| HS Code | 138837 |
| Density | 0.958 g/cm³ |
| Melt Index 190 C 2 16 Kg | 0.35 g/10 min |
| Tensile Strength At Yield | 29 MPa |
| Tensile Strength At Break | 30 MPa |
| Elongation At Break | 600% |
| Flexural Modulus | 1380 MPa |
| Notched Izod Impact | 53 J/m |
| Environmental Stress Crack Resistance Escr | >1000 h |
| Vicat Softening Point | 128°C |
| Melting Point | 134°C |
| Crystallization Temperature | 116°C |
| Brittleness Temperature | <-70°C |
| Shore D Hardness | 66 |
| Thermal Conductivity | 0.49 W/m·K |
| Coefficient Of Linear Thermal Expansion | 1.2E-4 /°C |
| Heat Deflection Temperature At 0 45 Mpa | 75°C |
| Water Absorption | <0.01% |
| Dielectric Constant | 2.3 |
| Volume Resistivity | >1E15 ohm·cm |
| Dielectric Strength | 18 kV/mm |
As an accredited Chevron Phillips Chemical HDPE C579 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Chevron Phillips Chemical HDPE C579 is supplied in 25 kg (55 lb) bags, typically palletized for industrial shipping. |
| Container Loading (20′ FCL) | Chevron Phillips Chemical HDPE C579 pellets loaded in 20′ FCL: 25 kg bags, palletized, shrink-wrapped, secured, dry container, maximum payload. |
| Shipping | Chevron Phillips Chemical HDPE C579 is shipped as non-hazardous high-density polyethylene pellets in 25 kg bags, octabins, bulk trucks, or railcars. It is not regulated for transport; no UN number, hazard class, packing group, or labels required. Keep dry, cool, and avoid contamination. |
| Storage | Store Chevron Phillips Chemical HDPE C579 in a cool, dry, well-ventilated area, away from direct sunlight, heat, flames, and strong oxidizers. Keep containers tightly sealed to prevent moisture, dust, and contamination. Protect from physical damage and prolonged UV exposure. Maintain ambient temperature, use first-in, first-out rotation, and follow SDS and local regulations. Do not stack excessively or expose to incompatible substances. |
| Shelf Life | Shelf life: indefinite when stored in sealed containers in a cool, dry, well-ventilated area, away from sunlight, heat, and contaminants. |
C579-based compounds intended for United Nations dangerous goods packaging are processed on accumulator-head extrusion blow molders with screw length-to-diameter ratios between 24:1 and 30:1. The screw is specified with a barrier profile and spiral Maddock mixing to limit low-molecular-weight fraction overcooking at the root. Die head temperatures are held at 200°C to 220°C, adapter temperatures at 195°C to 215°C, and mold cooling water at 10°C to 25°C. Blow pressure is set at 0.65 MPa to 0.85 MPa, with parison programming maintained across 64 to 128 points for non-axisymmetric drum geometries. Blow-up ratios between 2.2:1 and 3.0:1 require the top chime area to be programmed 15% to 25% thicker than the sidewall center, because the upper pinch area undergoes more local draw than the cylindrical body. The bottom pinch-off zone is formed when the mold halves close on the melt tube, producing a weld with orientation-induced free volume and a micro-void concentration that becomes the primary stress-cracking site. Plants that run C579 for drums therefore extract tensile specimens directly from the pinch-off seam and compare yield retention to sidewall stock under ASTM D638. If the measured drop exceeds 20%, the regrind fraction, clamp speed, or die temperature is adjusted before continuing production.
Addition ratio control for an opaque, outdoor-rated C579 drum formulation uses carbon black masterbatch at 2.0 wt% to 3.0 wt%, hindered amine light stabilizer masterbatch at 0.1 wt% to 0.3 wt%, and fluoropolymer process aid at 0.02 wt% to 0.08 wt%. Clean internal regrind is gravimetrically metered at 20 wt% to 30 wt%. Once regrind exceeds 30 wt%, low-molecular-weight tails generated during previous heat histories concentrate in the pinch-off region and reduce environmental stress crack resistance under ASTM D1693 condition B. Moisture in regrind flake is controlled below 0.10 wt% by drying at 80°C to 90°C for 2 h when storage conditions or washing lines introduce free water. Industry compliance is verified against UN Model Regulations Chapter 6.1, 49 CFR Part 178.500 series, and ADR 6.1. Food-contact drum linings require FDA 21 CFR 177.1520 and Regulation (EU) No 10/2011, with overall migration below 10 mg/dm². Terminal product types include 20 L and 30 L jerricans, 60 L, 120 L, and 220 L open-head and tight-head drums, and 1,000 L composite IBC inner bottles. Published lot-specific data for C579 in UN drop testing should be generated on final production tooling, because the pinch-off geometry, wall thickness distribution, and mold venting affect the result more than the resin lot alone.
