| HS Code | 587550 |
| Product Name | Chevron Phillips Chemical HDPE 99416 |
| Polymer Type | High Density Polyethylene |
| Comonomer | Hexene-1 |
| Density | 0.946 g/cm3 |
| Melt Index | 0.15 g/10 min |
| Tensile Yield Strength | 26 MPa |
| Tensile Break Strength | 30 MPa |
| Elongation At Break | 600% |
| Flexural Modulus | 1100 MPa |
| Environmental Stress Crack Resistance | >1000 hr |
| Vicat Softening Temperature | 125 °C |
| Brittleness Temperature | < -70 °C |
| Hardness Shore D | 65 |
| Coefficient Of Linear Thermal Expansion | 1.2E-4 cm/cm/°C |
| Thermal Conductivity | 0.45 W/m·K |
| Melting Point | 130 °C |
| Water Absorption | <0.01% |
| Dielectric Constant | 2.3 |
| Dielectric Strength | 20 kV/mm |
| Volume Resistivity | >1E15 ohm-cm |
| Crystallinity | 70% |
| Molecular Weight Distribution | Broad |
As an accredited Chevron Phillips Chemical HDPE 99416 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Typically, Chevron Phillips Chemical HDPE 99416 is packaged in 50 lb polyethylene bags, 1,000 lb bulk bags, or bulk railcars. |
| Container Loading (20′ FCL) | 20′ FCL loaded with Chevron Phillips Chemical HDPE 99416 in 25 kg bags, palletized, shrink-wrapped, and secured for ocean transport. |
| Shipping | Chevron Phillips Chemical HDPE 99416 ships as non-hazardous, solid polyethylene pellets. Typical packaging includes 25 kg bags, bulk bags, boxes, or bulk trucks/railcars. It is not DOT/IMDG/IATA regulated. Store in a dry, ventilated area away from heat, ignition sources, and oxidizing agents; protect packages from contamination and moisture. |
| Storage | Store Chevron Phillips Chemical HDPE 99416 in a cool, dry, well-ventilated area, away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep containers or bags tightly closed, off the floor, and protected from moisture, dust, and contamination. Avoid excessive stacking. Use first-in, first-out rotation. Follow the manufacturer’s SDS, local regulations, and hygiene practices. Do not store near food or water. |
| Shelf Life | For HDPE 99416, shelf life is indefinite under normal storage; keep cool, dry, away from direct sunlight and contaminants. |
Chevron Phillips Chemical HDPE 99416 is a high-flow high-density polyethylene injection molding resin with a melt flow rate of 16 g/10 min under ISO 1133-1:2022 at 190 °C/2.16 kg and a density of 0.953 g/cm³ under ASTM D1505. The material is supplied as pelleted virgin resin and is processed on conventional injection molding lines. The following application scenarios represent industrial use areas where the grade is technically applicable, with compliance limits, formulation loadings, production equipment settings, and finished article categories described separately for each downstream segment. All addition ratios are expressed on a 100 parts resin basis unless otherwise noted.
In thin-wall injection molding of dairy cups, deli containers, and lids, HDPE 99416 is processed at melt temperatures between 190 °C and 220 °C, with mold temperatures maintained at 15 °C to 40 °C. The melt flow rate of 16 g/10 min permits flow length-to-wall thickness ratios above 200:1 in cavities with wall stock from 0.4 mm to 0.9 mm, although gate land thickness should be held at 50 % to 70 % of nominal wall to ensure shear-induced flow without premature gate freeze. Production-scale all-electric injection molding machines with clamp force from 80 tonnes to 180 tonnes and general-purpose screws of 20:1 to 24:1 L/D ratio are used; screw back pressure is maintained at 0.5 MPa to 1.5 MPa, and injection velocity is set at 80 mm/s to 150 mm/s to avoid surface flow marks while limiting shear heating. Compliance for dairy and deli applications relies on FDA 21 CFR 177.1520(c) 3.2a and EU Regulation (EU) No 10/2011 with overall migration limit 10 mg/dm²; finished articles also require GB 4806.7-2016 where applicable.
The main process conflict in thin-wall tooling is that the injection velocity required to fill a 0.4 mm wall before freeze-off may exceed 120 mm/s; above 150 mm/s shear heating at the gate can raise local melt temperature above 240 °C, producing gate blush, streak formation, and reduced lidding seal strength. Formulation addition is typically 100 parts resin with 2.0 wt% to 4.0 wt% white or color concentrate, 0.05 wt% to 0.12 wt% slip/antiblock additive, and 0.03 wt% to 0.08 wt% antioxidant-acid neutralizer package; silicone mold release should not exceed 0.5 wt% because excessive migration can lower heat seal performance on lidding. Terminal product forms include 4 oz to 32 oz round and rectangular dairy cups, hinged deli containers, snap-on lids, and insertable vented lids for microwave reheating.
