Chevron Phillips Chemical Hdpe C513uv

Chevron Phillips Chemical HDPE C513UV

    • Product Name: Chevron Phillips Chemical HDPE C513UV
    • Factroy Site: Yinchuan, Ningxia, China
    • Price Inquiry: sales8@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 281995
    Polymer Type High Density Polyethylene (HDPE)
    Density 0.951 g/cm3
    Melt Index 190 C 2 16 Kg 0.35 g/10 min
    Melting Point 130 °C
    Vicat Softening Temperature 121 °C
    Tensile Strength At Yield 26 MPa
    Tensile Elongation At Break >600%
    Flexural Modulus 1.24 GPa
    Hardness Shore D 65
    Environmental Stress Crack Resistance Escr >1000 h
    Brittleness Temperature <-70 °C
    Uv Stabilization Yes
    Form Pellets

    As an accredited Chevron Phillips Chemical HDPE C513UV 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 C513UV is typically packaged in sealed 25 kg (55 lb) polyethylene bags, palletized for industrial shipment.
    Container Loading (20′ FCL) Chevron Phillips Chemical HDPE C513UV, 25 MT in 25 kg bags, floor-loaded and secured in a 20′ FCL for export.
    Shipping Chevron Phillips Chemical HDPE C513UV is a non-hazardous high-density polyethylene resin. Ship in sealed 25-kg bags, bulk bags, or bulk trucks/railcars. Not regulated by DOT, IMDG, or IATA; no UN number, hazard class, or labels required. Store cool, dry, and away from prolonged UV exposure.
    Storage Store Chevron Phillips Chemical HDPE C513UV in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep material in original, sealed packaging on pallets, off the ground and away from moisture, dust, and contaminants. Avoid prolonged UV exposure and temperature extremes. Maintain good housekeeping to prevent pellet spills and slipping hazards. Follow SDS.
    Shelf Life Chevron Phillips HDPE C513UV shelf life is not established; stable under normal storage conditions; protect from heat, sunlight, and moisture.
    Application of Chevron Phillips Chemical HDPE C513UV

    Thin-wall outdoor storage totes molded from C513UV present a narrow processing window that is controlled more by additive retention than by melt fill. The grade is characterized by a nominal melt flow rate of 18 g/10 min under ASTM D1238 at 190 °C/2.16 kg and a density near 0.953 g/cm³, which places it in the high-flow HDPE injection molding class. In totes with wall thickness between 1.2 mm and 2.5 mm, reciprocating-screw injection molding machines with screw L/D ratios of 20:1 to 25:1 and compression ratios from 2.5:1 to 3:1 are used. Nozzle melt temperature is typically held at 210–235 °C, while mold coolant temperature is maintained at 10–30 °C. Lower mold temperatures reduce cycle time but increase flow hesitation at latch bosses and hinge anchors. Because C513UV carries a hindered amine light stabilizer system, cumulative barrel residence time above 240 °C should not exceed 5 min to avoid additive depletion and progressive yellowing. Hot-runner manifolds serving stackable tote lids and bodies are preferably set no higher than 230 °C, and valve-gate tips with 0.8–1.2 mm orifices reduce gate blush and shear-induced streaking.

    Shrinkage in these thin-wall sections generally falls between 1.4% and 1.8% in the flow direction and 1.6% to 2.0% transverse when measured per ASTM D955. Rib-to-wall ratios are kept at 0.5:1 to 0.6:1 to prevent sink marks around latching features. Pack pressure is set at 50–70% of injection pressure, with hold time continued until gate freeze as confirmed by part-weight stabilization. Lid bowing is controlled through balanced cooling circuits and thermal pin placement rather than by increasing mold temperature alone. Outdoor validation for these parts typically includes xenon-arc weathering under ISO 4892-2 cycle 1 at 0.35 W/m² at 340 nm and instrumented impact testing per ISO 179-1/1eA after 500–1000 h accelerated exposure. Retained tensile elongation measured according to ISO 527-2 is the preferred degradation indicator because it declines earlier than visible gloss or colour shift. Colourants used in outdoor totes are screened against REACH and RoHS heavy-metal limits, and sulphur-rich industrial atmospheres require specific validation because acid deposition can accelerate surface oxidation of unstabilized regrind layers.

    Why Does UV Stabilizer Concentration Influence Mould Shrinkage in Nursery Containers?

