| HS Code | 962046 |
| Polymer Type | High Density Polyethylene (HDPE) |
| Density | 0.955 g/cm³ |
| Melt Index 190 C 2 16 Kg | 8.0 g/10 min |
| Tensile Strength At Yield | 28 MPa |
| Elongation At Break | 600% |
| Flexural Modulus | 1.24 GPa |
| Vicat Softening Point | 124 °C |
| Deflection Temperature At 0 46 Mpa | 74 °C |
| Hardness Shore D | 66 |
| Environmental Stress Crack Resistance | 50 h |
| Low Temperature Brittleness | -70 °C |
As an accredited Chevron Phillips Chemical HDPE HMN 5580 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Chevron Phillips Chemical HDPE HMN 5580 is supplied in 25 kg polyethylene-lined paper bags, palletized, and shrink-wrapped for transport. |
| Container Loading (20′ FCL) | Chevron Phillips HDPE HMN 5580: 20′ FCL usually loads as 25 kg bags, floor-loaded, approximately 17–18 metric tons per container. |
| Shipping | Chevron Phillips Chemical HDPE HMN 5580 ships as non-hazardous high-density polyethylene pellets, typically in 25-kg bags or bulk sacks on pallets. It is not regulated for transport. Keep containers clean, dry, closed, and away from heat, sunlight, moisture, and strong oxidizers. No special shipping labels required. |
| Storage | Store Chevron Phillips Chemical HDPE HMN 5580 in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and incompatible materials. Keep original containers or bags closed to prevent moisture, dust, and contamination. Avoid prolonged high temperatures and UV exposure. Use first-in, first-out stock rotation. Follow supplier SDS and local regulations for safe handling and storage. |
| Shelf Life | Shelf life is approximately 2 years from manufacture when stored in original packaging, cool and dry, away from direct sunlight and contaminants. |
Large-part blow moulding of HMN 5580 into tight-head and open-head industrial containers is executed on accumulator-head machines with extruder diameters between 90 mm and 120 mm, barrier screws of 24:1 to 30:1 L/D, and accumulator capacity of 5 kg to 15 kg. The melt temperature measured at the die is maintained between 185 °C and 205 °C. Below 180 °C, melt pressure rises sufficiently on a 90 mm extruder to create screw-speed instability and parison thickness oscillation; above 210 °C, parison sag contributes to wall-thickness loss exceeding 0.3 mm from die to mold. Parison programming is adjusted for die swell of 10% to 30% and final wall thickness from 1.8 mm to 4.0 mm in UN-rated drum bodies. Blow air pressure is held between 0.6 MPa and 1.2 MPa; mold temperature is controlled between 10 °C and 30 °C. Clamp force for a 200 L drum tool is specified between 1,500 kN and 2,500 kN to avoid parting-line flash. A process boundary occurs when regrind moisture is not controlled below 0.05% by weight because steam pockets visible at the parison surface become weld-line defects in the base pinch-off zone.
Per 100 parts by weight of HMN 5580 resin mixture, clean in-house regrind from trimmed flash and rejected containers replaces 25 to 35 parts of virgin resin. The additive package consists of 2.0 to 2.5 phr carbon black masterbatch, 0.5 to 1.0 phr HALS-based UV stabilizer masterbatch, and 0.05 to 0.15 phr processing aid. Calcium stearate is limited to 0.2 phr maximum to reduce die-lip deposits. Regrind containing fluorinated container scrap or crosslinked barrier-layer particles is excluded because melt-flow mismatch produces parison thickness deviation greater than 0.2 mm at the flash pockets. For hazardous materials service, finished containers are qualified under UN Model Regulations Chapter 6.1 and 49 CFR Part 178 Subpart O, with drop testing per 49 CFR 178.603 at 1.2 m or 1.8 m depending on Packing Group. Food-contact configurations are evaluated under FDA 21 CFR 177.1520(c). Terminal articles include 200 L open-head drums, 100 L to 125 L tight-head jerry cans, 1,000 L IBC inner bottles, and UN-rated agricultural chemical containers.
For heavy-gauge sheet between 4 mm and 12 mm, HMN 5580 is processed on a 90 mm to 120 mm single-screw extruder with a 30:1 L/D barrier screw and melt pump capacity of 100 cm³/rev to 250 cm³/rev. The sheet die lip gap is set at 2.0 mm to 4.0 mm. The three-roll polishing stack is held at 70 °C to 90 °C to prevent warpage. Infrared pyrometers are placed across sheet width to maintain surface temperature variation within ±3 °C; wider variation creates non-uniform sag in twin-sheet forming and corner thinning below 1.5 mm in the final part. Twin-sheet thermoforming is performed with mold temperature between 60 °C and 90 °C and forming air pressure between 0.4 MPa and 0.8 MPa. The process conflict is that sheet surface temperatures above 210 °C generate pinholes at the twin-sheet weld line, while temperatures below 175 °C produce insufficient sheet elasticity and cold folds at draw ratios exceeding 2:1.