| Regulation / standard | Scope | Test method / clause | Typical limit or condition |
|---|---|---|---|
| FDA 21 CFR 177.1520(c) 3.2a | Olefin polymers for food contact | End-test extraction, food-type simulation | No migration above prescribed extractives limits |
| EU Regulation (EU) No 10/2011 | Plastic food-contact materials | OML, Annex II | 10 mg/dm² or 60 mg/kg |
| GB 4806.7-2016 | Food-contact plastic resins and articles | Total migration | 10 mg/dm² |
| REACH Annex XVII | Restricted substances | Entry 51 phthalates, entry 50 PAHs | No intentional addition |
Beverage closure molding with HDPE 99416 shifts the processing constraint from melt flow to gate freeze time and dimensional stability after demolding. For tamper-evident screw caps and dispensing closures, the formulation is 100 parts resin with 1.5 wt% to 3.0 wt% color concentrate, 0.05 wt% to 0.15 wt% erucamide slip agent, 0.02 wt% to 0.10 wt% hindered phenolic antioxidant, and optional 0.2 wt% to 0.5 wt% fluoropolymer processing aid when high-speed cavity filling produces melt fracture at the gate. Excessive erucamide above 0.15 wt% can plate out on mold vent surfaces and reduce cap flavor performance on long production runs. Relevant compliance is FDA 21 CFR 177.1520(c) 3.2a for aqueous and low-alcohol beverage contact, EU Regulation (EU) No 10/2011 overall migration, and EU Regulation (EC) No 2023/2006 on good manufacturing practice for food-contact materials. Closure production lines typically use 24-cavity to 96-cavity high-speed injection molds with hot runner systems, melt temperatures of 200 °C to 240 °C, mold temperatures of 10 °C to 30 °C, and cycle times of 3.5 s to 6.5 s. Core pin design and ejection sleeve clearance are controlled within 0.02 mm to 0.05 mm per side to prevent cap ovality exceeding 0.3 mm on diameter. Terminal closure types include 28 mm and 38 mm tamper-evident beverage caps, push-pull sports closures, and snap hinge dispensing caps for personal care and condiment bottles.
Cosmetic packaging jars, thick-walled caps, and closure skirts molded from HDPE 99416 generate higher core pin ejection force when mold surface roughness falls below 0.1 µm Ra because the material's shrinkage of 1.5 % to 2.5 % increases contact pressure on polished cores. For jars with wall thickness from 1.0 mm to 2.5 mm, processing uses melt temperatures of 200 °C to 230 °C, mold temperatures of 15 °C to 30 °C, injection velocities of 60 mm/s to 120 mm/s, and hold pressures from 40 MPa to 70 MPa. Formulation addition is 100 parts HDPE 99416 with 2.0 wt% to 4.0 wt% white or tinted masterbatch, 0.05 wt% to 0.15 wt% antioxidant package, 0.05 wt% to 0.10 wt% UV absorber for package light protection, and 0.1 wt% to 0.3 wt% antistatic additive where powder makeup formulas create dust adhesion on external surfaces. Compliance for cosmetic packaging rests on EU Regulation (EC) No 1223/2009 for the final cosmetic product and REACH Annex XVII restrictions; packaging that may contact food requires EU Regulation (EU) No 10/2011, while RoHS 2011/65/EU applies only if the article contains electrical components. Terminal products include 50 ml to 500 ml double-wall jars, serum bottle closures, twist-up stick bases, and thick-walled overcaps for glass bottles.
For housewares and storage articles molded from HDPE 99416, hot runner imbalance becomes a visible defect source when multi-cavity tools exceed 8 cavities because the high melt flow rate reduces pressure drop and amplifies small gate-diameter differences. Processing on 200-tonne to 800-tonne hydraulic or hybrid injection molding machines uses melt temperatures of 190 °C to 230 °C, mold temperatures of 20 °C to 50 °C, injection velocities of 40 mm/s to 80 mm/s, and cycle times of 10 s to 20 s depending on part mass. The formulation ratio is 100 parts resin with 1.0 wt% to 2.0 wt% color concentrate, 0.05 wt% to 0.20 wt% UV stabilizer for outdoor storage products, 0.1 wt% to 0.3 wt% antistatic additive, and 0.03 wt% to 0.08 wt% antioxidant. Compliance for food-contact housewares is FDA 21 CFR 177.1520(c) 3.2a and EU Regulation (EU) No 10/2011; non-food products are evaluated under REACH Annex XVII and relevant sections of the California Proposition 65 list. Terminal product types include stackable storage boxes, waste bins, drawer organizers, clothes hangers, and utility baskets with wall thickness from 1.2 mm to 3.0 mm.