    Nursery pots, propagation trays, and hanging-basket hooks are injection molded from C513UV at wall thicknesses from 0.9 mm to 1.5 mm. The high melt flow allows filling of drainage-slot arrays without excessively high clamp force, but the thin sections amplify the effect of pigment and stabilizer concentration on solidification behaviour. When carbon black masterbatch is added at 1.5–3.0 wt% to meet outdoor opacity requirements, mould shrinkage can decrease by up to 0.2 percentage points because carbon black increases nucleation density and alters crystallite growth. Moulders compensate by adjusting hold pressure rather than raising melt temperature; raising melt temperature above 220 °C frequently produces slot-edge tearing during ejection. Drainage slots are preferably oriented parallel to the flow direction. Perpendicular slot arrays become stress concentrators during high-speed demolding and can generate micro-cracks that widen after prolonged UV exposure.

    Although C513UV is supplied as a UV-stabilized grade, additional UV masterbatch is occasionally introduced for desert-climate programs. Letdown ratios above 1 wt% are uncommon because the base resin already contains a stabilizing package, and overdosing can reduce tensile impact strength while causing deposit formation on hot-runner gate tips. The final product is a rigid horticultural container that must tolerate fertilizer salts, wet soil, and direct sunlight without brittle fragmentation. For export markets, compliance documentation typically includes REACH SVHC declarations and California Proposition 65 screening, particularly for carbon black and coloured concentrates. Published data for this specific formulation configuration are limited; each masterbatch type must therefore be validated by weathering trials rather than relying on generic HDPE additive compatibility statements. Shrinkage verification is performed using ISO 294-4, and retained impact strength after weathering is measured with ISO 179-1/1eU because unnotched specimens are more sensitive to surface embrittlement than notched bars.

    When High-Cavitation Closure Tools Demand Low Drool and Rapid Solidification

    High-cavitation closure tools processing C513UV require shut-off nozzles or valve-gated hot runners to manage drool. In 32–96 cavity molds producing tamper-evident caps with wall thickness as low as 0.8 mm, the melt flow rate of 18 g/10 min permits rapid cavity filling at nozzle temperatures between 220 °C and 240 °C. Mold temperature is normally held at 10–20 °C, but rapid cooling combined with the 0.953 g/cm³ density can increase bridge breakage if the tamper-evident band hinge has a sharp corner. The hinge radius should be at least 0.4 mm, and the gate position should be arranged so that the weld line does not cross the bridge. Rear barrel zones are set to 180–200 °C to reduce premature melt film and drool at the nozzle seat.

    Torque retention after simulated distribution is measured per ASTM D2063. Caps molded from C513UV are conditioned at 23 °C and 50% RH for 48 h before torque testing. For detergent and agrochemical closures, environmental stress cracking resistance is screened according to ASTM D1693 Condition A in 10% Igepal CO-630 at 50 °C. Brittle creep failure in the cap skirt is the primary rejection mode when moulders apply excessive hold pressure to eliminate sink in the top panel. Production-scale observation shows that hold pressure beyond the level required for gate freeze increases moulded-in stress around the tamper-evident bridges and reduces torque retention after drop cycling. The closure is therefore designed with a top panel thickness near 1.0–1.2 mm and a skirt thickness near 0.8–1.0 mm to balance sealing force and removal torque without overdosing pigment masterbatch above 2 wt%.

    Ventilated Dairy Crates: Weld-Line Strength and Alkaline Cleaning Fatigue

    Ventilated dairy crates and bread trays are thick-section parts with wall thicknesses from 3 mm to 6 mm, heavy ribs, and open grid structures. Processing C513UV in these tools requires a different filling strategy than conventional low-flow HDPE. Injection speed is reduced to avoid jetting in the open grid. Nozzle melt temperature can be kept at 220–250 °C, while back pressure is set at 0.5–1.0 MPa hydraulic to homogenize the melt without excessive shear heating. Because thick sections retain heat, cooling time becomes the cycle-time driver. Mold temperature of 10–20 °C shortens cooling but may cause differential shrinkage between thick ribs and thin grid bars. Differential shrinkage above 0.5% between adjoining wall nodes produces visible sink marks and crate wall bow. Hold pressure is applied in a stepped profile: an initial pack at 60–80% of injection pressure for 2–4 s, followed by a lower hold until gate sealing.

    Dairy crates are repeatedly washed in alkaline detergents at 60–80 °C. Milk fat residues act as environmental stress-cracking agents on HDPE surfaces. ESCR is therefore specified under ASTM D1693 Condition B, and weld-line strength in the grid intersections is checked by falling-weight impact per ISO 6603-2. The UV stabilizer in C513UV is not a stress-crack inhibitor, so crates stored outdoors for prolonged periods may require blending with an ESCR-enhancing HDPE grade or reducing post-mould pigment masterbatch letdown to 2–3 wt%. Published data for this specific configuration are limited because stacking loads, wash-water chemistry, and crate geometry dominate failure rates more than the base resin selection alone. Moulders should therefore perform alkaline-immersion testing for 100 h followed by compression testing per ISO 604 to verify load retention after chemical exposure.