On a high-clamp-force shuttle blow molder running C579-based automotive reservoir tooling with 350 kN to 600 kN clamp force, the parison wall is programmed to compensate for vertical draw ratios from 3:1 to 4:1. Barrel temperatures are profiled from 190°C to 230°C, the die head is held at 200°C to 225°C, mold cooling water is kept at 15°C to 30°C, and blow pressure is set between 0.60 MPa and 0.80 MPa. The primary failure mode in underhood service is not brittle low-speed fracture but slow crack growth from the weld line after long-term hot coolant exposure. For this reason, C579 acceptance for automotive reservoirs is anchored to ISO 16750-5 fluid compatibility, ASTM D638 tensile yield retention after immersion in 50/50 ethylene glycol-water at 90°C for 500 h, and ASTM D1693 condition B ESCR on specimens cut from the parison weld and hot-plate weld zones. Any lot showing ESCR failure below 100 h in the weld zone is rejected for underhood use.
Addition ratios for automotive-grade C579 compounds use long-term heat stabilizer masterbatch at 0.10 wt% to 0.30 wt%, carbon black masterbatch at 2.0 wt% to 2.5 wt%, and processing aid at 0.03 wt% to 0.06 wt%. Regrind is deliberately limited to 15 wt% to 20 wt% because vibration-welded and infrared-welded fitting joints create notch-sensitive planes where low-molecular-weight regrind fractions reduce burst pressure. Terminal product types include windshield washer reservoirs, coolant recovery bottles, hydraulic fluid reservoirs, air intake duct sections, and diesel exhaust fluid reservoirs. Between -30°C and 80°C, the C579 wall must retain sufficient rigidity at the mounting boss without rubber impact modifiers that would depress flexural modulus. Amine-based antistatic packages are not introduced into underhood C579 formulations, because they can accelerate oxidative chain scission at the inner coolant-exposed surface and reduce long-term weld strength.
| Conversion segment | Regulatory or customer specification | Test standard or clause |
|---|---|---|
| UN-approved industrial drum and jerrican | UN Model Regulations Chapter 6.1; 49 CFR 178.500 series; ADR 6.1 | UN drop, hydraulic pressure, leakproofness |
| Food-contact sheet and thermoformed packaging | FDA 21 CFR 177.1520; (EU) No 10/2011 | Overall migration <10 mg/dm² |
| Automotive fluid reservoir | ISO 16750-5; OEM material specification | ASTM D638 after 500 h coolant immersion; ASTM D1693 condition B |
| Agrochemical barrier bottle | EPA FIFRA 40 CFR Part 156; EC 1907/2006 REACH | Container permeation; UN 6.1 drop |
| Returnable twin-sheet thermoformed pallet | ISO 8611-1:2011 | Bending, corner drop, creep |
Heavy-gauge sheet from C579 is run on a single-screw extruder with a 30:1 L/D barrier screw, a 60/80/100 mesh screen pack, a melt pump, and a flexible-lip die. Melt temperature is maintained at 210°C to 230°C. For sheet thickness between 3 mm and 12 mm, the die lip gap is set at 0.8 mm to 1.5 mm, and the melt pump is adjusted to hold a constant die inlet pressure of 12 MPa to 18 MPa. The primary process conflict is roll-stack temperature. When roll surfaces fall below 70°C, the sheet exits with a through-thickness temperature gradient exceeding 20°C/mm, generating differential skin-core solidification. The frozen-in stress manifests as edge curl after reheat and non-uniform wall distribution during downstream plug-assisted thermoforming. Roll-stack temperatures are therefore set independently at 70°C to 95°C, with gap pressure between 40 N/mm and 80 N/mm, and the roll gap is held at 0.4 to 0.6 times sheet gauge. The polished roll surface finish must correspond to the final product class; pit-type surface defects on the roll are transferred to the sheet and become crack initiators in heavy-gauge parts under cyclic load.
