Chevron Phillips Chemical Hdpe Hmn 6060uv

Chevron Phillips Chemical HDPE HMN 6060UV

    • Product Name: Chevron Phillips Chemical HDPE HMN 6060UV
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 600713
    Density 0.960 g/cm3
    Meltindex 0.60 g/10 min (190°C/2.16 kg)
    Uvstabilization Yes
    Tensilestrengthatyield 26 MPa
    Tensilestrengthatbreak 31 MPa
    Elongationatbreak 600%
    Flexuralmodulus 1.20 GPa
    Environmentalstresscrackresistance 1000 h (F50, 10% Igepal)
    Vicatsofteningpoint 121 °C
    Brittlenesstemperature < -70 °C
    Hardnessshored 66
    Thermalconductivity 0.45 W/m·K
    Coefficientoflinearthermalexpansion 1.2E-4 cm/cm/°C
    Waterabsorption <0.01%
    Dielectricstrength 18 kV/mm
    Volumeresistivity >1E15 ohm·cm
    Processingtemperature 180-220 °C
    Bulkdensity 0.58 g/cm3
    Form Pellets

    As an accredited Chevron Phillips Chemical HDPE HMN 6060UV factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Chevron Phillips Chemical HDPE HMN 6060UV packaging: 25 kg polyethylene bags, 1,000 kg bulk bags, and bulk truck/railcar shipments.
    Container Loading (20′ FCL) 20′ FCL container loaded with palletized 25 kg bags of Chevron Phillips HDPE HMN 6060UV, securely stowed and sealed.
    Shipping Chevron Phillips Chemical HDPE HMN 6060UV is typically shipped as solid polyethylene pellets in 25 kg bags, bulk boxes, or bulk trucks/railcars. Packages are palletized, stretch-wrapped, and labeled. Transport in clean, dry vehicles away from moisture, heat, and contamination. Generally non-hazardous under DOT/IMDG/IATA; follow standard handling and storage guidelines.
    Storage Store Chevron Phillips Chemical HDPE HMN 6060UV in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, flames, and oxidizing agents. Keep original containers or bags tightly sealed and pallets stable. Avoid moisture, dust, and contamination. Maintain ambient temperatures, protect from physical damage, and follow supplier SDS, local regulations, and first-in, first-out stock rotation. Do not stack excessively.
    Shelf Life Store dry, covered, below 50°C; Chevron Phillips Chemical HDPE HMN 6060UV has a two-year shelf life from date of manufacture.
    Application of Chevron Phillips Chemical HDPE HMN 6060UV

    Injection molding of HMN 6060UV into 10 L, 20 L, and 25 L open-head pails is governed less by melt flow than by the need to maintain uniform sidewall thickness across a deep-draw core. The resin, a hexene-copolymer HDPE with a nominal melt flow rate of 6.0 g/10 min at 190 °C/2.16 kg per ASTM D1238 and ISO 1133-1:2022, and density of 0.960 g/cm³ per ASTM D1505, is processed neat in single-cavity tools with hot runner systems and a single edge gate located near the base chime. For a straight-sided 20 L pail with nominal wall thickness 1.8–2.2 mm, a two-platen hydraulic machine requires clamp force between 4,500 kN and 6,000 kN; smaller 5 L pails can be molded on 1,500–2,200 kN machines. The barrel profile is typically held at 200–230 °C from feed to nozzle, the mold temperature at 15–35 °C, and the cushion at 3–6 mm. Hold pressure in the range 50–70 MPa is maintained for 8–12 s after fill, because delayed pack transfer produces sink marks around handle bosses and lid-sealing surfaces. The reciprocating screw should have a compression ratio of 2.5:1–3.0:1 and a non-return valve checked daily for wear; cycle times for 20 L pails on two-platen machines are generally 40–60 s, depending on core cooling configuration.

    UN certification for dangerous-goods pails is tested under 49 CFR 178.603 for drop impact, 49 CFR 178.604 for leakproofness, and 49 CFR 178.606 for stacking. Packing Group II liquids require drop qualification from 1.2 m after conditioning at -18 °C for 24 h. Food-contact use falls under FDA 21 CFR 177.1520 olefin polymer provisions, while EU food contact requires compliance with Regulation (EU) No 10/2011. Formulation remains close to neat resin: color masterbatch addition is 1.0–2.5 wt% of a PE carrier, post-industrial regrind from the same tool family is limited to 15 wt% in UN-certified packagings unless re-qualification is performed, and mineral filler above 5 wt% is not recommended because it degrades environmental stress crack resistance and low-temperature drop survival. Neat HMN 6060UV does not require pre-drying when stored below 60% RH; if regrind or color masterbatch moisture exceeds 0.05 wt%, drying at 80 °C for 2 h is necessary to prevent splay. Terminal products are 5 L, 10 L, 20 L, and 25 L open-top pails with tamper-evident lids used for lubricant additives, agricultural surfactants, water-based coatings, detergents, and edible oil fractions.