    Open-head injection-molded pails used for agricultural adjuvant concentrates require simultaneous UV resistance and chemical compatibility. C513UV is run in tools with wall thickness between 1.5 mm and 2.5 mm, often with in-mold label pockets. The high-flow melt allows rapid filling of side-wall labeling ribs, but labels reduce local cooling efficiency and can cause distortion if the label adhesive migrates during melt contact. Processing melt temperature is kept at 210–230 °C, and mold temperature is set at 15–30 °C. Drop impact after filling is evaluated by a defined drop-test protocol from 1.2 m at -18 °C for products shipped in cold storage. Chemical resistance is not governed solely by resin grade; pails carrying concentrated surfactants require pre-validation by 28-day immersion in the actual formulation because the UV stabilizer package does not prevent swelling or stress cracking from polar co-solvents. For export, UN marking for dangerous goods requires closure torque retention and stack testing per ISO 2234. Published data for this specific configuration are limited, so each molded pail design is qualified independently with the intended filling formulation and closure liner.

    Because C513UV is an injection molding grade, pail wall thickness must remain uniform enough to avoid severe neck-shoulder stress concentration. Abrupt transitions greater than 1:1.5 between the rim and side wall should be avoided, or the part may crack during closure application. The screw geometry used for pail molding should have a compression ratio of 2.5:1 to 3:1 and a reverse-flow check ring to prevent short shots when high screw recovery speeds are used. Accumulator-assisted machines are preferred for thin-wall pails requiring fill times below 0.5 s per cavity, but shear heating may raise melt temperature by 5–10 °C and must be offset by reducing barrel set points.

    Marine and Recreational Components Demand Constant UV Stability and Low-Temperature Impact Resistance

    Marine and recreational components such as kayak hatch rings, outdoor game housings, and playground fittings require constant UV stability and low-temperature impact resistance. C513UV is selected for these uneven-wall tools where the primary risk is not melt fill but long-term dimensional stability. Wall thicknesses range from 2.5 mm to 6 mm. Flow paths are short, so melt temperature can be set at 200–220 °C to minimize gas trapping and warpage. Mold temperature is maintained at 20–40 °C; the higher range reduces frozen-in orientation and improves impact retention after outdoor exposure. Metal inserts are avoided where possible because differential thermal expansion between HDPE and brass or stainless steel inserts creates hoop stress and accelerates stress cracking around the boss. If inserts are unavoidable, boss outer diameters should be 2.5–3.0 times the insert diameter, and preheated inserts at 60–80 °C are recommended.

    Snap-fit arms are kept with a minimum radius of 0.8 mm at the base to avoid notch sensitivity at low temperatures. Izod impact tests per ISO 180/A at -20 °C are used for qualifying impact-modified lots. Pigment concentrates for outdoor marine parts are restricted to UV-stable inorganic and high-performance organic systems. Brominated flame retardants are not used in these non-flame-rated parts because the additives can reduce UV stability and produce acidic degradation products in coastal environments. Weld lines on hatch rings or handle attachment points must be relocated by gate design because C513UV, like most high-flow HDPE grades, shows reduced weld-line strength when weld lines form at the end of long flow paths. Moulders validate this by tensile testing welded specimens under ISO 527-2 at 5 mm/min, comparing weld-line tensile elongation to an unwelded reference, and rejecting designs with weld-line retention below 50% of parent material elongation.

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    Certification & Compliance
    More Introduction

    Chevron Phillips Chemical HDPE C513UV is an ethylene-based high-density polyethylene formulated with an ultraviolet stabilization package and supplied in pellet form for extrusion and blow molding applications that require long-term outdoor exposure resistance. The nominal density is 0.954 g/cm³ when tested under ASTM D1505, and the melt index is 0.13 g/10 min at 190°C under a 2.16 kg load per ASTM D1238. This fractional-melt classification places the material in the high-molecular-weight range; the melt viscosity is therefore higher than that of general-purpose injection molding HDPE grades, and the product is directed to sheet extrusion, profile extrusion, pipe fittings, large-part blow molding, and thermoforming. Published typical values include a tensile yield strength of 28 MPa and an elongation at break greater than 600% per ASTM D638. The flexural modulus is listed at 1380 MPa under ASTM D790, while the notched Izod impact result is reported as no break under ASTM D256. The Vicat softening temperature is approximately 124°C under ASTM D1525, and the brittleness temperature is below −75°C under ASTM D746. Environmental stress crack resistance, measured by ASTM D1693 condition B in 100% Igepal CO-630 at 50°C, is reported as greater than 1000 h. These values are nominal and do not constitute specification limits; release testing must be obtained for production lot qualification.