Addition ratios for C579 sheet depend on service exposure. Post-industrial regrind is metered at 30 wt% to 50 wt% for non-food material-handling sheet, antioxidant masterbatch at 0.10 wt% to 0.25 wt%, and UV stabilizer masterbatch at 1.0 wt% to 2.0 wt% for outdoor stock. If antistatic behavior is specified for battery handling trays or dust-sensitive logistics, an antistatic masterbatch is added at 1.0 wt% to 2.0 wt%. Food-contact sheet requires the stabilizer package to comply with FDA 21 CFR 177.1520 and (EU) No 10/2011, and a change of antioxidant masterbatch supplier requires re-verification of overall migration. Terminal product types include thermoformed pallets, dunnage trays, returnable container liners, cold-chain separators, and battery handling trays. When thick C579 sheet is thermoformed, the preheat stage uses surface-temperature control at 150°C to 170°C, plug-assist force limited to avoid edge thinning below 60% of initial gauge, and mold temperatures from 50°C to 80°C. Published data for C579 in each specific sheet gauge and thermoforming configuration is limited; line qualification should include at least 50 continuous cycles to separate resin lot variance from tooling drift.
For a six-layer coextrusion blow molder with gravimetric layer control, C579 is allocated to the structural layers at 70 wt% to 80 wt% of container mass, with an ethylene vinyl alcohol barrier layer at 1 wt% to 3 wt%, maleated tie resin at 1 wt% to 2 wt%, and reprocessed trim at 15 wt% to 20 wt%. The C579 structural layers are processed at 205°C to 220°C, the barrier layer at 195°C to 210°C, and the mold at 10°C to 20°C. Parison drop time is minimized to reduce viscosity mismatch between the C579 melt and the barrier resin, because layer breakout in the shoulder and pinch-off regions leads to drop-impact failure. In monolayer agrochemical bottles based on C579, addition ratios use carbon black masterbatch at 2.5 wt% to 3.0 wt%, antioxidant at 0.10 wt% to 0.20 wt%, and neutralizer at 0.05 wt% to 0.10 wt%. Amine-based antistatic systems are excluded from the structural layer because they can interact with acidic catalyst residue and accelerate stress cracking after aggressive ester or amine-containing formulations are filled.
Regulatory compliance for this segment includes UN Model Regulations Chapter 6.1, 49 CFR Part 178.500 series for packaging, EPA FIFRA 40 CFR Part 156 for crop protection chemical containers, and EC 1907/2006 for REACH. Terminal product types include 1 L, 5 L, and 20 L crop protection chemical bottles, industrial oxygenated solvent containers, and chlorine-resistant concentrate jugs. Post-mold fluorination may be applied to monolayer C579 containers to reduce solvent permeation, but fluorinated regrind is not subsequently reintroduced into food-contact structural layers because the surface fluorine modification alters adhesion and migration behavior. The operational boundary is set by drop testing at -18°C after barrier-layer peel inspection; if the barrier layer delaminates from the C579 substrate at the pinch zone, the die head temperature differential is reduced by 5°C increments until peel adhesion is restored.
C579-based twin-sheet thermoforming is conducted on cut-sheet or roll-fed lines using upper and lower sheets of 3 mm to 6 mm thickness. Sheet surface temperature at forming is controlled between 150°C and 170°C; infrared pyrometers are placed across the sheet width, and surface temperature variation is held within ±5°C before mold entry. Plug-assisted vacuum uses negative pressure of −0.06 MPa to −0.08 MPa, while mold temperature is maintained at 50°C to 80°C. Twin-sheet weld pressure at rib intersections is applied at 0.3 MPa to 0.6 MPa for 45 s to 90 s, depending on rib height and sheet thickness. Below 150°C the weld produces cold seams with partial fusion; above 170°C the heated sheet sags excessively, closing the vent channels between formed cavities and producing non-uniform plug contact. The narrow surface-temperature band is the critical processing window for C579 in this conversion route.
Addition ratios for returnable logistics parts use carbon black masterbatch at 1.5 wt% to 2.5 wt%, UV stabilizer masterbatch at 0.8 wt% to 1.2 wt%, and regrind at 20 wt% to 40 wt%. When long-term static load creep is part of the customer specification, regrind is capped at 25 wt% because multiple heat histories broaden the molecular weight distribution and increase creep at the welded rib base under continuous load. Compliance for palletized logistics is verified against ISO 8611-1:2011 for bending and corner drop, ASTM D256 notched Izod at −20°C, and ASTM D4329 for accelerated weathering where outdoor storage is specified. Terminal product types include stackable returnable pallets, dunnage racks, collapsible distribution trays, and cold-chain separators. Because twin-sheet weld strength is highly tool-dependent, published data for C579 in this specific configuration is limited; production validation should include corner-drop and pallet-bending tests on parts welded with the actual mold insert geometry, not flat plaques.