    TestStandard referenceQualification condition
    Drop impact, Packing Group II49 CFR 178.6031.2 m after -18 °C for 24 h
    Leakproofness49 CFR 178.604Internal air pressure 20 kPa for 5 min
    Stacking49 CFR 178.60640 °C for 28 days under calculated static load
    Environmental stress crack resistanceASTM D1693 Condition BNo cracking below 100 h for chemical compatibility evidence

    What Limits Post-Consumer Recyclate Loading in Outdoor Agricultural Crates?

    Post-consumer recyclate addition to HMN 6060UV in outdoor agricultural crates is constrained by low-temperature impact retention and UV stabilizer dilution rather than by melt-processing window. With a base melt flow rate of 6.0 g/10 min, the resin accommodates 10–25 wt% washed PE PCR in a typical 600 mm × 400 mm ventilation crate; above 25 wt%, notched Izod performance at -20 °C under ASTM D256 becomes batch-dependent and must be qualified crate-by-crate. The compounding approach for a ventilated harvest bin is therefore close to 80–90 wt% HMN 6060UV, 10–20 wt% washed PE PCR, and 0–2.0 wt% PE-based HALS masterbatch when the end-use is outdoor service beyond 24 months in high-UV regions. If non-black coloration is required in a dairy or aquaculture tray, the secondary UV/HALS masterbatch is normally raised to 1.5–2.5 wt% because dark colorants alone cannot substitute for light-stabilizer concentration.

    Compliance for dry food contact harvest crates is based on Regulation (EU) No 10/2011, with total migration below 10 mg/dm² for dry food simulants; reusable transport packaging also falls under ISO 18601:2013 reuse and recovery protocols. Outdoor weatherability is qualified by ISO 4892-2 exposure with a defined color-change limit, typically ΔE < 3.0 after 1,000 h for black or dark green crates. Injection molding of a 60 L crate uses sequential valve gating on a hot runner; clamp force ranges from 5,000 kN to 8,000 kN, melt temperature is held between 210 °C and 240 °C, and mold temperature remains at 10–30 °C. A two-stage packing profile of 55–65 MPa for 3–5 s followed by 30–40 MPa for 4–8 s reduces warpage at the side-wall rib intersections. Terminal products include citrus picking bins, ventilated potato and onion crates, vineyard grape totes, mushroom harvest boxes, and aquaculture grow-out trays.

    Closure Tear-Off Bands, Torque Retention, and Flexural Fatigue Testing

    In high-cavitation closure tools, the production of tamper-evident screw closures from HMN 6060UV places the resin's narrow molecular weight distribution under short cycle-time conditions where consistent tamper-band break and cap removal torque determine fill-line performance. For a 28 mm PCO 1881 beverage closure weighing approximately 2.8 g, a 64-cavity or 96-cavity hot-runner mold operates with melt temperature 210–230 °C, mold temperature 10–20 °C, injection time 0.3–0.6 s, and total cycle time 4.5–7.5 s on high-speed accumulator machines. Slip performance is adjusted with a PE-carrier erucamide masterbatch at 0.1–0.5 wt%, which must be allowed to bloom at the cap surface for 24–48 h before torque testing. Color concentrate for non-white closures is charged at 1.0–3.0 wt%; post-industrial regrind is limited to 10 wt% and is typically excluded from food-contact closures unless regulatory approval covers the specific source.

    Regulatory compliance for beverage and food closures is anchored to FDA 21 CFR 177.1520 and Regulation (EU) No 10/2011, with organoleptic testing per EN 1622:2006. Child-resistant agrochemical closures require ISO 8317 panel testing; tamper-evident band separation torque is typically specified in the range 0.6–1.2 N·m and cap removal torque at 1.0–2.0 N·m for 28 mm formats. Slitting of the tamper-evident band is performed immediately after ejection to avoid post-crystallization stress at the slit line, and in-line checkweighers verify cap mass variation below 0.05 g. Terminal products include 28 mm mineral water closures, 38 mm dairy and juice closures, 38 mm/45 mm agrochemical closures, and child-resistant caps for household chemicals.