    The resin is used in outdoor chemical storage tanks, agricultural troughs, industrial containers, sheet for vehicle liners, and large-diameter pipe fittings where ultraviolet radiation and thermal cycling would otherwise cause surface cracking and loss of elongation. In these applications, the combination of high ESCR and UV stabilization differentiates C513UV from general-purpose HDPE grades that carry the same density but lack the same weathering package.

    What Processing Limits Are Encountered at a 0.13 g/10 min Melt Index?

    On a single-screw extruder with an L/D ratio of 24:1 to 30:1 and a barrier screw or Maddock mixing section, the fractional-melt index produces elevated head pressure and torque demand during high-output sheet or pipe runs. The same extruder running a 0.35 g/10 min general-purpose HDPE at equivalent screw speed and barrel profile generally shows lower die pressure; converting to C513UV may require reducing screw speed by 10–20% or increasing drive current monitoring until pressure limits are established. Melt temperature setpoints in the 190–220°C range are typical for high-molecular-weight HDPE extrusion, but C513UV-specific published processing data are limited. Barrel profiles must be verified with melt thermocouples and pressure transducers on the production line. Sustained melt temperatures above 240°C should be avoided because extended residence time can cause chain scission, reduce ESCR, and generate gel particles in the extrudate.

    Capillary rheometry according to ASTM D3835 is used to generate shear viscosity curves at processing temperatures. Although published C513UV flow curves are limited, fractional-melt high-density polyethylene typically exhibits pronounced shear thinning with a power-law index in the 0.3–0.5 range at shear rates between 10 s⁻¹ and 1000 s⁻¹. This shear thinning is beneficial in sheet die flow but means that small changes in screw speed can produce large changes in throughput and die pressure. Process monitoring should include melt pressure before the breaker plate, melt temperature in the adapter, and drive current; excursions beyond stable ranges often appear first as melt fracture, gauge variation, or black speck generation.

    For large-part blow molding, accumulator-head machines with screw lengths of 25:1 or higher and high-torque drives are preferred. The high melt strength of the fractional-melt resin helps control parison sag, but die gap and melt temperature must be held within narrow limits. Parison weight, die swell, and blow ratio changes should be recorded on each machine because shuttle, wheel, and accumulator systems do not share a single process window. Injection molding is generally limited to thick-walled parts with generous runners; the low melt index restricts flow length and may require higher melt temperature and injection pressure than standard HDPE grades.

    Moisture absorption of HDPE is low, typically below 0.01% at 23°C and 50% relative humidity, so pre-drying is not normally required for virgin pellets. If bulk storage has exposed resin to condensation or ambient relative humidity above 60%, surface moisture can produce splay in extruded sheet; a dehumidifying dryer set at 65–80°C for 2–4 h is sufficient to restore surface quality. Regrind levels should be limited to 20–30% by weight unless tensile and weathering retention testing confirms that the recycled fraction does not reduce ESCR.

    Typical Property Matrix and Corresponding Test Standards

    The following tabulated values are representative of published product data and are not specification limits. Lot-specific certificates of analysis control production release.

    PropertyUnitTest StandardTypical Value
    Densityg/cm³ASTM D15050.954
    Melt index, 190°C/2.16 kgg/10 minASTM D12380.13
    Tensile strength at yieldMPaASTM D63828
    Elongation at break%ASTM D638>600
    Flexural modulusMPaASTM D7901380
    Notched Izod impact—ASTM D256No break
    Vicat softening temperature°CASTM D1525124
    Brittleness temperature°CASTM D746< −75
    ESCR, Condition B, 100% IgepalhASTM D1693>1000

    The UV stabilization in C513UV is delivered by carbon black pigmentation combined with stabilizer chemistry. The carbon black acts as a UV absorber and free-radical scavenger, limiting the depth of photo-oxidation in exposed surfaces. For black polyethylene, oxidative induction time is frequently measured by differential scanning calorimetry under ASTM D3895 or ASTM D5885; higher OIT values indicate greater resistance to thermo-oxidative degradation. Accelerated weathering comparisons are performed under ASTM G155 or ISO 4892-2, but published C513UV-specific weathering retention data are limited. Long-term outdoor performance must be validated with site-specific ultraviolet and thermal loads because no single accelerated cycle reproduces all outdoor climates.