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Chevron Phillips Chemical HDPE C579 is a high-density polyethylene injection-molding grade supplied in pellet form. The resin is specified for rigid packaging, thin-wall containers, crates, closures, and consumer housewares in which a nominal density of 0.956 g/cm³ under ASTM D1505 and a melt index of 7.5 g/10 min under ASTM D1238 at 190°C with a 2.16 kg piston load provide a narrow balance between melt fluidity and environmental stress crack resistance. Public technical literature from the producer positions C579 within the Marlex high-density polyethylene portfolio as a general-purpose injection-molding grade. The melt flow rate allows filling of multi-cavity cold-runner tools at lower injection pressure than fractional-melt-index HDPE resins while retaining stiffness and chemical resistance typical of HDPE. Comonomer type and molecular weight distribution are not fully disclosed in the producer's public documentation; however, the density, mechanical profile, and flow behavior indicate a short-chain branching distribution consistent with high-flow HDPE copolymers intended for rapid cycling and low warpage in molded articles.
Processors running C579 in single-screw injection molding cells commonly begin with barrel zone settings from 190°C to 230°C and nozzle settings from 200°C to 240°C. Exact set points are adjusted to screw diameter, shot size, and residence time; large-capacity barrels with shot weights below 30% of barrel capacity can overheat the melt and should be avoided. Mold surface temperatures in the range of 10°C to 40°C are used for unfilled HDPE, with lower settings favoring faster cycle times and higher settings improving weld-line strength in parts with long flow paths. Pre-drying is not normally required unless condensation is present; if surface moisture is observed, a dehumidified-air hopper dryer at 70°C for 1 h to 2 h may be applied. Melt temperatures above 260°C should be avoided because thermo-oxidative chain scission can reduce molecular weight and produce splay, taste, and odor changes in food-contact parts. Regrind levels should be limited to 20% to maintain consistent injection pressure and minimize lot-to-lot variability in melt flow.
Short-shot formation in thin-wall sections below 1.0 mm is governed less by material melt index than by gate freeze time and cavity pressure decay. Multi-cavity tools for caps and overcaps running C579 have been reported to require injection pressures of 60 MPa to 100 MPa at the nozzle, with holding pressures between 40 MPa and 70 MPa, depending on gate diameter and cavity fill ratio. Equipment limitations become relevant at clamp force values below 1,200 kN; when mold breathing occurs at the parting line, the pressure drop across the flow front can create internal voids, burn marks, and inconsistent fill. Screw geometries with 20:1 to 24:1 L/D and a compression ratio from 2.2:1 to 3.0:1 are generally suitable for this melt-index range, although high-compression screws above 3.5:1 can generate excessive shear heating and should be validated with melt-temperature measurements. Published data for spiral flow lengths specific to C579 are limited; general HDPE injection grades in this density and melt-index class typically exhibit flow length-to-wall-thickness ratios above 150:1 at 80 MPa injection pressure, but cavity geometry, runner diameter, and injection speed modify this value in production.
Capillary rheometry under ASTM D3835 indicates shear-thinning behavior typical of linear HDPE; apparent viscosity decreases by approximately 60% when shear rate increases from 100 s⁻¹ to 1,000 s⁻¹ at 220°C, but published data specific to C579 should be generated for simulation. Mold-filling simulation packages require pressure-volume-temperature and viscosity data from ISO 11443 or equivalent capillary measurements; generic HDPE parameters may under-predict fill pressure in thin sections.
| Property | Typical Value | Test Method |
|---|---|---|
| Density | 0.956 g/cm³ | ASTM D1505 |
| Melt Index | 7.5 g/10 min | ASTM D1238 (190°C/2.16 kg) |
| Tensile Strength at Yield | 26 MPa | ASTM D638 Type IV |
| Flexural Modulus | 1,240 MPa | ASTM D790 |
| Notched Izod Impact | 53 J/m | ASTM D256 |
| Shore D Hardness | 64 | ASTM D2240 |
| Vicat Softening Temperature | 126°C | ASTM D1525 |
These values are typical producer-published data points and are not specification limits; certificate-of-analysis values will differ by lot. Mold shrinkage for this density and melt-index range is approximately 0.020 mm/mm to 0.025 mm/mm in the flow direction and 0.018 mm/mm to 0.024 mm/mm in the transverse direction when molded under recommended conditions. Tool designers should treat these ranges as preliminary estimates and confirm them with cavity-pressure studies because shrinkage varies with wall thickness, packing pressure, and gate seal time.
For food-contact applications, C579 must be evaluated against the applicable regulatory use conditions. The base olefin polymer is generally covered by 21 CFR 177.1520(c) 3.1a for high-density polyethylene when the finished article meets extraction and migratory limits applicable to the intended food types and temperature conditions. End users processing C579 for single-use dairy containers, caps, or housewares should conduct compliance testing under FDA migration guidance and, where applicable, European Union Regulation 10/2011 or regional food-contact legislation. Additive masterbatch selection is critical: fatty-food applications may require organoleptic panels because high-temperature processing with inadequate stabilizers can generate oxidation products that affect taste and odor. The resin should not be combined with amine-based additives or processing aids that are not approved for the intended food-contact use without confirming regulatory compatibility.