    If Underhood Fluid Reservoirs Replace PA66 or PP-GF

    If HMN 6060UV is considered for underhood fluid reservoirs as a lower-density alternative to glass-filled PP or PA66, the design review must separate atmospheric overflow containers from pressurised coolant loops. HDPE is acceptable for non-pressurised windshield washer reservoirs, headlamp washer tanks, and coolant expansion bottles operating below 105 °C; it is not appropriate for pressurised coolant degassing circuits where continuous hot glycol-water contact above 120 °C produces creep and weld-line stress cracking. Formulation is typically 100 wt% HMN 6060UV for translucent reservoir halves, or 97–98 wt% HMN 6060UV with 2–3 wt% carbon black masterbatch where a dark interior is specified. No plasticizer, impact modifier, or filler is required for standard atmospheric reservoir designs.

    Compliance is verified through FMVSS 302 or ISO 3795 flammability, ISO 175 immersion testing in 50% aqueous ethylene glycol at 90 °C for 168 h, and pressure-decay leak testing for welded shells. The downstream process is two-shell injection molding followed by hot-plate welding: platen temperature 210–240 °C, welding pressure 0.15–0.30 MPa, and weld time 12–25 s for a 3 mm nominal wall. Residual moisture from post-weld cooling or regrind must be kept below 0.05 wt% before injection to avoid splay at the weld bead. Published data for HMN 6060UV in extended hot coolant immersion is limited; each reservoir design must be validated on the actual welded assembly under thermal cycling. Terminal products are windshield washer reservoirs, headlamp cleaning tanks, rear washer reservoirs, and atmospheric coolant expansion bottles.

    Meter Enclosures Demand UV Resistance Without UL Yellow Card Contradiction

    Outdoor utility enclosures made from HMN 6060UV require simultaneous demonstration of UL 94 HB at final wall thickness and long-term UV retention, because a resin yellow card may not cover the end-product wall thickness, color, or regrind level. Molding a 600 mm × 400 mm × 150 mm irrigation valve box or a cable junction enclosure requires a hot-runner tool with conformal cooling channels to maintain flatness across the sealing flange; melt temperature is kept at 200–220 °C, mold temperature at 15–25 °C, and two-stage packing at 50–70 MPa for 6–10 s reduces corner warpage. Formulation for non-black enclosures uses 97.0–98.5 wt% HMN 6060UV and 1.5–2.5 wt% UV/HALS masterbatch; black enclosures use 2–4 wt% carbon black masterbatch, which provides the highest resistance to photo-oxidative surface chalking.

    Compliance is documented by ASTM D256 notched impact at -20 °C for buried service, ISO 4892-2 or ASTM G154 weatherability testing to 1,500 h, and IEC 62262 impact classes for enclosures installed in vehicle-traffic zones. Drainage valve boxes and meter pits are tested for top-load strength under EN 124 load classes where pedestrian or light-vehicle loading applies. Terminal products are irrigation valve boxes, meter pits, telecom splice vaults, low-voltage cable junction enclosures, and gas-service riser guards.

    Regulated toys and outdoor leisure articles represent a downstream segment where HMN 6060UV is processed at lower melt temperatures than packaging applications because large flat shell components must satisfy extractable-element limits without sink marks at gate areas. Under EN 71-3:2019, migration of aluminium, boron, chromium, and zinc from the compounded article is quantified with 0.07 mol/L hydrochloric acid at 37 °C for 2 h; under ASTM F963-23, extractable elements are measured according to the specified substrate and solubility limits. Formulation uses HMN 6060UV as the sole polymeric binder at 97–99 wt%, with a cadmium-free, heavy-metal-free PE color masterbatch at 1–3 wt%; post-industrial regrind from the same material family is permitted up to 10 wt% in non-load-bearing components where full traceability under ISO 9001:2015 is maintained. Processing follows thin-wall injection molding with melt temperature 190–220 °C, mold temperature 15–30 °C, and fast injection velocities to avoid hesitation lines in large flat panels. Tools for playground shell components require clamp force between 2,500 kN and 4,500 kN, and parting-line venting must be adequate because HDPE volumetric shrinkage can trap air at the end of fill. Terminal products include sandbox shells, outdoor play panels, pool-side equipment housings, snow slider shells, and garden toy wheel components.