Because toy and recreational component lines operate under EN 71-3 and ASTM F963-23 migration limits, HDPE 99416 is processed without external lubricants that can raise heavy-metal extractables or create a surface bloom on dark pigments. The formulation is 100 parts resin with 1.0 wt% to 3.0 wt% colorant masterbatch, 0.05 wt% to 0.15 wt% hindered phenolic antioxidant, and 0.1 wt% to 0.2 wt% antistatic additive; no phthalate plasticizers or heavy-metal pigments are added. Molding equipment for toy components uses melt temperatures of 190 °C to 225 °C, mold temperatures of 20 °C to 45 °C, injection velocities of 50 mm/s to 100 mm/s, and cycle times of 8 s to 15 s depending on wall thickness. Compliance includes EN 71-3 for migration of certain elements, ASTM F963-23 soluble heavy-metal requirements, REACH Annex XVII entries for cadmium and phthalates, and European Food Contact Regulation (EU) No 10/2011 when the toy may be placed in the mouth. Terminal product types include building blocks, board game components, outdoor play set parts, and toy vehicle wheels.
Industrial pails and open-head containers molded from HDPE 99416 with post-industrial regrind require a narrower processing window when regrind content exceeds 10 wt%. At 20 wt% recyclate, melt viscosity shifts upward enough to require an increase in melt temperature of 10 °C to 15 °C or a reduction in injection velocity of 10 mm/s to 20 mm/s to maintain consistent filling of wall sections from 1.8 mm to 3.0 mm. The formulation ratio is 100 parts total resin, comprising 80 parts virgin HDPE 99416 and 20 parts clean post-industrial regrind from the same product family, with 0.5 wt% to 2.0 wt% colorant, 0.1 wt% to 0.3 wt% UV stabilizer, and 0.03 wt% to 0.08 wt% antioxidant. Process equipment includes 500-tonne or larger injection molding machines with accumulator-assisted injection, melt temperatures of 200 °C to 230 °C, mold temperatures of 30 °C to 50 °C, hold pressures of 50 MPa to 80 MPa, and cycle times from 15 s to 30 s. Compliance for hazardous goods pails is governed by UN 1H2 certification under ADR/RID/ADN or IMDG Code when tested at drop heights, and the resin formulation must not contain recycled material from non-food unknown sources if the pail is used for food, under EU Regulation (EU) No 10/2011 and FDA 21 CFR 177.1520(c). Terminal product types include 5-gallon and 7-gallon open-head pails, tamper-evident lids, and stackable containers for paints, lubricants, adhesives, and construction chemicals.
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Chevron Phillips Chemical HDPE 99416 is an injection-molding high-density polyethylene supplied in pellet form. Under ASTM D1238 at 190 °C and 2.16 kg, the nominal melt mass-flow rate is 40 g/10 min. Under ASTM D1505, the solid density is typically 0.953 g/cm³. These two values place the resin in the high-flow HDPE class, where cavity fill is governed less by plastication and more by gate freeze time and mold cooling. The product is specified for thin-wall injection molding of overcaps, rigid food containers, housewares, toys, and small appliance parts in multi-cavity tools.
In production-scale injection molding with screws of 20:1 to 24:1 L/D, a melt-temperature set point of 210 °C to 230 °C is a normal starting condition. At melt temperatures below 190 °C, cavity short shots can occur when wall thickness drops below 0.8 mm. Above 240 °C, thermal-oxidative degradation becomes design-limiting, especially in hot-runner systems with stagnant flow regions. Back pressure between 0.3 MPa and 0.7 MPa and screw surface speeds of 0.2 m/s to 0.4 m/s are often used to homogenize the melt without excessive shear heating. Published data for this specific configuration is limited; process validation with cavity-pressure transducers and short-shot studies is required before tool release.
Molten HDPE 99416 is not thermally indefinite. In valve-gate and open hot-runner manifolds, the high melt-flow index reduces pressure drop, but any dead zone can retain material for several cycles. At manifold temperatures of 230 °C to 240 °C, a melt-residence time of 10 min to 15 min is generally considered the upper practical limit before measurable discoloration or molecular-weight shift occurs. A change in melt mass-flow rate of more than 10% from the as-received value under ASTM D1238 indicates degradation. Spiral flow and fill-balance tests should be repeated after 30 min of hot residence to detect viscosity drift. Hot-runner channels should be sized so that shear rates remain below the shear-rate threshold specified by the hot-runner supplier.