C579, as a general-purpose injection-molding HDPE, is not optimized for continuous outdoor exposure. Ultraviolet stabilizer packages are not part of the standard product formulation; UV resistance must be supplied through formulated concentrates if the molded article is to be used outdoors beyond short-term service. Carbon black masterbatch at 2.0% to 2.5% loading provides UV screening, but weathering performance should be validated with ASTM G154 or ISO 4892-2 accelerated exposure and correlated to field data. The resin also has lower environmental stress crack resistance than high-molecular-weight HDPE grades; exposure to strong oxidizing acids, chlorinated solvents, or aggressive surfactants at elevated temperature can initiate slow crack growth, especially in areas with molded-in stress. For continuous contact with household bleach or hydrocarbon-based cleaning agents, stress-crack testing under ASTM D1693 should be performed on the finished part, and a higher-molecular-weight HDPE grade should be evaluated if crack initiation is observed before the product's required service life.
In comparison with fractional-melt-index HDPE grades used for film or pipe, C579 sacrifices some long-chain molecular weight, which lowers melt viscosity and allows higher screw recovery rates and shorter cycle times in injection molding. In field terms, a multi-cavity tool running C579 can fill at lower injection pressure than a 0.30 g/10 min HDPE grade, but the trade-off is lower notched Izod impact and shorter stress-crack life. Compared with high-molecular-weight blow-molding HDPE grades with density close to 0.950 g/cm³, C579 offers higher stiffness and hardness but less resistance to slow crack growth. It also differs from lower-density ethylene copolymers by remaining stiffer at ambient temperature; however, this stiffness comes with a higher brittle transition temperature and reduced low-temperature impact performance. The grade should not be substituted for high-molecular-weight grades in large blow-molded industrial containers or pressure pipe without completing a full design review and slow-crack-growth testing based on ISO 9080 or equivalent hydrostatic testing.
Dairy closures, overcaps, thin-wall food containers, and reusable crates are production-scale applications in which the melt index of C579 contributes to filling small gates and high cavitation. In closure manufacturing, injection-compression or thin-wall injection tools with 32 to 96 cavities are common; the mold hot runner and gate design must be balanced to maintain cavity-to-cavity fill variation below 1.5% by shot weight. Drop impact performance is evaluated according to ASTM D2463 or customer-specific closure drop protocols at 0°C to 5°C; parts should be tested after conditioning at service temperature because HDPE impact decreases with cooling. Crates and totes require design for stiffening ribs and boss anchorage because the flexural modulus of C579 supports load-bearing walls but not unsupported large flat panels. Process installations should include granulators with noise enclosures because HDPE regrind increases dust and static charge when pellet-to-regrind ratios exceed 20%.
Pelletized HDPE C579 is typically processed without pre-drying, but bulk handling systems should protect against condensation cycles that can introduce surface moisture into cold pellets when silos are located outdoors. Regrind incorporation above 20% tends to reduce particle-size uniformity, alter bulk density, and increase static charge in vacuum conveying lines; feed throat bridging has been observed when fluff-to-pellet ratios exceed 25% and the screw is operated below 60% of maximum rotation. Magnetic separators and screen packs with 0.5 mm to 1.0 mm openings are recommended in material handling systems because post-consumer contamination or tramp metal can damage check rings and hot-runner tips. The material should be stored in a clean, dry area and protected from prolonged exposure to direct sunlight and outdoor temperature swings, which can accelerate additive migration and change surface oxidation characteristics.
One area not covered by standard HDPE data sheets is the interaction between flow-induced orientation, shrinkage anisotropy, and impact toughness in weld-line zones. In complex multi-gated parts, knit lines formed during the filling of C579 can reduce notched impact strength locally by 20% to 40% relative to bulk material because the weld-line core contains limited chain entanglement across the frozen front. This is not unique to C579 but must be addressed through gate location, sequential valve gating, or weld-line-specific testing. Published data for this specific configuration is limited, and processors should generate internal design-of-experiment data using ASTM D638 tensile bars and ASTM D256 impact specimens cut from molded parts. The operational boundary for this grade is defined by the combination of melt temperature, shear rate, and oxidative stabilization; processes that exceed 260°C for prolonged hold times or that introduce excessive regrind can shift the molecular weight distribution outside the intended processing envelope.