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    Certification & Compliance
    More Introduction

    Chevron Phillips Chemical HDPE HMN 6060UV is a UV-stabilized high-density polyethylene supplied in pellet form; the grade carries a nominal density of 0.960 g/cm³ under ASTM D1505-18 and a conventional melt flow index of 6.0 g/10 min under ASTM D1238-23 at 190 °C/2.16 kg. These values place the product in the injection-molding viscosity class rather than in the high-load melt index family used for large-part extrusion blow molding. It is specified for rigid, non-food-contact parts that require resistance to ultraviolet exposure during outdoor storage or transport; typical part geometries include industrial totes, agricultural containers, material-handling trays, and outdoor furniture components.

    The product designation includes a UV suffix indicating a light-stabilizer system not present in the corresponding unmodified grade. Because the additive formulation is proprietary, weather-related performance should be qualified using a molded plaque protocol rather than inferred from base-polyethylene data. The grade is not a crosslinkable material, and it is not formulated for rotational molding or film extrusion.

    Material specification boundaries and ASTM D4976 compliance data

    The values in the following table are representative datasheet values, not contractual release limits. Batch certificates of analysis should control lot acceptance.

    ParameterMethodRepresentative value
    Melt flow indexASTM D1238-236.0 g/10 min
    DensityASTM D1505-180.960 g/cm³
    Tensile yield strengthASTM D638-1426 MPa
    Elongation at breakASTM D638-14>600%
    Flexural modulusASTM D790-171,380 MPa

    ASTM D4976-23 is used as a classification framework for high-density polyethylene; it does not replace weathering, environmental stress crack resistance, or lot-specific mechanical testing. Compliance with this grade’s density and melt flow specification does not guarantee outdoor life, because molecular architecture, additive concentration, and processing history are not captured by cell classification alone.

    What limits outdoor service life in UV-stabilized HDPE components?

    Ultraviolet exposure initiates free-radical photo-oxidation in polyethylene by abstracting hydrogen from the polymer chain, producing hydroperoxides that decompose to carbonyl and hydroxyl species. The stabilizer system in HMN 6060UV interrupts this cycle, but it cannot eliminate the effects of thermal history, part thickness, or surface stress. A more reliable failure index than gloss loss is retention of tensile elongation at break under ASTM D638-14 combined with carbonyl index measured by infrared spectroscopy under ASTM D5576.

    Accelerated weathering per ASTM G154 or ISO 4892-2 is used for comparative screening. Published multi-year natural weathering data for this exact grade is limited; therefore, qualification programs should include a non-UV-stabilized HDPE control of equivalent melt flow and density. Time to 50% elongation retention is useful only when irradiance, black-panel temperature, and chamber moisture are reported. Parts with wall sections below 2 mm may embrittle earlier than thicker plaques due to the shorter oxygen-diffusion path and the higher surface-to-volume ratio.

    For injection molding, the flow behavior of a 6.0 g/10 min high-density polyethylene permits moderate fill velocities and short holding-pressure times. Published machine-specific parameters for HMN 6060UV are limited, so the following starting window is derived from general HDPE injection-molding practice at 0.960 g/cm³ density. Initial trials should bracket the lower barrel temperatures to minimize gate blush and the upper temperatures to deal with thin-wall filling; a melt-temperature probe should record actual temperature rather than the barrel set point.

    Zone or parameterStarting rangeEquipment note
    Feed throat40–60 °Cwater-cooled feed throat
    Rear zone180–200 °Cgeneral-purpose screw
    Middle zone200–220 °Creduce for thick sections
    Front zone215–230 °Cmelt-temperature verification required
    Nozzle220–230 °Cdecompression after screw recovery
    Mold temperature15–40 °Clower for cycle, higher for weld-line appearance
    Fill pressure70–120 MPahydraulic or electric injection unit
    Holding pressure50–70% of fill pressuregate-seal monitoring required
    Back pressure0.3–0.7 MPauniform melt density
    Screw recovery speed40–80 min⁻¹avoid excessive shear heating
    Cushion3–8 mmconsistent transfer point

    The material does not normally require desiccant drying when resin is stored in dry conditions. If surface condensation occurs at ambient relative humidity above 60%, pellets should be dried at 80 °C for 1 h to 2 h in a dehumidifying or convection hopper dryer. Residence time at melt temperatures above 230 °C should be kept below 5 min to minimize chain scission, yellowing, and loss of impact strength. On cold-runner tools, molders should check the gate freeze point because HDPE of this density solidifies rapidly; a cushion above 3 mm and holding-pressure time determined by gate-seal measurement reduce sink marks in thick bosses.