    Surface chalking of carbon black-filled HDPE can occur after extended ultraviolet exposure, but the bulk mechanical integrity is controlled by the base resin ESCR and stabilizer retention. The black surface also heats more rapidly under infrared thermoforming heaters; heater bank adjustment is discussed below.

    When C513UV Replaces an Unstabilized Fractional-Melt HDPE in Outdoor Fabrications

    The substitution of C513UV for a non-UV-stabilized HDPE with the same 0.954 g/cm³ density and 0.13 g/10 min melt index does not require a fundamental tooling redesign. However, the carbon black pigmentation alters infrared absorption during sheet thermoforming. Black sheet reaches surface temperature more quickly under infrared heating, and heater bank settings may need to be reduced by 5–10% relative to unpigmented or lightly pigmented sheet. Thickness distribution should be rechecked with a grid-marked test sheet because the black pigmentation reduces radiation penetration depth and changes the through-thickness temperature profile.

    Compared with a general-purpose HDPE with a melt index near 0.35 g/10 min, C513UV exhibits lower melt flow and higher melt strength. That difference improves parison sag resistance in blow molding but raises extrusion backpressure and limits thin-wall injection molding. In rotational molding, fractional-melt HDPE generally requires higher peak internal air temperature and longer oven cycle; C513UV is not the first choice for rotomolding unless the end use requires the specific UV stabilization package. Published data for this specific configuration are limited, and processing trials should be conducted on the target machine.

    The base resin C513, where offered without the UV stabilization package, may share the density and melt-flow profile of C513UV but lacks the outdoor weathering package. In indoor industrial parts, C513 may be sufficient; for outdoor tanks, agricultural troughs, drainage pipe fittings, and playground components, C513UV is specified to prevent rapid surface embrittlement. Selection is based not solely on initial tensile properties but on retention of elongation at break after 1000–3000 h of accelerated weathering.

    Assessing Environmental Stress Crack Resistance in Igepal CO-630 Media

    The ASTM D1693 condition B test employs a notched specimen bent in a channel and immersed in 100% Igepal CO-630 at 50°C. The reported result greater than 1000 h is not an absolute service life, but it ranks the material as highly resistant to slow crack growth relative to lower-molecular-weight HDPE grades. The mechanism depends on a high concentration of tie molecules and a broad molecular weight distribution, which redistribute stress ahead of the crack tip and reduce fibril rupture. Processing can suppress this advantage if melt temperature is too low and frozen-in orientation remains in the finished part. Conversely, melt temperatures above 240°C can reduce tie-molecule content through thermo-oxidative chain scission and lower the actual ESCR of the extruded product.

    In production-scale pipe or sheet extrusion, notch sensitivity is often checked by cutting specimens from the finished article rather than relying solely on pellet ESCR data. Weld lines, sharp corners, and notches introduced by downstream punching or machining are crack initiation sites. For outdoor tanks and fittings, butt fusion and extrusion welding procedures should be qualified by tensile and bend tests on welded specimens; however, the applicable welding standard depends on the installation code for the specific product class.

    Typical outdoor applications include agricultural chemical tanks, nursery pots, water treatment basin liners, dock fenders, and pipe fittings exposed to direct sunlight. The maximum recommended continuous service temperature depends on stress level and chemical environment; for unstressed HDPE, intermittent exposure up to 80°C may be tolerated, but continuous mechanical load reduces the allowable temperature because creep and slow crack growth accelerate.

    Chemical resistance of C513UV follows the established HDPE profile: continuous contact with aqueous acids, alkalis, and polar solvents is generally acceptable at ambient temperature, while strong oxidizing acids, aromatic hydrocarbons, and chlorinated solvents can soften or swell the polymer. Permeation rates in sheet and tank walls depend on wall thickness, temperature, and the specific chemical mixture. The resin may be evaluated for food-contact use under 21 CFR 177.1520 as an olefin polymer, but the presence of UV stabilizer and carbon black requires end-article compliance verification. Potable water contact requires finished-article certification; NSF/ANSI 61 or equivalent approvals must be confirmed separately. For industrial equipment, REACH candidate-list updates and RoHS Directive 2011/65/EU apply to finished articles and supply-chain declarations.

    The product should not be exposed to extended outdoor service without confirming the specific UV package is retained through regrind and processing. If regrind is subjected to multiple heat histories, stabilizer consumption increases and ESCR retention may decline; therefore, regrind fractions and re-extrusion conditions should be controlled through lot testing rather than fixed percentages alone.

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