In-house edge trim and skeletal regrind is incorporated at 20 wt% to 30 wt% of the resin stream, provided its melt mass-flow rate is within ±0.2 g/10 min of virgin HMN 5580 when tested per ISO 1133-1:2022. Per 100 parts by weight of resin mixture, carbon black masterbatch is added at 2.0 to 2.5 phr, HALS stabilizer masterbatch at 0.5 to 1.0 phr, and processing aid at 0.05 to 0.15 phr. Calcium carbonate filler is limited to 5 phr or less because higher loading reduces weld strength at thermoformed corners and increases density beyond typical HDPE sheet specifications. Food-contact dunnage is evaluated under EU Regulation (EU) No 10/2011 with overall migration limit 10 mg/dm² and FDA 21 CFR 177.1520(c). Industrial automotive dunnage entering the EU is screened against REACH (EC) No 1907/2006 Annex XVII and RoHS Directive 2011/65/EU Annex II. Tensile acceptance is anchored to ASTM D638-14 and ISO 527-2:2012. Terminal products are twin-sheet thermoformed pallet tops, automotive rack dunnage trays, battery handling trays, and heavy-gauge tote liners.
In three-dimensional suction-blow moulding of diesel exhaust fluid reservoirs, HMN 5580 is evaluated primarily for pinch-off weld integrity and long-term exposure to 32.5% aqueous urea solution. Extrusion blow moulding is performed at melt temperatures of 190 °C to 210 °C and mold temperatures of 20 °C to 40 °C. Three-dimensional parison manipulation places the parison into the mold cavity before mold closure, so the weld line is formed along the parting line rather than at the bottom tail. Weld-line failure is the dominant rejection mode because the pinch-off area contains discontinuous flow fronts with reduced environmental stress crack resistance; testing per ASTM D1693-15e1 condition A in 10% Igepal CO-630 at 50 °C is applied to specimens cut across the weld. Published data for HMN 5580 in this exact 3D DEF tank configuration is limited, requiring end-user validation against OEM cycle durability tests.
Per 100 parts by weight of resin mixture, 25 to 30 parts of clean HDPE regrind from HMN 5580 trimmings replace virgin resin. Carbon black masterbatch is added at 2.0 to 2.5 phr for UV resistance, and acid-neutralizer/lubricant masterbatch is incorporated at 0.05 to 0.15 phr. Regrind containing polyamide or EVOH barrier-layer films is excluded because barrier-layer inclusions as small as 50 µm create localized delamination at the weld line and reduce pinch-off impact strength by more than 15%. Post-consumer recyclate is not introduced into automotive fluid reservoirs unless the recyclate stream has been validated for migration resistance under ISO 22241-3:2019 exposure conditions. Compliance for diesel exhaust fluid contact is anchored to ISO 22241-3:2019 for AUS 32 handling and storage compatibility, with additional material restrictions under REACH (EC) No 1907/2006 and end-of-life heavy-metal limits in Directive 2000/53/EC Annex II. Terminal components are diesel exhaust fluid reservoirs, windshield washer solvent reservoirs, and coolant overflow bottles.
After blow moulding and cooling, HMN 5580 agrochemical containers intended for solvent-based crop-protection products are fluorinated in-line with a fluorine/nitrogen mixture of 0.1% to 0.5% fluorine at 25 °C to 60 °C for 0.5 h to 2 h. The treatment produces a fluorinated surface barrier typically 5 µm to 15 µm thick, which reduces weight loss and panel deformation caused by hydrocarbon and ketone solvent permeation. For coextruded barrier containers, HMN 5580 forms the outer structural layer at 60 wt% to 70 wt% of total wall thickness, while a polyamide or EVOH barrier layer constitutes 3 wt% to 6 wt% and a tie layer constitutes 1 wt% to 2 wt%. The downstream process is continuous coextrusion blow moulding with six or seven layer heads; layer distribution is verified by infrared microscopy on microtomed wall sections. Regrind from barrier structures is restricted to 10 wt% to 20 wt% because barrier-layer particles above 30 µm reduce impact strength and create visible streaks on the inner surface.
Formulation per 100 parts by weight of resin mixture: for monolayer fluorinated containers, carbon black masterbatch at 2.0 to 2.5 phr, HALS UV stabilizer masterbatch at 0.5 to 1.0 phr, and acid scavenger at 0.05 to 0.15 phr. For coextruded structures, the barrier and tie layers are fed by separate extruders at the stated layer ratios. Chlorinated paraffin additives are excluded because they interfere with fluorine uptake and reduce barrier uniformity. Compliance is based on UN Model Regulations Chapter 6.1, 49 CFR Part 178 Subpart O, and the FAO/WHO Guidelines for the Packaging of Pesticides. Terminal products are 1 L to 25 L agrochemical bottles, solvent-based herbicide containers, and UN-rated jerry cans for crop-protection formulations.
Fabricated secondary containment liners made from HMN 5580 sheet are butt-fusion welded with a heating plate temperature of 200 °C to 220 °C and joining pressure of 0.15 MPa, followed by cooling under pressure for 6 min to 10 min depending on sheet thickness. Weld bead geometry is checked against DVS 2207-1; acceptable beads are double-roll beads with uniform width and a root gap not exceeding 0.5 mm. The process is sensitive to plate contamination and residual moisture; sheet edges must be dry and free of oxidized saw-cut debris. Addition ratio per 100 parts by weight of resin mixture is 25 to 30 parts clean regrind, carbon black masterbatch at 2.0 to 2.5 phr, and HALS UV stabilizer at 0.5 to 1.0 phr. Halogenated flame-retardant masterbatches are excluded from sheet intended for chemical containment because they lower weld strength and can leach acidic decomposition species under contact with strong oxidizers. Compliance for hazardous waste containment is anchored to EPA 40 CFR 264.175; material evaluation follows ASTM D638-14 tensile testing and ISO 527-2:2012. Terminal products are secondary containment liners, spill pallet decks, and fabricated tank saddles for chemical storage areas.
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