    When lower-density or non-UV-stabilized HDPE is substituted for HMN 6060UV

    Substituting a 0.952 g/cm³ HDPE of similar melt flow index reduces flexural modulus and tensile yield strength, which can increase deflection in load-bearing ribs and snap-fit geometries. A flexural modulus difference of 200 MPa to 300 MPa is observable in constant-load creep and top-load tests. The higher density of HMN 6060UV contributes to lower permeation and higher top-load strength for rigid containers.

    Substituting a non-UV-stabilized HDPE does not significantly alter short-term melt processing, but it changes the failure mode after outdoor exposure from ductile drawing to brittle fracture. The time to 50% tensile elongation retention under ASTM G154 is typically shorter for unstabilized grades; an exact multiplier cannot be stated without lot-specific exposure data. For indoor-only parts, the substitution may be technically acceptable, but any incidental sunlight exposure in loading docks or open storage should trigger requalification.

    Compared with extrusion blow-molding HDPE grades that use a high-load melt index near 6.0 g/10 min under 21.6 kg, HMN 6060UV has much lower melt strength because its melt flow index is measured under 2.16 kg. This is a fundamental difference: the grade fills injection molds easily but cannot maintain parison stability in large blow-molded containers.

    Chemical resistance follows the general behavior of high-density polyethylene: aliphatic hydrocarbons, dilute acids, and aqueous salt solutions are absorbed or tolerated with minimal property loss, while strong oxidizing acids, chlorinated solvents, and some surfactants reduce molecular weight or promote environmental stress cracking. For containers holding agricultural or industrial liquids, the specific chemical mixture rather than the polyethylene grade is often the controlling variable; ASTM D1693 bent-strip ESCR testing using 10% Igepal CO-630 or 100% Igepal CO-630 at 50 °C is recommended when comparing lots or alternative grades. Published ESCR values for this specific grade may be available only from the manufacturer’s certificate of analysis; a minimum F50 value should not be inferred from density alone.

    Regulatory inquiries should be directed to the supplier’s current compliance documentation. HDPE base resins of this type are generally assessed against FDA 21 CFR 177.1520 for olefin polymers and against REACH substance registration obligations, but the UV stabilizer package must be cleared in the final additive statement. RoHS Directive 2011/65/EU restriction thresholds are typically met by polyolefins of this class; nevertheless, a grade-specific analytical report should be requested when documenting lead, cadmium, mercury, hexavalent chromium, PBB, and PBDE content below the directive’s maximum concentration values.

    High-cavitation tooling responds to lot-to-lot rheology variation

    Polyethylene polymerization and pelletizing introduce measurable lot-to-lot variation even when the grade remains within its release limits. A melt flow index shift from 5.5 g/10 min to 6.5 g/10 min can alter fill pressure and pack time on a high-cavitation tool. Injection molders should monitor cushion position, peak hydraulic pressure, and part weight at a fixed transfer position; a change in part weight exceeding 0.5% at constant settings is a practical signal that the resin lot or barrel condition has drifted. This is not unique to HMN 6060UV, but the UV additive package can contribute to slight viscosity shifts if concentrated masterbatch dispersion is incomplete.

    Twin-screw compounding is not required for this grade because the stabilizer is incorporated during pelletization; however, if converters add color concentrate at the press, a metering accuracy of ±0.2 wt% and a screw with adequate distributive mixing are recommended. Poor dispersion of color concentrate or UV masterbatch can cause surface streaks and localized loss of weather resistance. In high-speed injection presses with clamp force below 80 t, filling thin-walled containers may require melt temperatures near 230 °C; under these conditions, the stabilizer package should be protected by limiting barrel residence time rather than by lowering screw recovery speed below the point of excessive shear heating.

    In rigid industrial packaging, HMN 6060UV is used where the part must survive ultraviolet exposure in open yards or on flatbed trailers. Typical failure modes reported are not softening or gross warpage but surface embrittlement, chalking, and cracking at molded-in stress concentrations such as sharp corners, gate vestiges, and ejector marks. Corrective actions include radius increases above 0.5 mm at high-stress corners, gate location shifts to reduce elongational flow patterns, and use of textured surfaces to disguise the early stages of photo-oxidative chalking.

    For outdoor furniture and agricultural containers, long-term performance depends more on part design and weathering protocol than on resin density alone. The specified UV stabilization package in HMN 6060UV permits processing at standard HDPE melt temperatures without demanding the elevated temperatures that can accelerate degradation in unstabilized grades. Published multi-year field data for this exact grade is limited; validation programs should therefore combine accelerated weathering, mechanical property retention, and stress-crack resistance rather than relying on a single data sheet value.

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