit lines at the head tooling interface; therefore, continuous parison travel and clean die-lip surfaces are maintained. Terminal products are 50–500 US-gallon vertical and horizontal storage tanks for drinking water, agricultural water, and diluted aqueous chemical solutions.
Where returnable bulk bins replace fiberboard and steel in repetitive intra-plant and closed-loop distribution cycles, HDPE 9506 is blow molded into double-wall lids and bases with molded-in fork pockets and reinforcement ribs. Production uses 100 phr virgin HDPE 9506 plus 10–30 wt% regrind generated from the same article, and 0.3–0.8 wt% UV stabilizer when bins are stored outdoors; the formulation is not blended with low-viscosity HDPE unless a specific HLMI reduction is required for thin-wall sections. Compliance for food-ingredient bins follows FDA 21 CFR 177.1520 and EU No 10/2011, while industrial chemical bins are tested for stack stability under ASTM D642 compression protocols and for puncture resistance under ASTM D3763 high-rate impact. Blow molding machines with 20–30 kg accumulator heads extrude at 210–230 °C, using parison programming that increases wall thickness from 4 mm in side walls to 8–12 mm at fork pockets, and blowing pressure is maintained at 0.5–0.7 MPa. Terminal products include 40–80 cubic-foot bulk bins, nestable totes, and closed-loop distribution trays for granular resin and food ingredient handling.
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