Because HDPE is non-hygroscopic, drying is not automatically required. If pellets are transferred from cold storage to a warm, humid processing floor, surface condensation may form. When pellet surface moisture exceeds 0.1 wt%, pre-drying at 70 °C for 2 h in a circulating-air hopper dryer is sufficient. Drying temperatures above 90 °C should be avoided because pellet softening and bridging can occur. These limits matter most in central conveying systems that combine regrind with virgin material; regrind fraction above 30 wt% may reduce bulk density and alter feed stability unless a consistent blend is maintained.
| Property | Method | Value |
|---|---|---|
| Melt mass-flow rate | ASTM D1238, 190 °C/2.16 kg | 40 g/10 min |
| Density | ASTM D1505 | 0.953 g/cm³ |
| Tensile yield strength | ASTM D638 Type IV, 50 mm/min | 26 MPa |
| Flexural modulus, 2% secant | ISO 178 | 1,380 MPa |
| Shore D hardness | ISO 868 | 66 |
| Vicat softening temperature | ISO 306/A50 | 124 °C |
Solid-state properties depend on density and cooling rate. The 0.953 g/cm³ density produces a stiff part; tensile yield strength is measured according to ASTM D638 Type IV at 50 mm/min and is typically reported as 26 MPa. Flexural modulus under ISO 178 is typically 1,380 MPa at 2% secant strain. Notched Izod impact testing under ASTM D256 is sensitive to notch radius and molding-induced orientation; values from thin-wall parts can differ significantly from standardized 3.2 mm specimens. Environmental stress-crack resistance under ASTM D1693 is expected to be lower than that of fractional-melt HDPE grades because high melt flow is associated with a lower molecular-weight fraction. For applications involving surfactants, oils, or alcohols, chemical compatibility should be verified by testing finished parts under the service temperature and strain level, not by resin-grade comparisons alone.
Food-contact status is not inherent to the base resin; it depends on the full formulation and converting conditions. The supplier can provide a statement of compliance for the base resin under FDA 21 CFR 177.1520 for olefin polymers. European food-contact compliance is evaluated under Commission Regulation (EU) No 10/2011, where overall migration must not exceed 10 mg/dm² under the intended use condition. REACH registration obligations for polymers are generally limited because polymers are exempt under Article 2(9) of Regulation (EC) No 1907/2006, but imported monomers and additives must be registered. RoHS compliance under Directive 2011/65/EU requires certificate review for the homogeneous material; HDPE grades in this family are not formulated with restricted heavy metals or halogenated flame retardants.
| Reference | Condition | Status |
|---|---|---|
| FDA 21 CFR 177.1520 | Olefin polymers for food contact | Certification by supplier required; use in printed or multilayer structures may require additional extractive testing |
| EU 10/2011 | Plastics in food contact | Overall migration 10 mg/dm²; compliance depends on additives and conversion |
| REACH | Regulation (EC) No 1907/2006 | Polymer exempt under Article 2(9); monomer registration by supplier |
| RoHS | Directive 2011/65/EU | Requires homogeneous-material certificate; no restricted heavy metals or halogenated flame retardants are normally used |
The distinction between HDPE 99416 and lower-flow HDPE becomes visible in cavity-fill pressure and part weight. A single-digit melt-flow HDPE with a melt mass-flow rate near 8 g/10 min can generate excessive pressure drop in hot-runner channels and may not fill a 0.6 mm wall section at practical injection pressures. HDPE 99416, at 40 g/10 min, enters the cavity with lower pressure loss and can fill thinner sections at lower melt temperature, but the same molecular-weight character reduces melt strength and makes the resin unsuitable for extrusion blow molding or pipe extrusion where sag resistance and long-term hydrostatic strength are required. Compared with a high-density HDPE of 0.960 g/cm³, HDPE 99416 may exhibit slightly lower hardness and stiffness, but its density-dependent shrinkage and warpage behavior are closer to other 0.953 g/cm³ injection-molding grades than to fractional-melt blow-molding resins.
When compared with isotactic polypropylene of similar melt flow, HDPE 99416 has lower heat deflection temperature and lower modulus, but better impact behavior at sub-ambient temperatures because the glass-transition temperature of HDPE is below -100 °C. It also has a lower mold shrinkage range, typically 0.015 mm/mm to 0.035 mm/mm under ASTM D955, depending on wall thickness and packing. Shrinkage anisotropy is a processing variable rather than a fixed material constant; in thin-wall containers, flow-induced orientation can produce higher shrinkage in the flow direction than in the transverse direction. Mold designers should plan for this anisotropy by measuring shrinkage on prototype cavities and adjusting the cavity dimensions accordingly.
Thin-wall packaging applications with wall sections from 0.5 mm to 1.2 mm represent the core use envelope. In accumulator-assisted injection molding machines running 100 mm/s to 250 mm/s fill speeds, the resin can fill multi-cavity tools at mold temperatures of 10 °C to 30 °C. Mold temperatures below 10 °C can cause condensation and surface defects on high-humidity production floors; mold temperatures above 40 °C may extend cycle time without equivalent improvement in part flatness. For ultraviolet-exposed outdoor service, a UV-stabilized variant or post-molding stabilization is required; the base resin alone should not be specified for long-term exterior weathering under ISO 4892-2 without testing.